series 50-200 evaporator for chlorine

SERIES 50-200

EVAPORATOR

FOR CHLORINE

BOOK NO. IM 50.200AA UA ISSUE B

50-200 EVAPORATOR FOR CHLORINE

EQUIPMENT SERIAL NO. _________________

DATE OF START-UP _____________________

START-UP BY ___________________________

Prompt service available from nationwide authorized service contractors.

ORDERING INFORMATION

In order for us to fill your order immediately and correctly, please order material by description and part number, as shown in this book. Also, please specify the serial number of the equipment on which the parts will be installed.

WARRANTY

Seller warrants for a period of one year after shipment that the equipment or material of its manufacture is free from defects in workmanship and materials. Corrosion or other decomposition by chemical action is specifically excluded as a defect covered hereunder, except this exclusion shall not apply to chlorination equipment. Seller does not warrant (a) damage caused by use of the items for purposes other than those for which they were designed, (b) damage caused by unauthorized attachments or modifications, (c) products subject to any abuse, misuse, negligence or accident, (d) products where parts not made, supplied, or approved by Seller are used and in the sole judgement of the Seller such use affects the products’ performance, stability or reliability, and (e) products that have been altered or repaired in a manner in which, in the sole judgement of Seller, affects the products’ performance, stability or reliability. SELLER MAKES NO OTHER WARRANTY OF

ANY KIND, AND THE FOREGOING WARRANTY IS IN LIEU OF ALL OTHER WARRANTIES, EXPRESS OR IMPLIED,

INCLUDING ANY WARRANTY OF MERCHANTABILITY OR OF FITNESS OF THE MATERIAL OR EQUIPMENT FOR

ANY PARTICULAR PURPOSE EVEN IF THAT PURPOSE IS KNOWN TO SELLER. If Buyer discovers a defect in material or workmanship, it must promptly notify Seller in writing; Seller reserves the right to require the return of such defective parts to Seller, transportation charges prepaid, to verify such defect before this warranty is applicable. In no event shall such notification be received by Seller later than 13 months after the date of shipment. No action for breach of warranty shall be brought more than 15 months after the date of shipment of the equipment or material.

LIMITATION OF BUYER’S REMEDIES. The EXCLUSIVE REMEDY for any breach of warranty is the replacement f.o.b.

shipping point of the defective part or parts of the material or equipment. Any equipment or material repaired or replaced under warranty shall carry the balance of the original warranty period, or a minimum of three months. Seller shall not be liable for any liquidated, special, incidental or consequential damages, including without limitation, loss of profits, loss of savings or revenue, loss of use of the material or equipment or any associated material or equipment, the cost of substitute material or equipment, claims of third parties, damage to property, or goodwill, whether based upon breach of warranty, breach of contract, negligence, strict tort, or any other legal theory; provided, however, that such limitation shall not apply to claims for personal injury.

Statements and instructions set forth herein are based upon the best information and practices known to U.S. Filter/Wallace

& Tiernan, Inc., but it should not be assumed that every acceptable safety procedure is contained herein. Of necessity this company cannot guarantee that actions in accordance with such statements and instructions will result in the complete elimination of hazards and it assumes no liability for accidents that may occur.

IM 50.200AA UA (B/1-01)

WALLACE & TIERNAN PRODUCTS

1901 West Garden Road, Vineland, NJ 08360

1.010-42D

INTRODUCTION


!

The USF/W&T Series 50-200 Evaporator for Chlorine described in this instruction book changes the state of chlorine from liquid to gas to supply other gaseous flow control apparatus.

The Series 50-200 Evaporator comprises a steel cylinder immersed in a hot water bath, an external heat exchanger, and associated control devices.

WARNING: HAZARDOUS GAS IS PRESENT IN THIS EQUIP-

MENT DURING NORMAL OPERATION. TO AVOID POSSIBLE

SEVERE PERSONAL INJURY OR DAMAGE TO THE EQUIP-

MENT THROUGH MISUSE, THIS EQUIPMENT SHOULD BE

INSTALLED, OPERATED, AND SERVICED ONLY BY TRAINED,

QUALIFIED PERSONNEL WHO ARE THOROUGHLY FAMIL-

IAR WITH THE ENTIRE CONTENTS OF THIS INSTRUCTION

BOOK AND THE CHLORINE HANDLING MANUAL.

This instruction book covers two versions of the evaporator: (1) standard version AAA8639 and, (2) lethal certified version AAA8651.

Both versions have identical subassembly and component parts except for the pressure cylinder. The cylinder in the “standard” version is fabricated to meet all requirements of Section VIII of the ASME Code for Unfired

Pressure Vessels. The “standard” evaporator is therefore suitable for chlorine, sulfur dioxide, or ammonia service (as labeled) in all applications. If, however, the customer requires either a “lethal certified” cylinder or a greater wall thickness for extra corrosion allowance, the “lethal rated” version is provided.

CANADIAN USERS NOTE: Canadian law requires that the owner of an evaporator have it registered with the local authorities prior to operating it, as it is a pressure vessel. The evaporator cylinder is manufactured to ASME codes and is stamped with Canadian Registration Number CRN HO 618-5 or D1429-5.

NOTE: When submitting correspondence or ordering material,always specify model and serial number of apparatus.

IM 50.200AA UA (B/1-01) Introd.


TABLE OF CONTENTS

Very Important Safety Precautions (Chlorine) ......... 1.010-40,-41

Very Important Safety Precautions ........................... SP-1,-2,-3

Regional Offices ....................................................... 1.010-1

Technical Data .......................................................... Section 1

Installation ................................................................ Section 2

Operation .................................................................. Section 3

Service ...................................................................... Section 4

Illustrations ............................................................... Section 5

Spare Parts List ......................................................... Section 6

Literature/Manuals .................................................... Section 7

Chlorine Handling Manual .................................... IM 25.000AA

IM 50.200AA UA (B/1-01) Introd. (Cont’d)


VERY IMPORTANT SAFETY PRECAUTIONS - CHLORINE

This and the following pages titled “Very Important Safety Precautions” provide, in brief, information of urgent importance relative to safety in the installation, operation, and maintenance of this equipment.

WARNING

TO AVOID POSSIBLE SEVERE PERSONAL INJURY OR EQUIPMENT DAMAGE, OBSERVE

THE FOLLOWING:

THIS EQUIPMENT SHOULD BE INSTALLED, OPERATED, AND SERVICE ONLY BY TRAINED,

QUALIFIED PERSONNEL WHO ARE THOROUGHLY FAMILIAR WITH THE ENTIRE CON-

TENTS OF THIS INSTRUCTION BOOK AND THE CHLORINE GAS HANDLING MANUAL.

CHLORINE GAS IS A RESPIRATORY IRRITANT. EXPOSURE TO CHLORINE GAS IN SUFFI-

CIENT CONCENTRATION PRODUCES IRRITATION OF THE MUCOUS MEMBRANES, THE

RESPIRATORY SYSTEM, AND THE SKIN. IN EXTREME CASES, SUFFOCATION AND DEATH

CAN OCCUR.

WHEN CHANGING CHLORINE CYLINDERS, IT IS RECOMMENDED PRACTICE TO HAVE

AN APPROVED GAS MASK AVAILABLE THAT YOU HAVE BEEN TRAINED TO USE AND

YOU MUCH BE COMPLETELY FAMILIAR WITH YOUR LOCAL PLANT OPERATING AND

EMERGENCY PROCEDURES AND CHLORINE INSTITUTE RECOMMENDED EMERGENCY

PROCEDURES.

DO NOT TOLERATE ANY CHLORINE LEAKS. CHLORINE LEAKS NEVER GET BETTER.

CHLORINE LEAKS ALWAYS GET PROGRESSIVELY WORSE IF THEY ARE NOT PROMPTLY

CORRECTED. IT IS RECOMMENDED PRACTICE TO HAVE AN APPROVED GAS MASK AVAIL-

ABLE WHEN MAKING LEAK CHECKS.

AS SOON AS THERE IS ANY INDICATION OF CHLORINE IN THE AIR, TAKE IMMEDIATE

STEPS TO CORRECT THE CONDITION.

IMPORTANT INFORMATION RELATED TO SAFETY OF CHLORINATION EQUIPMENT IN-

STALLATION IS PROVIDED IN THE CHLORINE GAS HANDLING MANUAL. IN THE INTER-

EST OF SAFE OPERATION, THIS INFORMATION MUST BE READ, UNDERSTOOD, AND

PRACTICED BY EQUIPMENT OPERATORS AND THEIR SUPERVISORS.

AT TIME OF INITIAL INSTALLATION, WHEN CHLORINE SUPPLY LINES HAVE BEEN DIS-

CONNECTED FOR ANY REASON AND ON A ROUTINE DAILY BASIS, THOROUGHLY CHECK

ALL JOINTS, CONNECTIONS, AND EQUIPMENT FOR POSSIBLE CHLORINE LEAKS AND

IMMEDIATELY CORRECT ANY THAT MAY BE FOUND.

IM 50.200AA UA (B/1-01) 1.010-40


VERY IMPORTANT SAFETY PRECAUTIONS - CHLORINE (CONT’D)

WHEN ANY CONNECTION IS BROKEN EVEN FOR A SHORT TIME, IMMEDIATELY PLUG

THE RESULTANT OPENINGS WITH A RUBBER STOPPER OR EQUIVALENT TO PREVENT

THE ENTRANCE OF MOISTURE. MOISTURE MUST BE EXCLUDED FROM ANY PART OF

THE EQUIPMENT THAT IS NORMALLY EXPOSED TO DRY CHLORINE ONLY. WHILE DRY

CHLORINE IS NON-CORROSIVE, MOIST CHLORINE IS EXTREMELY CORROSIVE TO COM-

MON METALS, SUCH AS BRASS OR STEEL.

THE TWO MOST COMMON CAUSES OF CHLORINE PIPING LEAKS ARE:

1. RE-USE OF GASKETS. THIS SHOULD NEVER BE DONE. ALWAYS HAVE AN AD-

EQUATE SUPPLY ON HAND AND ALWAYS USE NEW GASKETS OF THE CORRECT

MATERIAL AND SIZE AS IDENTIFIED ON THE EQUIPMENT PARTS DRAWING.

2. IMPROPERLY MADE-UP THREADED PIPE JOINTS. SEE CHLORINE GAS HAN-

DLING MANUAL FOR RECOMMENDED PROCEDURE.

EXCEPT IN CASES OF LEAK DETECTION OR CALIBRATION ADJUSTMENTS, THE CHLO-

RINE GAS SUPPLY MUST BE SHUT OFF AT THE GAS SUPPLY CONTAINERS AND THE CHLO-

RINE GAS IN THE SYSTEM EXHAUSTED BEFORE SERVICING THE EQUIPMENT.

USE ONLY USF/W&T LISTED PARTS, EXCEPT FOR COMMERCIALLY AVAILABLE PARTS

AS IDENTIFIED ON THE PARTS LIST. THE USE OF UNLISTED PARTS CAN RESULT IN EQUIP-

MENT MALFUNCTIONS HAVE HAZARDOUS CONSEQUENCES.

DO NOT DISCARD THIS INSTRUCTION BOOK UPON COMPLETION OF INSTALLATION.

INFORMATION PROVIDED IS ESSENTIAL TO PROPER AND SAFE OPERATION AND MAIN-

TENANCE.

ADDITIONAL OR REPLACEMENT COPIES OF THIS BOOK ARE AVAILABLE FROM:

USFILTER'S WALLACE & TIERNAN PRODUCTS

1901 WEST GARDEN ROAD

VINELAND, NEW JERSEY 08360

PHONE: (856) 507-9000

FAX: (856) 507-4125

NOTE

Minor part number changes may be incorporated into USF/W&T products from time to time that are not immediately reflected in the instruction book. If such a change has apparently been made in your equipment and does not appear to be reflected in your instruction book, contact your local USF/W&T sales office for information.

Please include the equipment serial number in all correspondence. It is essential for effective communication and proper equipment identification.

IM 50.200AA UA (B/1-01) 1.010-41


VERY IMPORTANT SAFETY PRECAUTIONS

WARNING

THIS EQUIPMENT IS SUITABLE FOR USE WITH CHLORINE ONLY. DO NOT USE WITH OTHER

GASES. SUCH USE CAN RESULT IN MALFUNCTION OR FAILURE OF VARIOUS COMPO-

NENTS, CAUSING POSSIBLE SEVERE PERSONAL INJURY.

TO AVOID SEVERE PERSONAL INJURY AS A RESULT OF A CHLORINE LEAK(S), ENSURE

THAT THE CHLORINATOR IS READY FOR OPERATION BEFORE CHLORINE IS INTRODUCED

INTO THE EVAPORATOR AND ITS CONNECTING PIPELINES. OPERATION OF THE CHLO-

RINATOR MAY BE NECESSARY TO DISPOSE OF CHLORINE TO PERMIT THE REPAIR OF

LEAKS. IF THE EVAPORATOR IS USED WITHOUT A CHLORINATOR, PROVIDE AN ALTER-

NATE MEANS OF DISPOSAL.

IF THE SUPPLY CONTAINER DOES NOT HAVE ADEQUATE RESERVE CAPACITY TO AC-

CEPT THE MAXIMUM CONTENTS THAT ARE BEING FORCED FROM THE EVAPORATOR

CYLINDER, DO NOT STOP CHLORINATION. INSTEAD, IN ORDER TO PREVENT OVER-FILL-

ING AND DEVELOPING EXTREME PRESSURES WITHIN THE SUPPLY CONTAINER, CLOSE

THE SUPPLY VALVE AND USE THE CHLORINATOR OR GAS DISPOSAL SYSTEM TO COM-

PLETELY EVACUATE THE EVAPORATOR AND ITS CONNECTING PIPELINES.

TO AVOID SEVERE PERSONAL INJURY OR CYLINDER RUPTURE, DO NOT INSTALL A

VALVE OF ANY TYPE BETWEEN THE EVAPORATOR DISCHARGE AND THE GAS PRES-

SURE RELIEF SYSTEM. RUN THE OUTFLOW FROM THE RELIEF VALVE TO ATMOSPHERE.

TERMINATE THE RELIEF LINE IN AN AREA WHERE GAS FUMES CANNOT CAUSE DAM-

AGE OR INJURY TO PERSONNEL. DO NOT TERMINATE THE RELIEF LINE AT A LOCATION

ROUTINELY USED BY PERSONNEL, SUCH AS WORK AREAS OR PATHWAYS, NOR NEAR

WINDOWS OR VENTILATION SYSTEM INTAKES. IF AN AREA MEETING THESE REQUIRE-

MENTS IS NOT AVAILABLE, REFER TO THE CHLORINE INSTITUTE FOR ALTERNATE

METHODS OF DISPOSAL.

TO AVOID AN OVERPRESSURE CONDITION CAPABLE OF RUPTURING THE PIPING SYS-

TEM AND RESULTING IN A DISCHARGE OF GAS FROM THE GAS PRESSURE RELIEF SYS-

TEM, DO NOT CLOSE ANY VALVE OR VALVES BETWEEN THE EVAPORATOR AND THE

CHLORINE SUPPLY WITHOUT FOLLOWING THE EVACUATION PROCEDURE DESCRIBED

IN THIS INSTRUCTION BOOK. LIQUID CHLORINE HAS A HIGH COEFFICIENT OF THERMAL

EXPANSION. DO NOT CLOSE VALVES IN SUCH A WAY THAT LIQUID CHLORINE MAY BE

TRAPPED, SINCE DANGEROUS PRESSURES CAPABLE OF RUPTURING THE PIPING SYS-

TEM MAY BUILD UP WITH A SMALL INCREASE IN TEMPERATURE.

DO NOT REMOVE THE PRESSURE RELIEF SYSTEM WHILE THE EVAPORATOR IS PRES-

SURIZED.

IM 50.200AA UA (B/1-01) SP-1


VERY IMPORTANT SAFETY PRECAUTIONS (CONT’D)

TO AVOID A MAJOR RELEASE OF CHLORINE, DO NOT OPEN THE LIQUID LINE PRESSURE

RELIEF SYSTEM WHILE THE EVAPORATOR IS PRESSURIZED.

THE GAS LINE TO THE REGULATING VALVE MUST BE SHORT WITH A SLIGHT DOWN-

GRADE TOWARD THE EVAPORATOR, ALLOWING ANY RELIQUEFIED CHLORINE TO DRAIN

BACK TO THE EVAPORATOR. THIS WILL PREVENT ANY RELIQUEFIED CHLORINE FROM

REACHING AND DAMAGING EQUIPMENT DOWNSTREAM OF THE REGULATING VALVE.

TO AVOID RUPTURE OF THE SUPPLY CONTAINER, CAUSING POSSIBLE SEVERE PER-

SONAL INJURY, CLOSE THE SUPPLY VALVE AND USE THE CHLORINATOR OR GAS DIS-

POSAL SYSTEM TO COMPLETELY EVACUATE THE EVAPORATOR CYLINDER AND ITS

CONNECTING PIPELINES.

ALL TWO-BOLT AMMONIA AND RUPTURE DISC UNIONS ARE ONLY LIGHTLY TIGHT-

ENED FOR SHIPPING. TO AVOID SEVERE PERSONAL INJURY FROM A CHLORINE LEAK,

FIRMLY TIGHTEN ALL UNIONS AFTER PIPING IS INSTALLED.

TO AVOID THE RUPTURE OF THE EVAPORATOR PRESSURE CYLINDER OR ITS CONNECT-

ING PIPELINES, CAUSING POSSIBLE SEVERE PERSONAL INJURY AND EQUIPMENT DAM-

AGE, DO NOT ATTEMPT TO DISASSEMBLE OR REPAIR THE RELIEF VALVE. IF IT MAL-

FUNCTIONS, REPLACE IT.

SECURELY SUPPORT THE EXPANSION TANK (e.g., WITH A BRACKET) TO AVOID DAMAGE

THAT COULD RESULT IN A MAJOR RELEASE OF LIQUID.

USE ONLY WATER TO FILL THE HOT WATER TANK AND HEAT EXCHANGER. DO NOT USE

ANY SUBSTITUTE FLUID. THE BOILING TEMPERATURE OF WATER PROVIDES A LIMIT ON

AN ACCIDENTAL OVER-TEMPERATURE CONDITION, THEREBY LIMITING THE GAS PRES-

SURE INSIDE THE EVAPORATOR CYLINDER.

THE TOP OF THE TANK WILL BE HOT (180°F). TO AVOID SEVERE PERSONAL INJURY DUE

TO HOT SURFACES, DO NOT REMOVE OR REINSTALL CAPLUG WITH BARE HANDS; USE

A GLOVE OR OTHER INSULATING MATERIAL.

WHEN DRAINING HOT WATER OUT OF HEAT EXCHANGER, ALLOW WATER TO COOL

BEFORE REMOVING PLUG.

TO AVOID SEVERE PERSONAL INJURY FROM BURNS DUE TO HOT WATER IN SIGHTGLASS

TUBE, TURN POWER OFF AND DRAIN THE TANK ENOUGH SO THAT NO WATER IS VISIBLE

IN THE SIGHTGLASS. ALLOW THE SIGHTGLASS TO COOL BEFORE HANDLING.

IM 50.200AA UA (B/1-01) SP-2



WHEN HANDLING HAZARDOUS MATERIAL, IT IS THE RESPONSIBILITY OF THE EQUIP-

MENT USER TO OBTAIN AND OBSERVE ALL SAFETY PRECAUTIONS RECOMMENDED BY

THE MATERIAL MANUFACTURER/SUPPLIER.

BOLT THE EVAPORATOR SECURELY TO THE CONCRETE PAD.

LIFT THE EVAPORATOR BY A CRANE HAVING NO LESS THAN A ONE-TON CAPACITY

RATING.

TO AVOID SEVERE PERSONAL INJURY FROM ACCIDENTAL EXPOSURE TO HIGH VOLT-

AGE, THE EVAPORATOR MUST BE SUITABLY GROUNDED TO EARTH BEFORE START-UP.

USE THE GROUNDING CONNECTOR PROVIDED.

LINE VOLTAGE IS PRESENT INSIDE THE CONTROL BOX EVEN WHEN THE PANEL POWER

SWITCH IS IN THE OFF POSITION. TO AVOID POSSIBLE SEVERE PERSONAL INJURY DUE

TO ELECTRICAL SHOCK, DISCONNECT THE EXTERNAL POWER SUPPLY BEFORE SER-

VICING.

TO AVOID POSSIBLE SEVERE PERSONAL INJURY FROM ELECTRICAL SHOCK, BE CARE-

FUL NOT TO TOUCH THE METAL SCREWS ON THE TERMINALS OF THE PRESSURE SWITCH.

THESE TERMINALS ARE CONNECTED TO 115 VOLTS.

TO AVOID POSSIBLE SEVERE PERSONAL INJURY DUE TO EQUIPMENT MALFUNCTION,

SEMI-ANNUALLY MAKE A COMPLETE ELECTRICAL CHECK OF THE OPERATION OF THE

TEMPERATURE, WATER LEVEL AND PRESSURE RELIEF ALARM SWITCHES. IF THE AP-

PROPRIATE RESPONSE IS NOT OBSERVED, REPLACE THE FAULTY CONTROL UNIT.

THE TWO MOST COMMON CAUSES OF CHLORINE PIPING LEAKS ARE:

1.

RE-USE OF GASKETS. THIS SHOULD NEVER BE DONE. ALWAYS HAVE AN AD-

EQUATE SUPPLY ON HAND AND ALWAYS USE NEW GASKETS OF THE CORRECT MATE-

RIAL AND SIZE AS IDENTIFIED ON THE EQUIPMENT PARTS DRAWING.

2.

IMPROPERLY MADE-UP THREADED PIPE JOINTS. SEE CHLORINE HANDLING

MANUAL FOR RECOMMENDED PROCEDURE.

USE ONLY USF/W&T LISTED PARTS, EXCEPT FOR THOSE COMMERCIALLY AVAILABLE

PARTS IDENTIFIED BY COMPLETE DESCRIPTION ON THE PARTS LIST. THE USE OF UN-

LISTED PARTS CAN RESULT IN EQUIPMENT MALFUNCTIONS CAUSING POSSIBLE SE-

VERE PERSONAL INJURY.

IM 50.200AA UA (B/1-01) SP-3



DO NOT DISCARD THIS INSTRUCTION BOOK UPON COMPLETION OF INSTALLATION.

INFORMATION PROVIDED IS ESSENTIAL TO PROPER AND SAFE OPERATION AND MAIN-

TENANCE.

ADDITIONAL OR REPLACEMENT COPIES OF THIS INSTRUCTION BOOK ARE AVAILABLE

FROM:

USFILTER'S WALLACE & TIERNAN PRODUCTS

1901 W. GARDEN ROAD

VINELAND, NJ 08360

PHONE: (856) 507-9000

FAX: (856) 507-4125

NOTE

Minor part number changes may be incorporated into USF/W&T products from time to time that are not immediately reflected in the instruction book. If such a change has apparently been made in your equipment and does not appear to be reflected in your instruction book, contact your local USF/W&T sales office for information.

Please include the equipment serial number in all correspondence. It is essential for effective communication and proper equipment identification.

IM 50.200AA UA (B/1-01) SP-4


REGIONAL OFFICES

INSTALLATION, OPERATION, MAINTENANCE, AND SERVICE INFORMATION

Direct any questions concerning this equipment that are not answered in the instruction book to the

Reseller from whom the equipment was purchased. If the equipment was purchased directly from

USFilter's Wallace & Tiernan Products (USF/W&T), contact the office indicated below.

UNITED STATES

1901 West Garden Road

Vineland, NJ 08360

TEL: (856) 507-9000

FAX: (856) 507-4125

CANADA

If the equipment was purchased directly from USF/W&T Canada, contact the nearest office indicated below.

ONTARIO QUEBEC

250 Royal Crest Court

Markham, Ontario

L3R3S1

(905) 944-2800

243 Blvd. Brien

Bureau 210

Repentigny, Quebec

(514) 582-4266

MEXICO

If the equipment was purchased directly from USF/W&T de Mexico, contact the office indicated below.

Via Jose Lopez Portillo 321

Col. Sta. Maria Cuautepec

Tultitlan, Edo. de Mexico

54900 Mexico

TEL: 525 879 0260

FAX: 525 875 2171

IM 50.200AA UA (B/1-01) 1.010-1D

IM 50.200AA UA (B/1-01)



SECTION 1 - TECHNICAL DATA

List Of Contents

PARA. NO.

General ...................................................................... 1.1

Application ............................................................... 1.2

Technical Data .......................................................... 1.3

IM 50.200AA UA (B/1-01) 1

1.1

General

!


WARNING: THIS EQUIPMENT IS SUITABLE FOR USE WITH

CHLORINE ONLY. DO NOT USE WITH OTHER GASES. SUCH

USE CAN RESULT IN MALFUNCTION OR FAILURE OF VARI-

OUS COMPONENTS CAUSING POSSIBLE SEVERE PERSONAL

INJURY.

1.2

Application

The Series 50-200 Evaporator is available for either Indoor or Outdoor

Service (optional), and in the following chlorine evaporating capacities:

• 6,000 lb/24 hr. maximum capacity with 12 kW heaters.



Part numbers for these arrangements are provided in Section 5. See Dwg.

50.200.000.011.

IM 50.200AA UA (B/1-01) 2


1.3

Technical Data

C

H

E h e l e l a o t r c t r i n

S e o

C u r i c a l a c e p

R e a c i t y q u i r e m e n t s

6 , 0 0 0 t o 1 0 , 0 o n h e a t e r s i z e .

0 0 l b / 2 4 h r .

d e p e n d i n g

E l e c t r i c a l l y p o w e r e d e x c h a n g e r .

h o t w a t e r h e a t

3 P h l e v e l a s d e e t e p o w e r a t r m i n e d b n o m i n a l v o l t a g e y c u s t o m e r d u r i n g o r d e r .

A v a i l a b l e n o m i n a l v o l t a g e r e q u

3 8 0 i r

V , e m e n t s

4 4 0 V , 4 a r e : 2 0 8 V ,

8 0 V a n d

2 2 0 V ,

5 5 0 V .

2 4 0 V ,

1 0 p s i m i n i m u m c i t y q u a l i t y w a t e r

3 0 1 4 0 p s i

W a t e r R e q u i r e m e n t s

L i q u i d C h l o r i n e

P r e s s u r e

S u p p l y

N O T E : C u s t o m e r v o l t a g e s u p p l y c o r r e s p o n d i n g t o t h e n o m i n a l m u v o l s t t a g b e e w i t h i n t h s p e c i f i e d e i n r a n

S e g c e t i o o f n t h e

2 , m i n

T a b l e i m u m

2 .

1 .

a n d

S i n g m l e a x p h i m u m a s e 1 1 v a l u e s

5 V p o o w e f r i s n o t p o w e r r e q u i r e d t h r o u g h

.

t

T h e h e u s c o n t r o l s e o f a a n d

1 k V A e q u i p m e n t t r a n s f o r m e o r b t a i n s i l o c a t e d n g i n l e p t h e h a s e c o n t r o l b o x .

E v a p o r a t o r C y l i n d e r R a t e d

W o r k i n g P r e s s u r e

5 6 0 p s i

R e l i e f V a l v e S e t t i n g

I n s t a l l e d W e i g h t ( H o t w a t e r t a n k a n d c y l i n d e r f i l l e d )

5 6 0 p s i

1 1 0 0 l b .

( a p p r o x i m a t e l y )

IM 50.200AA UA (B/1-01) 3


IM 50.200AA UA (B/1-01) 4


SECTION 2 - INSTALLATION


PARA./DWG. NO.

General .................................................................. 2.1

Unpacking and Base Mounting ............................ 2.2

Piping .................................................................... 2.3

Chlorine Gas and Liquid Piping ........................ 2.3.1

Water Piping ...................................................... 2.3.2

Evaporator Gas Pressure Relief System ............... 2.4

Gas Pressure Relief Valve Discharge Piping ..... 2.4.1

Liquid Line Pressure Relief System ..................... 2.5

Wiring ................................................................... 2.6

Controls ............................................................. 2.6.1

Heat Exchanger .................................................. 2.6.2

Hot Water Circulating Pump ............................. 2.6.3

Alarm Units ....................................................... 2.6.4

Evaporator Gas and Liquid Line Pressure

Relief Systems ................................................ 2.6.5

Illustrations

Dimensions ........................................................ 50.200.100.010A&B

Typical Installation ............................................ 50.200.110.010A&B

Installation - Evaporator Lifting Method ........... 50.200.110.030

Installation Wiring

Evaporator ...................................................... 50.200.130.010

Alarm Units .................................................... 50.100.130.011

Pressure Relief System-Alarm Switch ............ 50.200.130.020

IM 50.200AA UA (B/1-01) 5


!

WARNING: TO AVOID POSSIBLE SEVERE PERSONAL INJURY

OR DAMAGE TO EQUIPMENT, READ AND UNDERSTAND

THIS ENTIRE PREPARATION PROCEDURE AND FAMILIAR-

IZE YOURSELF WITH THE CHLORINE HANDLING MANUAL

BEFORE PERFORMING ANY WORK. BE SURE THE CHLO-

RINE SUPPLY REMAINS OFF UNTIL INSTRUCTED TO TURN

IT ON.

2.1

General

!

NOTE: Reference to optional equipment, such as an individual alarm unit, may be disregarded if such equipment is not a part of your installation.

WARNING: WHEN HANDLING HAZARDOUS MATERIAL, IT

IS THE RESPONSIBILITY OF THE EQUIPMENT USER TO OB-

TAIN AND OBSERVE ALL SAFETY PRECAUTIONS RECOM-

MENDED BY THE MATERIAL MANUFACTURER/SUPPLIER.

The Series 50-200 Evaporator is shipped completely assembled and ready for installation. For the location of the various evaporator components, see Dwg. 50.200.110.010.

2.2

Unpacking and Base Mounting

a. Unfasten and remove shipping crate.

b. If a back cover (outdoor option) was provided, remove it. Loosen and remove the bolts located at the top of the evaporator where the enclosure sides are fastened together.

c. Loosen the black, quarter-turn screws in the side panels of the enclosure.

NOTE: Do not attempt to remove the quarter-turns screws as they are retained on the reverse side of the panel by grommets.

d. Remove the side panels. Do not replace them until the evaporator is ready for operation.

e. Remove top cover and pipe trim.

f.

Attach two lifting hooks, each with no less than 1/2-ton capacity rating, to the lifting brackets that extend out a few inches from the gray insulation ring.

6 IM 50.200AA UA (B/1-01)


!

g. Chain the lifting hooks together to a hoist or crane.

WARNING: TO AVOID SEVERE PERSONAL INJURY, LIFT THE

EVAPORATOR BY A CRANE HAVING NO LESS THAN A ONE-

TON CAPACITY RATING. LIFT EVAPORATOR ONLY IN THE

MANNER SHOWN ON DWG. 50.200.110.030.

h. Unbolt the evaporator from the wooden base. Lift and lower the evaporator onto a concrete mounting pad prepared according to the mounting details in Dwg. 50.200.100.010. Bolt the evaporator to the pad.

f.

Replace top cover and pipe trim.

!

WARNING: TO AVOID SEVERE PERSONAL INJURY OR

EQUIPMENT DAMAGE, BOLT THE EVAPORATOR SECURELY

TO THE CONCRETE PAD.

2.3

Piping

2.3.1

Chlorine Gas and Liquid Piping

!

WARNING: ALL TWO-BOLT AMMONIA AND RUPTURE DISC

UNIONS ARE ONLY LIGHTLY TIGHTENED FOR SHIPPING.

TO AVOID SEVERE PERSONAL INJURY FROM A CHLORINE

LEAK, FIRMLY TIGHTEN ALL UNIONS AFTER PIPING IS IN-

STALLED.

NOTE: Piping for chlorine should conform to Chlorine Institute recommendations.

!

IM 50.200AA UA (B/1-01)

An ammonia-type union is furnished to accommodate the one-inch chlorine gas outlet (discharge) pipe. The chlorine gas outlet pipe and union extends upward from the gray insulation ring at the top of the evaporator.

The gas pressure relief system and a vacuum regulator-check unit (or gas pressure reducing valve) must be installed in this line. Refer to Dwg.

50.200.110.010 for proper installation. The vacuum regulator-check unit is electrically operated. The gas pressure reducing valve can be pilotoperated by air or water or can be electrically operated. Separate instructions are furnished with either valve.


OR EQUIPMENT DAMAGE, THE GAS LINE TO THE REGU-

LATING VALVE MUST BE SHORT, WITH A SLIGHT DOWN-

GRADE TOWARDS THE EVAPORATOR, ALLOWING ANY

RELIQUIFIED CHLORINE TO DRAIN BACK TO THE EVAPO-

7


2.3.2

RATOR. THIS WILL PREVENT ANY RELIQUIFIED CHLORINE

FROM REACHING AND DAMAGING EQUIPMENT DOWN-

STREAM OF THE REGULATING VALVE.

There are two points at which chlorine liquid can be brought into the evaporator. The top connection may be used as a convenience from a piping standpoint when there is only a single evaporator being used. The bottom connection is required when manifolding several evaporators for high capacity. For single evaporators, the bottom connection provides an alternate inlet connection. The bottom connection is also used as a drain when cleaning the evaporator in place. Ammonia unions are furnished at both liquid inlet points.

Water Piping (See Dwg. 50.200.110.010)

In the unlikely occurrence of a leak in the evaporator pressure cylinder, chlorine may be present in the water drain-overflow and vapor vent outlet lines.

!

WARNING: TERMINATE THE VAPOR VENT AND DRAIN/

OVERFLOW LINES IN AREAS WHERE NO INJURY TO PER-

SONNEL OR DAMAGE TO EQUIPMENT WILL OCCUR.

a. Make a 1-1/4-inch connection to the combination water bath drainoverflow line, and connect it to the appropriate plant piping.

b. Make a 1-1/4-inch connection to the vapor vent outlet and connect it to the appropriate plant piping.

c. Connect a 1/2-inch supply (10 psi min., 135 psi max.) to the water supply for the purpose of water make-up to the hot water tank.

2.4

Evaporator Gas Pressure Relief System

!

IM 50.200AA UA (B/1-01)

The Gas Pressure Relief System (see Dwg. 50.202.008.011) is provided as a preassembled unit.

WARNING: TO AVOID SEVERE PERSONAL INJURY OR CYL-

INDER RUPTURE, DO NOT INSTALL A VALVE OF ANY TYPE

BETWEEN THE EVAPORATOR DISCHARGE AND THE GAS

PRESSURE RELIEF SYSTEM. RUN THE OUTFLOW FROM THE

RELIEF VALVE TO ATMOSPHERE. TERMINATE THE RELIEF

LINE IN AN AREA WHERE GAS FUMES CANNOT CAUSE DAM-

AGE OR INJURY TO PERSONNEL. DO NOT TERMINATE THE

RELIEF LINE AT A LOCATION ROUTINELY USED BY PER-

8


2.4.1

SONNEL, SUCH AS WORK AREAS OR PATHWAYS, NOR NEAR

WINDOWS OR VENTILATION SYSTEM INTAKES. IF AN AREA

MEETING THESE REQUIREMENTS IS NOT AVAILABLE, RE-

FER TO THE CHLORINE INSTITUTE FOR ALTERNATE METH-

ODS OF DISPOSAL.

CAUTION: To ensure proper operation, install the system with the relief valve in a vertical position.

!

Install the Gas Pressure Relief System in the gas discharge line as shown in Dwg. 50.200.110.010. The purpose of this system is to prevent rupture of the pressure cylinder or related piping in case of an extreme overpressure condition. A detailed view of this system is provided in Dwg.

50.202.008.011.

Gas Pressure Relief Valve Discharge

NOTE: The relief valve outlet may be either 1-1/2-inch or 1-inch NPT depending on valve furnished.

To provide for friction losses, use the following pipe sizes:

Discharge line less than 50 feet long: use 1-or 1-1/2-inch, schedule 40 carbon steel pipe.

Discharge line 50 to 100 feet long: use 1-1/2-inch, schedule 40 carbon steel pipe.

The ASME Boiler and Pressure Vessel Code, Section VIII Division 1 UA-

356, appendix M, provides guidance for relief system discharge piping.

The following is an excerpt from that code:

UA-356 Discharge Lines From Safety Devices.

(a) Where it is feasible, the use of a short discharge pipe or vertical riser, connected through long-radius elbows from each individual device, blowing directly to the atmosphere, is recommended. Such discharge pipes shall be at least of the same size as the valve outlet….

(b) When discharge lines are long … the effect of the back pressure that may be developed therein … must be considered ….

(c) All discharge lines shall be run as direct as is practicable to the point of final release for disposal. For the longer lines, due consideration shall be given to the advantage of long-radius elbow, avoidance of

9 IM 50.200AA UA (B/1-01)


close-up fittings, and the minimizing of excessive line strains by expansion joints and well-known means of support to minimize linesway and vibration under operating conditions.

NOTE: It is recognized that no simple rule can be applied generally to fit the many installation requirements which vary from simple short lines that discharge directly to the atmosphere to the extensive manifold discharge piping systems where the quantity and rate of the product to be disposed of requires piping to a distant safe place.

2.5

Liquid Line Pressure Relief System

If liquid is trapped in the supply pipe between two pipes, liquid expansion can result in pipe rupture. To avoid this, a means of pressure relief is furnished. (See the Chlorine Handling Manual.)

The liquid line pressure relief system is provided as a pre-assembled unit and needs only to be installed in the liquid line. (See Dwgs. 50.200.110.010

and 50.202.007.011.)

!

!

!

CAUTION: To prevent damage to the rupture disc due to inadvertent overpressure, and to permit checking the pressure switch electrical alarm wiring, do not install rupture disc until initial leak testing is completed.

CAUTION: To ensure proper operation of the Liquid Line Pressure

Relief System, install the expansion chamber vertically, with the pressure switch on top.

WARNING: SECURELY SUPPORT THE EXPANSION TANK

(E.G., WITH A BRACKET) TO AVOID DAMAGE THAT COULD

RESULT IN A MAJOR RELEASE OF LIQUID, CAUSING POS-

SIBLE SEVERE PERSONAL INJURY.

2.6

Wiring

!

IM 50.200AA UA (B/1-01)

The components inside the control box and the equipment inside the evaporator enclosure have been factory pre-wired. Customer-made connections for power, alarms, and the gas regulating valve are shown on

Dwg. 50.200.130.010.

CAUTION: Alarm connections on the printed circuit board must be wired to actuate appropriate alarm devices (either customer-supplied or supplied by USF/W&T) as shown in the Installation drawings.

10


Connect alarm devices for low water temperature, high water temperature, and low water level conditions to the unpowered contacts on the printed circuit board. These contacts are rated for 10 amps at 120 volts ac and 30 volts dc. Connect the vacuum regulator-check unit (or gas pressure reducing valve) to the powered contacts on the printed circuit board.

(Refer to Figure 2.1.) Run the wiring for these devices through the rigid conduit supplied at the top left of the enclosure. Clamps are provided inside the box for securing these wires (for alarms and the regulating valve) neatly to the panel.

!

Figure 2.1 - Control Enclosure Circuit Board

CAUTION: Improper wiring may damage equipment.

Connect the appropriate three-phase power supply to the disconnect switch located in the upper right hand corner of the control box. Connect the ground wire of the supply to the grounding connector provided to the left of the disconnect switch. (Refer to Figure 2.2.) Run these wires through the rigid conduit provided at the top right of the enclosure.

IM 50.200AA UA (B/1-01) 11


!

!

Figure 2.2 - Three-Phase Power Supply and Ground Location

WARNING: TO AVOID SEVERE PERSONAL INJURY FROM

ACCIDENTAL EXPOSURE TO HIGH VOLTAGE, THE EVAPO-

RATOR MUST BE SUITABLY GROUNDED TO EARTH BEFORE

START-UP. USE THE GROUNDING CONNECTOR PROVIDED.

(SEE DRAWING 50.200.130.010 FOR LOCATION OF GROUND-

ING LUG INSIDE CONTROL BOX.)

CAUTION: The three-phase user power supply must be within the minimum and maximum voltage range corresponding to the nominal voltage rating label located just above the disconnect switch in the control box. See Table 2.1 for this voltage range. Refer to the actual control box to verify that the nominal voltage rating of the evaporator controls is the same as your power supply.

IM 50.200AA UA (B/1-01) 12


2.6.1

Table 2.1 - Power Supply Voltage Ranges

N o m i n a l V o l t a g e

R a t i n g

2 0 8

2 2 0

2 4 0

3 8 0

4 4 0

4 8 0

5 5 0

U s e r V o l t a g e S u p p l y

M i n i m u m

1 9 2

M a x i m u m

2 1 8

1 9 4

2 1 2

3 3 6

3 8 9

4 2 4

4 8 6

2

2

4

4

5

5

3

5

0

3

4

2

6 6

0 8

8 2

!

CAUTION: If your power supply does not fall within the proper range, do not connect power. Contact your nearest USF/W&T regional office for assistance.

NOTE: Field wiring must conform to local electrical code requirements.

Controls (Dwg. 50.200.170.010)

!

The evaporator controls and equipment obtain 115-volt, single-phase power from the secondary side of a transformer, located in the control box. The primary side of this transformer is connected to two lines of the threephase power supply; therefore, a separate 115-volt, single-phase supply is not required from the user to power the controls.

When the operating handle (located at the front right of the control box) for the disconnect switch is in the off position, power is turned off to the heat exchanger and control equipment. Line voltages for the customerconnected alarms and the three-phase power supply are present inside the control box, however, so observe the following warning when servicing the controls.

WARNING: LINE VOLTAGE IS PRESENT INSIDE THE CON-

TROL BOX EVEN WHEN THE PANEL POWER SWITCH IS IN

THE OFF POSITION. TO AVOID POSSIBLE SEVERE PER-

SONAL INJURY DUE TO ELECTRICAL SHOCK, DISCONNECT

EXTERNAL POWER SUPPLY BEFORE SERVICING.

IM 50.200AA UA (B/1-01) 13


2.6.2

2.6.3

2.6.4

2.6.5

Heat Exchanger

The heat exchanger nameplate voltage must be within the user voltage supply range corresponding to the nominal voltage labeled inside the control box above the disconnect switch. See Table 2.1. If this is not the case, the heater must be exchanged for one of the proper value. If necessary, contact your nearest USF/W&T regional office for assistance.

NOTE: For 220 Nominal Voltage Users: If the heat exchanger nameplate voltage rating reads as either 220/240 VOLTS or 240 VOLTS, do not return the heater. This is the proper heater for this evaporator arrangement.

For 440 Nominal Voltage Users: If the heat exchanger nameplate voltage rating reads as either 440/480 VOLTS or 480 VOLTS, do not return the heat exchanger. This is the proper heat exchanger for this arrangement.

Hot Water Circulating Pump

A circulating pump is provided and runs continuously while the evaporator is working. The controls are designed to shut the pump off in the event of a low water level condition.

The fractional hp 50/60 Hz motor that drives the pump is a totally enclosed type, suitable for outdoor use.

Alarm Units

If USF/W&T alarm units are provided, connect as shown in Dwg.

50.100.130.011.

Evaporator Gas and Liquid Line Pressure Relief Systems

Wire the pressure switch of each system directly to an alarm device or relay coil per Dwg. 50.200.130.010.

Every relief system, either liquid line or gas pressure relief, is supplied with the appropriate rupture disc, which is to be installed after all initial pressure testing is completed. (See paragraph 3.1, Preparation For Initial

Operation.)

IM 50.200AA UA (B/1-01) 14


NOTE: A NOT FURNISHED BY USF/W&T.

IM 50.200AA UA (B/1-01)

SERIES 50-200 EVAPORATOR - DIMENSIONS

50.200.100.010A

ISSUE 0 1-01

15


NOTE: A NOT FURNISHED BY USF/W&T.

IM 50.200AA UA (B/1-01)

SERIES 50-200 EVAPORATOR - DIMENSIONS

50.200.100.010B

ISSUE 0 1-01

16


IM 50.200AA UA (B/1-01)

NOTE: SEE DWG. 50.200.110.010B FOR EXPLANATION OF SYMBOLS.

SERIES 50-200 EVAPORATOR - TYPICAL INSTALLATION

50.200.110.010A

ISSUE 0 1-01

17


WARNING:

TO AVOID PERSONAL INJURY FROM ACCIDENTAL EXPOSURE TO HIGH VOLTAGE, SUITABLY GROUND THE

EVAPORATOR TO EARTH BEFORE START-UP.

!

THE RELIEF LINE MUST TERMINATE IN AN AREA WHERE GAS FUMES CANNOT CAUSE DAMAGE OR INJURY TO

PERSONNEL. DO NOT TERMINATE THE RELIEF LINE AT A LOCATION ROUTINELY USED BY PERSONNEL SUCH

AS WORK AREAS OR PATHWAYS NOR NEAR WINDOWS OR VENTILATION SYSTEM INTAKES. IF AN AREA MEET-

ING THESE REQUIREMENTS IS NOT AVAILABLE, REFER TO THE CHLORINE INSTITUTE, INC. OR THE COM-

PRESSED GAS ASSOCIATION, INC. FOR ALTERNATE METHOD OF RELIEF DISPOSAL.

NOTES:

!

SURFACE TEMPERATURE MAY REACH 212°F.

A

ACCESSORY ITEM FURNISHED ONLY IF SPECIFICALLY LISTED IN QUOTATION.

!

GAS PRESSURE REDUCING VALVE CAN BE FURNISHED BY USF/W&T FOR PRESSURE SUPPLY ARRANGE-

MENTS.

"

USE WHEN TWO OR MORE EVAPORATORS ARE MANIFOLDED. FOR ONE EVAPORATOR, CONNECTION MAY BE

AN ALTERNATE TO TOP INLET.

"

THE SYSTEM MUST BE INSTALLED WITH THE RELIEF VALVE IN A VERTICAL POSITION AND WITH THE CLOSED

END OF THE EXPANSION TANK FACING UP.

X

ALL PIPING AND FITTINGS TO BE SUPPLIED BY THE CUSTOMER. USE SCHEDULE 80 SEAMLESS CARBON

STEEL PIPE WITH 3000 LB. FORGED STEEL FITTINGS.

FOR REMOVAL OF CYLINDER, MINIMUM CEILING HEIGHT MUST BE 10'-0" PLUS LIFTING GEAR. FOR REMOVAL

OF CABINET, ALLOW 15" MINIMUM SIDE CLEARANCE.

IM 50.200AA UA (B/1-01)

SERIES 50-200 EVAPORATOR - TYPICAL INSTALLATION

50.200.110.010B

ISSUE 0 1-01

18


WARNING:

"

TO AVOID POSSIBLE SEVERE PERSONAL INJURY AND EQUIPMENT DAMAGE, DO NOT

ATTEMPT TO LIFT EVAPORATOR BY INLET AND OUTLET CONNECTIONS.

NOTE: X

NOT FURNISHED BY USF/W&T.

IM 50.200AA UA (B/1-01)

EVAPORATOR LIFTING METHOD - INSTALLATION

50.200.110.030

ISSUE 2 4-91

19


NOTE: X


A


FIELD WIRING (NOT BY USF/W&T) MUST CONFORM TO LOCAL ELECTRICAL CODES.

NOMINAL EVAPORATOR VOLTAGE SPECIFIED BY CUSTOMER AT TIME OF ORDER.

IN THE EVENT OF A LOW WATER TEMPERATURE, HIGH WATER TEMPERATURE, OR LOW WATER

LEVEL CONDITION, THE "C" AND "NC" TERMINALS ARE CLOSED BY A RELAY TO COMPLETE A

CIRCUIT. THEREFORE, CONNECT APPROPRIATE ALARMS TO THESE TERMINALS. THE "C" AND

"NO" TERMINALS MAY BE USED TO INDICATE NORMAL OPERATION.

SERIES 50-200 EVAPORATOR - INSTALLATION WIRING

50.200.130.010

ISSUE 0 4-88

IM 50.200AA UA (B/1-01) 20


NOTE: X


A


FIELD WIRING (NOT BY USF/W&T) MUST CONFORM TO LOCAL ELECTRICAL CODES.

WIRING BY USF/W&T.

IM 50.200AA UA (B/1-01) 21

ALARM UNITS - INSTALLATION WIRING

With Switch Powered From Equipment

50.100.130.011

ISSUE 2 5-83


NOTE: X


IM 50.200AA UA (B/1-01)

SERIES 50-200 EVAPORATOR - INSTALLATION WIRING

Liquid Line & Pressure Relief System - Alarm Switch

50.200.130.020

ISSUE 0 4-88

22


SECTION 3 - OPERATION


PARA./DWG. NO.

Preparation for Initial Operation ............................... 3.1

Controls ................................................................. 3.1.1

Leak Testing .......................................................... 3.1.2

Cathodic Protection System ................................... 3.1.3

Enclosure ............................................................... 3.1.4

Operation .................................................................. 3.2

Startup .................................................................... 3.2.1

Operating Routine .................................................. 3.2.2

Shutdown ............................................................... 3.2.3

Theory of Operation ................................................. 3.3

Illustrations

Operation-Evaporator Front Panel Indicators ........ 50.200.170.010

IM 50.200AA UA (B/1-01) 23


3.1

Preparation For Initial Operation

3.1.1

Controls

!

WARNING: FOR YOUR SAFETY AND THE SAFETY OF ALL

PLANT PERSONNEL, READ AND UNDERSTAND THIS ENTIRE

PREPARATION PROCEDURE AND FAMILIARIZE YOURSELF

WITH THE CHLORINE HANDLING MANUAL BEFORE PER-

FORMING ANY WORK.

!

a. Turn on the water supply to the solenoid valve.

WARNING: TO AVOID SEVERE PERSONAL INJURY OR

EQUIPMENT DAMAGE, USE ONLY WATER TO FILL THE HOT

WATER TANK AND HEAT EXCHANGER. DO NOT USE ANY

SUBSTITUTE FLUID. THE BOILING TEMPERATURE OF WA-

TER PROVIDES A LIMIT ON AN ACCIDENTAL OVER-TEM-

PERATURE CONDITION, THEREBY LIMITING THE GAS

PRESSURE INSIDE THE EVAPORATOR CYLINDER.

NOTE: Water supply pressure must be 10 psi minimum.

b. Turn the power switch located on the front of the control box to ON.

The solenoid valve in the water supply line will be energized and opened, admitting water to the hot water tank, pump, and heat exchanger. The LOW WATER LEVEL alarm light on the control box will go out when the water level reaches a point just above the bottom of the sightglass. At this point, the LOW WATER LEVEL individual alarm unit, if furnished, will go from red to green and the circulating pump will switch on. The coil in the contactor for the heat exchanger will be energized, resulting in the raising of the temperature of the water bath. When the water level reaches normal operating height, 2/3 to 3/4 of the height of the sightglass, the water level control switch will de-energize the solenoid valve and shut off the water supply.

c. Check to see that the low water temperature alarm switch, labeled

TS3-LOW, is set to actuate at 160°F (+10°, -5°). This switch is factory calibrated. No adjustment is necessary.

Below the tank water temperature of 160°F, the LOW TEMPERA-

TURE alarm light on the control box will stay on. When the temperature reaches 160°F (+10°,-5°) the low temperature switch will close, causing the vacuum regulator-check unit (or gas pressure reducing

IM 50.200AA UA (B/1-01) 24


3.1.2

!

valve) to open. At this time, the low temperature alarm unit, if furnished, will go from red to green.

d. The water bath will reach operating temperature about 45-60 minutes after start-up, depending on initial water temperature and heater capacity. The water bath temperature is controlled electronically by the printed circuit board. The control circuitry has been factory-calibrated to maintain the water temperature at approximately 180°F; adjustments are not required.

e. The high temperature alarm switch, labeled TS2-HIGH and located next to the low temperature switch TS3-LOW, is factory calibrated.

No adjustment is necessary.

f.

The pressure relief alarm switches are factory preset at 20 psi. No further adjustment of these switches is needed. When power is connected, the individual alarm unit, if furnished, will be green.

WARNING: IF ANY OF THE RESPONSES TO THE ELECTRI-

CAL CONTROLS IN B, C, D, AND E ARE NOT OBSERVED, A

FAULTY CONTROL DEVICE OR WIRING ERROR IS INDI-

CATED. IN ORDER TO AVOID POSSIBLE PERSONAL INJURY

OR EQUIPMENT DAMAGE, TAKE CORRECTIVE ACTION

BEFORE PROCEEDING. SEE THE TROUBLESHOOTING

GUIDE IN SECTION 4.

Leak Testing

!

WARNING: TO AVOID SEVERE PERSONAL INJURY AS A RE-

SULT OF A CHLORINE LEAK(S), ENSURE THAT THE CHLO-

RINATOR IS READY FOR OPERATION BEFORE CHLORINE

IS INTRODUCED INTO THE EVAPORATOR AND ITS CON-

NECTING PIPELINES. OPERATION OF THE CHLORINATOR

MAY BE NECESSARY TO DISPOSE OF CHLORINE TO PER-

MIT THE REPAIR OF LEAKS. IF THE EVAPORATOR IS USED

WITHOUT A CHLORINATOR, PROVIDE AN ALTERNATE

MEANS OF DISPOSAL.

NOTE: Do not install the rupture discs yet; wait until instructed to do so.

a. Connect a supply of dry air or nitrogen to the evaporator supply line.

b. Purge the system with the dry air or nitrogen to remove all moisture.

IM 50.200AA UA (B/1-01) 25

!

!

!

!

IM 50.200AA UA (B/1-01)


WARNING: TO AVOID SEVERE PERSONAL INJURY DUE TO

A CHLORINE LEAK(S), THE SUPPLY LINE MUST BE COM-

PLETELY DRY AND FREE OF OIL OR GREASE. AVOID LEAK

TESTING WITH WATER. STEEL PIPING WILL RAPIDLY COR-

RODE IF ANY MOISTURE IS PRESENT WHEN CHLORINE IS

ALSO IN THE PIPE.

c. Pressurize the system with dry air or nitrogen to 50 psi and check the pressure switches for correct operation. When the 50 psi is applied, the pressure relief alarm switch contacts will close and the optional

USF/W&T alarm unit, if provided, will turn red.

d. Vent the pressure and install the rupture discs, taking care not to let moisture enter the system.

CAUTION: When installing the rupture discs, ensure that the groove of the disc fits the mating tongue of the safety head to avoid altering the operation level of the rupture disc. Install the disc as per the instructions that accompany the rupture discs.


A CHLORINE LEAK(S), INSTALL BOTH PRESSURE RELIEF

SYSTEMS’ RUPTURE DISCS FOR LEAK TESTING WITH DRY

AIR OR NITROGEN NOW, BEFORE LEAK TESTING WITH

CHLORINE LATER.

e. Connect the evaporator inlet connection to the gas valve (rather than the liquid valve) on the chlorine supply container. This temporary connection is required to minimize the release of chlorine in the event that repairs are needed. Do not open the gas valve yet.

f.

Pressurize the system with the dry air or nitrogen supply to 150 psi and check for leaks by applying soapy water to the pipe joints. If bubbles form, a leak is present and must be corrected. If an alarm in either or both of the pressure relief systems is actuated, a leak(s) in the rupture disc(s) is indicated. If the disc is damaged, do not attempt to repair it; replace it with a new one.

WARNING: TO AVOID SEVERE PERSONAL INJURY, BE FA-

MILIAR WITH EMERGENCY PROCEDURES RECOMMENDED

BY THE CHLORINE INSTITUTE, INC. AND ANY APPLICABLE

PLANT EMERGENCY PROCEDURES FOR DEALING WITH

CHLORINE LEAKS THAT DO NOT RESPOND TO NORMAL

REPAIR PROCEDURES. HAVE AN APPROVED GAS MASK

AVAILABLE WHEN TESTING FOR CHLORINE LEAKS.

26

!

IM 50.200AA UA (B/1-01)


g. Reduce the pressure in the system to slightly below the chlorine supply pressure. Open the chlorine container gas valve and allow some chlorine gas to enter the system. Turn off the chlorine, repressurize with the dry air (or nitrogen) supply to 150 psi, and test for leaks with

26° Baume solution of ammonia. If a cloud of white mist forms when the ammonia solution is held near a pipe joint, a chlorine leak is present and must be corrected. If a leak is discovered, operate the chlorinator to dispose of the chlorine-in-air mixture. (If the evaporator is used without a chlorinator, provide an alternate means of disposal. See the warning in paragraph 3.1.2.) If no leaks are found, dispose of the chlorine-in-air mixture and proceed to the next step.

h. Close all valves between the evaporator and the source of supply.

Then slowly open the gas valve at the chlorine tank car or the ton container and test for leaks using the ammonia supplied with the evaporator. Open valves progressively, testing for leaks as each new section is filled with chlorine. If a leak is discovered, shut off the gas supply immediately, open the gas discharge line of the evaporator and operate the chlorinator to dispose of the gas. (If the evaporator is used without a chlorinator, provide an alternate means of gas disposal. See the gas disposal warning in paragraph 3.1.2.) Repair the leak before proceeding.

Moisture, including atmospheric, when combined with chlorine, forms hydrochloric and hypochlorous acids, which are highly corrosive.


CHLORINE LEAKS, WHEN ANY CONNECTION IN A CHLO-

RINE SYSTEM IS BROKEN EVEN FOR A SHORT TIME, PLUG

THE OPENING IN THE SYSTEM IMMEDIATELY TO PREVENT

THE ENTRANCE OF MOISTURE. PLUG THE OPENING OR USE

AUXILIARY CONTAINER VALVES TO PREVENT ENTRANCE

OF MOISTURE WHEN CONNECTING AND DISCONNECTING

THE CHLORINE SUPPLY.

i.

After the system up to the chlorinator inlet valve has been tested and found acceptable, close the gas supply valve and run the chlorinator to exhaust the gas in the evaporator and in the inlet line. When the evaporator pressure gauge reads zero, the evaporator chlorine outlet valve may be closed. If the evaporator pressure gauge shows pressure after the outlet valve has been closed for several minutes, repeat the above procedure until the evaporator pressure gauge holds zero.

When this is done, disconnect the piping from the gas valve and connect it to the liquid valve on the supply container. With the evaporator water bath adequately filled and up to operating temperature (ap-

27


3.1.3

proximately 180°F), open the liquid valve slowly and check this new connection for leaks.

!

WARNING: ONCE THE LIQUID SUPPLY VALVE HAS BEEN

OPENED, ALL VALVES IN THE LIQUID SUPPLY LINE MUST

BE LEFT OPEN UNTIL EITHER THE SUPPLY OF LIQUID HAS

BEEN EXHAUSTED OR THE SUPPLY LINE AND EVAPORA-

TOR ARE BEING EMPTIED BY THE CHLORINATOR OR

OTHER MEANS OF DISPOSAL. FAILURE TO FOLLOW THIS

PROCEDURE MAY RESULT IN AN OVERPRESSURE CONDI-

TION AND DISCHARGE OF GAS FROM THE RELIEF SYSTEM.

Cathodic Protection System

!

!

IM 50.200AA UA (B/1-01)

Sodium sulfate is added to the water bath to increase its conductivity, thus aiding in the start of the cathodic protection process. Observe and follow these instructions: a. Remove the caplug covering the 2-3/4-inch hole in the top of the tank.

WARNING: THE TOP OF THE TANK WILL BE HOT (180°F). TO

AVOID SEVERE PERSONAL INJURY DUE TO HOT SURFACES,

DO NOT REMOVE OR REINSTALL CAPLUG WITH BARE

HANDS; USE A GLOVE OR OTHER INSULATING MATERIAL.

b. Add 1/4 lb. (approximately 1/4 of the bottle provided) of sodium sulfate to the water bath when starting up for the first time. For best results, dissolve 1/4 lb. of sodium sulfate in one or two quarts of water and pour this solution into the water tank.

c. Replace caplug (See above warning.)

NOTE: Due to the insulating quality of the chlorine cylinder paint finish, there may be little or no initial reading on the milliammeter.

If a reading is now observed, adjust the potentiometer located next to the milliammeter on the front of the control box to obtain a reading between 25 and 50% on the meter. See Dwg. 50.200.170.010. If the needle remains on zero, check the cathodic protection system’s electrical connections. Before opening the control box to check connections, observe the following warning.

WARNING: LINE VOLTAGE IS PRESENT AT THIS LOCATION

EVEN WHEN THE PANEL POWER SWITCH IS IN THE OFF

POSITION. TO AVOID POSSIBLE SEVERE PERSONAL INJURY

28


!

DUE TO ELECTRIC SHOCK, DISCONNECT THE EXTERNAL

POWER SUPPLY BEFORE SERVICING.

d. If, after six months to one year, the milliammeter shows no reading, add another 1/4 lb. of sodium sulfate. If the water bath is drained, add 1/4 lb. of chemical on refill and adjust for a 25 to 50% reading.

NOTE: One-quarter lb. of chemical is all that is required at each addition of chemical. Using more than 1/4 lb. will not increase the efficiency of the cathodic protection system.

CAUTION: Always replace caplug after adding sodium sulfate solution. This will prevent the introduction of foreign objects or substances into the water bath.

3.1.4

Enclosure

Replace the enclosure on the evaporator. The evaporator is now ready for operation. Refer to Dwg. 50.200.060.030.

3.2

Operation

3.2.1

Startup

3.2.2

When the procedures in paragraph 3.1, Preparation For Initial Operation, are completed, the water bath will be at the operating temperature of

180°F. Slowly open the evaporator liquid supply valve. Open the outlet valve of the evaporator and put the chlorinator in service.

Operating Routine

Regular observation of the evaporator function indicators and alarm lights will enable the operator to verify that the evaporator is working properly.

• EVAPORATOR PRESSURE GAUGE: The gauge indicates the pressure inside the evaporator cylinder, which is also the equilibrium pressure inside the chlorine supply container corresponding to the temperature of the chlorine liquid. If a blockage develops or a valve is closed while chlorination is stopped, the pressure will increase substantially. Normal operating pressure is 30 to 140 psi. If the pressure rises into the 180 to 200 psi range, take corrective action. Refer to the Troubleshooting guide, Symptoms Group 2, in Section 4. The pressure gauge is designed for exposure up to 600 psi without loss of calibration.

IM 50.200AA UA (B/1-01) 29

IM 50.200AA UA (B/1-01)


• WATER TEMPERATURE METER: The meter indicates the water bath temperature. Normal operating temperature is approximately

180°F.

• CONTROL BOX ALARM LIGHTS: The front of the control box contains three alarm lights and one power indicator light. The red

HIGH TEMPERATURE alarm lights will go on when the water bath temperature exceeds 200°F. The orange LOW TEMPERATURE alarm light will illuminate when the water bath temperature drops below 160°F. If the water level drops below the bottom of the sightglass, the red LOW WATER LEVEL alarm light will come on.

NOTE: When the evaporator is turned on after short-term shutdown and the water is at normal operating level, the LOW WATER LEVEL alarm light will remain on for several seconds. Then the circulating pump will turn on. This pause is a part of the normal control operations of the evaporator.

• CATHODIC PROTECTION AMMETER: Refer to paragraph 3.1,

Preparation For Initial Operation. The meter may not indicate current for the first several months of service. Normal operating current is between 50 and 250 milliamps. If it exceeds this value, it may be reduced by turning counterclockwise the knob located to the right of the milliammeter. If the current is allowed to rise above 250 milliamps, the anodes of the cathodic protection system will not last as long as they would if the reading is maintained. The 50- to 250-milliamps reading assures full protection. More than 250 milliamps unnecessarily consumes anodes.

• WATER LEVEL SIGHTGLASS: The sightglass provides a direct indication of water bath level. If a LOW WATER LEVEL alarm light or separate alarm actuates, observation of the sightglass will confirm the low level condition or indicate a low water level switch malfunction. The normal operating level in the sightglass tube, as maintained by the automatic water level control, is 2/3 to 3/4 full. Low water level is approximately 1/8 full or less.

• OBSERVATION OF NEED FOR CYLINDER CLEANING: A buildup of impurities in the evaporator cylinder will result in gradual loss of heat transfer and loss of evaporating capacity. An obvious indication of this will be a cooling of the pipe coming from the outlet of the vacuum regulator-check unit (or gas pressure reducing valve). This cooling can be sensed by touching the pipe or observing condensation of frost on the outlet pipe.

30

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WARNING: TO AVOID DAMAGING THE INTERNAL PLASTIC

COMPONENTS OF THE CHLORINATOR, OR TO AVOID SE-

VERE PERSONAL INJURY CAUSED BY THE RELEASE OF

CHLORINE GAS, BE CERTAIN THAT NO LIQUID CHLORINE

EXISTS IN CHLORINATOR ROTAMETER TUBE. IF CHLORINE

LIQUID IS PRESENT IN THE ROTAMETER TUBE, IMMEDI-

ATELY SHUT DOWN THE EVAPORATOR BY FOLLOWING

THE CYLINDER EVACUATION PROCEDURES IN PARA-

GRAPH 3.2.3B. REFER TO SECTION 4 FOR CYLINDER CLEAN-

ING INSTRUCTIONS.

The need for cylinder cleaning can also be determined by observing the gas temperature gauge on the front panel next to the pressure gauge. The gas temperature gauge will show a drop in gas temperature at a given pressure and rate of withdrawal as impurities are deposited inside the chlorine cylinder. With some experience, the operator can use this indication to determine when the evaporator will need cleaning. As long as there are no blockages or closed valves between the evaporator and the supply, the pressure within the evaporator cylinder is the same as the pressure in the tank car or ton container, which in turn is a function of the temperature of the liquid chlorine in the tank car or ton container. By reading the pressure gauge for the evaporator cylinder, a close approximation of the liquid chlorine temperature can be obtained by referring to the temperature/pressure scale on the face of this gauge.

After evaporation at this temperature, the chlorine will pick up heat during its passage through the evaporator. The additional heat picked up is called “Superheat”. The amount of superheat at a particular time is function of the difference in temperatures between the water bath and the liquid chlorine, the efficiency of heat transfer through the wall of the chlorine cylinder and the rate of withdrawal of gaseous chlorine.

The face of the pressure gauge is graduated for pressure and the equilibrium (evaporating) temperature at that pressure. Using the gas temperature gauge, an approximate value of superheat can be obtained by reading the pressure and gas temperature gauge. For example, the pressure is 85 psi and temperature is 87°F. Reference to the temperature scale on the pressure gauge will show that the equilibrium (evaporating) temperature for a pressure of 85 psi is 70°F. Since the actual gas temperature is 87°F, the superheat is 17°F. It will be observed that a decrease in the withdrawal rate will result in an increase in superheat.

Likewise, increasing the withdrawal rate will result in a decrease in superheat.

IM 50.200AA UA (B/1-01) 31


In general, as long as there is some superheat, the evaporator is functioning properly. By periodically recording the superheat at a given chlorine feed rate and water bath temperature, the plant operator has an indication of the condition of the inside of the chlorine cylinder.

Contaminants in the liquid chlorine tend to accumulate in the evaporator cylinder and deposit on the inside wall, thus reducing heat transfer from the water bath. When sufficient impurities have collected to result in insufficient heat transfer, the superheat will have dropped close to zero and liquid chlorine will begin passing through the evaporator outlet, resulting in a hazardous condition of operation. Therefore, a periodic record of superheat will permit the operator to schedule the cleaning of the evaporator well in advance. As noted previously, the evaporator is functioning properly as long as there is some superheat. Due to tolerance in gauges, the first cleaning of a new evaporator should be scheduled when the superheat has dropped to about 10°F. Examination of the interior of the cylinder when the head

(upper flange) is removed for cleaning can guide the operator in judging what value of superheat should be used as a criterion for further cleanings.

NOTE: The specific pressure/temperature values used in this example were obtained from the Chlorine Manual, published by the

Chlorine Institute, Inc.

3.2.3

Shutdown

!

IM 50.200AA UA (B/1-01)

• Short-Term Shutdown.

a. Close the evaporator outlet valve. When the outlet valve is closed, gas will form inside the cylinder, pushing liquid back to the supply container.

b. If the supply container does not have adequate reserve capacity to accept the maximum contents being forced from the evaporator cylinder, do not stop chlorination.

WARNING: TO AVOID RUPTURE OF THE SUPPLY CON-

TAINER, CAUSING POSSIBLE SEVERE PERSONAL INJURY,

CLOSE THE SUPPLY VALVE AND USE THE CHLORINATOR

OR GAS DISPOSAL SYSTEM TO COMPLETELY EVACUATE

THE EVAPORATOR CYLINDER AND ITS CONNECTING PIPE-

LINES.

NOTE: The warning above applies if a situation is created, for example, where a new, capacity-filled supply is connected to the evapo-

32

!

IM 50.200AA UA (B/1-01)

50-200 EVAPORATOR FOR CHLORINE rator and the previous supply is disconnected or closed. If a liquid supply valve is then closed, after additional liquid is forced into the capacity-filled supply container, pressures capable of rupturing the container will develop with a slight increase in temperature.

c. If the supply container can accept the maximum contents without exceeding its rated capacity, the outlet valve can remain closed throughout the short-term shutdown; however, do not shut any valves in the chlorine supply piping. With the evaporator outlet closed or with chlorination stopped, as long as the inlet valve to the evaporator and the valves to the ton container or tank cars are open, the pressure within the evaporator cylinder is limited to never exceeding the pressure in the ton container or tank car.

WARNING: TO AVOID AN OVERPRESSURE CONDITION

THAT MAY RESULT IN A DISCHARGE OF GAS FROM THE

GAS PRESSURE RELIEF SYSTEM, DO NOT CLOSE ANY VALVE

OR VALVES BETWEEN THE EVAPORATOR AND THE CHLO-

RINE SUPPLY WITHOUT FOLLOWING THE EVACUATION

PROCEDURE DESCRIBED IN STEP B, BELOW. LIQUID CHLO-

RINE HAS A HIGH COEFFICIENT OF THERMAL EXPANSION.

DO NOT CLOSE VALVES IN SUCH A WAY THAT LIQUID

CHLORINE MAY BE TRAPPED, SINCE DANGEROUS PRES-

SURES CAPABLE OF RUPTURING THE PIPING SYSTEM MAY

BUILD UP WITH A SMALL INCREASE IN TEMPERATURE.

d. Re-open the gas outlet valve to resume evaporator operation.

• Long-Term Shutdown.

a. Follow the instruction for Short-Term Shutdown, steps a, b, and c. If the liquid can be safely pushed back to the supply container, shut the evaporator outlet valve for a period of approximately 30 minutes. Under these conditions, most of the liquid chlorine will be forced back to the supply tank through the nipple and remaining liquid will be evaporated by the heat of the water bath.

b. At the end of this period, shut the supply valve at the tank car or the ton container; immediately open the evaporator outlet valve and run the chlorinator to exhaust the gas in the evaporator and the gas and liquid in the inlet line.

c. When the evaporator pressure gauge reads zero, the chlorine outlet valve may be closed.

33


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d. If the evaporator pressure gauge shows pressure after the outlet valve has been closed for several minutes, repeat steps a through c until the evaporator pressure gauge reads zero with outlet valve closed. Then turn off power to the control box and alarm units.

e. If no standby evaporator is being used, shut down the chlorinator.

f.

Drain the hot water tank by opening the drain valve at the back of the unit.

g. Drain the heat exchanger by removing the 1/2-inch plug at the bottom (underside) of the heat exchanger. A small container may be used to capture the water (approximately 1/2 gallon) when the plug is removed.

WARNING: TO AVOID SEVERE PERSONAL INJURY WHEN

HOT WATER DRAINS OUT OF HEAT EXCHANGER, ALLOW

WATER TO COOL BEFORE REMOVING PLUG.

h. Replace the plug after the water has completely drained from the heater. Remove the 1/4 NPT plug at the bottom of the pump impeller housing (Dwg. 50.200.110.010 in Section 2). Allow the pump to drain thoroughly before replacing the plug.

!

3.3

Theory Of Operation

CAUTION: The pump and heat exchanger must be drained to prevent corrosion build-up during long-term shutdown.

Liquid chlorine from the source container is piped to the evaporator chlorine cylinder. This cylinder is immersed in a temperature-controlled hot water bath. Liquid enters the cylinder through the top, but a drop pipe inside carries the liquid almost to the bottom. The alternate inlet connection at the bottom has a riser that terminates at approximately the same level as the end of the drop pipe. Thus, the liquid chlorine enters near the bottom of the cylinder and the vapor leaves from a point somewhat below the top, as the discharge connection also has a short drop pipe. This arrangement limits cylinder pressure to that of the source container and prevents the complete filling of the cylinder with liquid chlorine. The heat transfer surface in the gas-filled portion of the cylinder superheats the chlorine vapor.

IM 50.200AA UA (B/1-01) 34


When the entering liquid chlorine contacts the hot inner surface of the evaporator cylinder, it boils inside this cylinder. When sufficient gas has formed to satisfy the demand of the chlorination process, the incoming liquid chlorine flow stabilizes because the pressure in the evaporator cylinder and supply container have equalized. If too much liquid enters the evaporator cylinder, more gas is formed than is required by the chlorination process. The evaporator cylinder pressure rises above that of the supply container, causing some liquid chlorine to be forced back into the supply container until the pressure in the evaporator cylinder and supply container have again equalized. Therefore, as long as the line to the supply container is open, the liquid level in the evaporator cylinder is automatically adjusted by the rate of gas used. If no gas is withdrawn, the evaporator will empty itself as the gas formed pushes the liquid back to the supply container. When the liquid level falls below the end of the inlet pipe, it is pushed back to the supply container by gas until no liquid remains. Conversely, if more gas is called for than a particular liquid level is able to generate, the liquid level will rise, causing more liquid to change to gas to meet the demand.

NOTE: For detailed description of control equipment, refer to Section 4 - Service.

IM 50.200AA UA (B/1-01) 35


IM 50.200AA UA (B/1-01)

EVAPORATOR FRONT PANEL INDICATORS - OPERATION

50.200.170.010

ISSUE 0 4-88

36


SECTION 4 - SERVICE


PARA./DWG. NO.

General ...................................................................... 4.1

Inspection ............................................................... 4.1.1

Temperature Control and Indication ......................... 4.2

High and Low Temperature Switches ...................... 4.3

Relief System Pressure Switches .............................. 4.4

Automatic Water Level Control and Low Level

Switches ................................................................. 4.5

Electrical System Checks ......................................... 4.6

Temperature Switches ........................................... 4.6.1

Water Level Switch and Low Level Switch .......... 4.6.2

Pressure Switch (Evaporator Relief Systems) ....... 4.6.3

Cathodic Protection System ...................................... 4.7

Power and Alarm Lights on Control Box ................. 4.8

Hot Water Circulating Pump .................................... 4.9

Evaporator Pressure Relief System .......................... 4.10

Liquid Line Pressure Relief System ......................... 4.11

“In-Place” Cleaning of the Evaporator Cylinder ...... 4.12

Five Year Inspection of Evaporator Cylinder ........... 4.13

Operational Inspection of the Pressure Relief

Systems .................................................................. 4.14

Evaporator Gas Pressure Relief System ................ 4.14.1

Liquid Line Pressure Relief System ...................... 4.14.2

Pressure Alarm Switch .......................................... 4.14.3

Troubleshooting Guide ............................................. 4.15

Warning Summary Pages ......................................... 2 Pages

Caution Summary Page ............................................ 1 Page

Illustrations

Wiring - Cathodic Protection ................................. 50.200.140.010

Service

U20208 Drying Kit ............................................. 50.200.150.010

Lifting Method .................................................... 50.200.150.060

Schematic Wiring

Level and Temperature Control .......................... 50.200.155.020

Controls and Equipment ..................................... 50.200.155.010

IM 50.200AA UA (B/1-01) 37

4.1

General

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FROM EXPOSURE TO CHLORINE, REVIEW THE CHLORINE

HANDLING MANUAL BEFORE BREAKING ANY CHLORINE

CONNECTIONS.

Piping leaks are usually caused by either improperly assembling pipe joints or reusing gaskets.

WARNING: LINE VOLTAGE IS PRESENT INSIDE THE CON-

TROL BOX. TO AVOID POSSIBLE SEVERE PERSONAL INJURY

FROM ELECTRICAL SHOCK, DEACTIVATE EXTERNAL

POWER SOURCE(S) BEFORE OPENING THE CONTROL BOX.

WARNING: TO REDUCE THE POSSIBILITY OF CHLORINE

LEAKAGE, ASSEMBLE ALL THREADED JOINTS IN ACCOR-

DANCE WITH THE CHLORINE HANDLING MANUAL. DO NOT

REUSE GASKETS; ALWAYS USE NEW GASKETS.

WARNING: TO AVOID SEVERE PERSONAL INJURY, WHEN

ANY PIPING CONNECTION IS BROKEN, EVEN FOR A SHORT

PERIOD OF TIME, PLUG THE RESULTANT OPENING IMME-

DIATELY TO PREVENT THE ENTRANCE OF MOISTURE.

MOISTURE, INCLUDING ATMOSPHERIC, WHEN COMBINED

WITH CHLORINE, IS HIGHLY CORROSIVE TO PIPING. WHEN

CHANGING CHLORINE SUPPLY CONTAINERS, PREVENT

THE ENTRANCE OF MOISTURE INTO THE CHLORINE PIP-

ING BY PLUGGING OPEN ENDS OR USING AUXILIARY TON

CONTAINER VALVES.

4.1.1

Inspection

When performing preventive maintenance or servicing of the evaporator, perform the following inspection routine: a. Check for any physical damage to removed parts (chipped, cracked, damaged threads; excessive corrosion). Replace all damaged components.

b. Discard and replace all removed gaskets, seals, and O-rings.

NOTE: Refer to Section 6 for a list of approved USF/W&T spare parts.

38 IM 50.200AA UA (B/1-01)


4.2

Temperature Control and Indication

The tank water temperature is sensed by an electronic temperature probe immersed in the water bath. The probe is mounted in the probe housing block located on the top of the hot water tank. The electronic signal from the probe is processed by the printed circuit board to control the operation of the heat exchanger and to indicate the water temperature on the analog meter on the front of the control box. This circuitry has been factorycalibrated; adjustments are not required. Refer to the Troubleshooting

Guide in case of malfunction.

4.3

High and Low Temperature Switches

This is a dual temperature switch that senses the water bath temperature directly at the tank. The low temperature switch (TS3-LOW) is set to

160°F; the high temperature switch (TS2-HIGH) is set to 200°F. The switches are rated for 10 amperes at 120 VAC and 30 VDC. Alarm connections for the switches are located on the printed circuit board inside the box.

4.4

Relief Systems Pressure Switches

This single-setting pressure sensing device is pre-set for 20 psi at the factory and requires no readjustment. The switch is rated at 10 amperes for

125 or 250 Vac.

Should the pressure switch (U24680) function improperly on either the liquid line pressure relief system (U27615) or the pressure relief system

(U25471), proceed as follows:

!

!

IM 50.200AA UA (B/1-01)

WARNING: TO AVOID A MAJOR RELEASE OF CHLORINE,

CAUSING POSSIBLE SEVERE PERSONAL INJURY, DO NOT

REMOVE THE PRESSURE RELIEF SYSTEM WHILE THE

EVAPORATOR IS PRESSURIZED. BEFORE ATTEMPTING TO

SERVICE THE PRESSURE RELIEF SYSTEM, FOLLOW STEPS

A AND B IN PARAGRAPH 4.12.

If after performing step a in paragraph 4.12, the pressure switch remains actuated, chlorine under pressure is still present in the pressure relief system. This indicates a leaking (not ruptured) rupture disc.


INHALATION OF CHLORINE GAS, USE AN APPROVED GAS

MASK AND VENTILATION EQUIPMENT WHEN REMOVING

THE RUPTURE DISC.

39

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a. Turn off the evaporator controls, alarm unit power supplies, and power to the alarm circuit being serviced. Ensure that the chlorine supply valve will remain closed while work is in progress.

b. Remove the front cover from the pressure switch and disconnect the alarm wiring and electrical conduit from the switch’s terminals.

NOTE: The relief system pressure switch is protected from corrosion by an oil-filled diaphragm capsule.

CAUTION: Do not disturb the threaded connections between the pressure switch and this capsule, as a loss of oil will cause the pressure switch to malfunction or become inoperative.

c. Remove the pressure switch-diaphragm capsule assembly from the pressure relief system at the point where the diaphragm capsule bottom connection and the expansion tank reducing bushing meet. Do not remove the reducing bushing from the expansion tank, as this is a permanent joint.

d. Using the Resistance Mode, connect a volt/ohmmeter across the “C”

(Common) and “NO” (Normally Open) terminals.

e. Connect the pressure switch-diaphragm capsule assembly to a controlled pressure source. Install a calibrated pressure gauge in the line to the source.

f.

Raise and lower the pressure to determine if the switch is functioning properly and at what pressure the switch closes.

g. The pressure switch should be able to close repeatedly on a rising pressure at 15 to 20 psi. If it does not, adjust the response point by turning counterclockwise the knurled nut on the switch located below the microswitch. Repeat step f and this step to confirm proper actuating pressure.

h. Reconnect the alarm wiring and the conduit to the switch and replace the front cover.

i.

Energize the alarm portion of the electrical circuit.

IM 50.200AA UA (B/1-01) 40


4.5

Automatic Water Level Control and Low Level Switches

Water level is sensed by four stainless steel probes (one common, one low level, and two differential service) mounted in the probe housing block on the top of the tank. Two independent switches are actuated by these probes.

The differential service probes actuate the Automatic Water Level Control Switch filling the evaporator hot water tank 2/3 to 3/4 of the height of the sightglass and will refill the tank when the water level has dropped to about two inches or more below this position. The Low Water Level switch will operate just before the water level drops below the sightglass.

The probe lengths are pre-cut and no adjusting is required.

Periodically clean the sightglass tube in the water level indicator on the front panel so that the water level can be easily seen. The tube is easily accessible after removing the plastic indicator cover.

!

WARNING: TO AVOID SEVERE PERSONAL INJURY FROM

BURNS DUE TO THE HOT WATER IN THE SIGHTGLASS TUBE,

TURN THE POWER OFF AND DRAIN THE TANK ENOUGH SO

THAT NO WATER IS VISIBLE IN THE SIGHTGLASS. ALLOW

THE SIGHTGLASS TO COOL BEFORE HANDLING.

4.6

Electrical System Checks

Make electrical checks described in paragraphs 4.6.1 and 4.6.2.

4.6.1

4.6.2

!


DUE TO EQUIPMENT MALFUNCTION, SEMI-ANNUALLY

MAKE A COMPLETE ELECTRICAL CHECK OF THE OPERA-

TION OF THE TEMPERATURE, WATER LEVEL, AND PRES-

SURE RELIEF ALARM SWITCHES. IF THE APPROPRIATE RE-

SPONSE IS NOT OBSERVED, REPLACE THE FAULTY CON-

TROL UNIT.

Temperature Switches

The high and low temperature switches are factory calibrated. No adjustment is necessary.

Water Level Switch and Low Level Switch

a. Drain the water to below the sightglass and allow it to refill. If level control is working properly, it will refill automatically and the low level alarm will activate and reset.

IM 50.200AA UA (B/1-01) 41


4.6.3

b. Close drain tightly when testing is completed.

Pressure Switch (Evaporator Relief System)

a. Remove the switch cover.

b. Using a thin screwdriver, operate the microswitch and observe operation of the alarm.

!


FROM ELECTRICAL SHOCK, BE CAREFUL NOT TO TOUCH

THE METAL SCREWS ON THE TERMINALS. THEY ARE CON-

NECTED TO 115 VOLTS.

c. Replace the switch cover when testing is completed.

4.7

Cathodic Protection System

An annual inspection of the cathodic protection anodes will, under normal conditions, show that the anodes are almost expended. Replace the four magnesium anodes. On a new evaporator, the anodes normally last well over a year. After the first replacement, they should be replaced annually.

Before new anodes are installed, it is recommended that the water be drained from the system and an inspection of the tank and cylinder be made. Sludge formed by the corrosion of the anodes should be flushed from the hot water tank and discharged through the water overflow line.

If the cathodic protection system has been operated in the recommended range, little or no corrosion will be found. Add fresh water after the new anodes have been installed. If no reading on the ammeter is obtained, additional sodium sulfate (1/4 lb.) may be added.

4.8

Power and Alarm Lights on Control Box

The lamps inside the power and alarm lights on the control box are rated for 5000 hours of life, therefore, they will eventually burn out. See Section

6, Spare Parts List, for information on ordering replacement bulbs.

4.9

Hot Water Circulating Pump

This pump is completely sealed; no lubrication or maintenance is required. However, the manufacturer of the pump has made two repair kits available for the pump:

IM 50.200AA UA (B/1-01) 42


• Pump housing seal kit

• Shaft seal kit.

Part numbers for these kits are found in the Section 6 - Spare Parts List.

The pump is the end-suction type. If the evaporator is to be shut down for an extended period of time, remove the plug at the bottom of the pump impeller housing to fully drain the pump.

!

CAUTION: Failure to fully drain the pump could lead over time to corrosion build-up and permanently damage the pump.

Replace plug after draining.

4.10

Evaporator Pressure Relief System

!

IM 50.200AA UA (B/1-01)

A pressure relief system conforming to ASME Boiler and Pressure Vessel

Code recommendations is supplied with the evaporator. This pressure relief system consists of a rupture disc (rupture point 400 psi), a pressure switch (set at 20 psi), and a pressure relief valve (set at 560 psi). The evaporator will not, under normal operating conditions, reach these pressures, but in abnormal circumstances, such as a closed inlet and outlet valve, these pressures could develop. The alarm actuates when the disc ruptures or develops a leak. This alarm serves as a signal that conditions exist that can cause gas to be relieved out of the system. A Pressure Relief

System Alarm indicates that the evaporator system requires immediate corrective attention.

WARNING: TO AVOID SEVERE PERSONAL INJURY, BE FA-

MILIAR WITH EMERGENCY PROCEDURES, TROUBLE-

SHOOTING PROCEDURES, AND SERVICE SO THAT PROMPT

AND EFFECTIVE ACTION CAN BE TAKEN.

Overpressure in the evaporator cylinder can result from a closed outlet valve or stopping of the chlorinator in conjunction with a blockage in the liquid inlet line, a closed valve in the liquid inlet line, or excessive “air padding” of tank cars. If the pressure relief system alarm actuates, the cause must immediately be determined and corrected. Refer to the Troubleshooting Guide, Symptom, Group 2, in this section. If an alarm is actuated, observe the evaporator pressure gauge. If it reads normal (30 to 140 psi), the rupture disc may be faulty.

To resume operation after correction of the overpressure problem, replace the rupture disc. Purge any gas from the pressure relief system piping lines

43


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!

!

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with dry air, nitrogen, or carbon dioxide as soon as possible after system actuation. Check the relief valve for leaks using 150 psi pressure. The valve must be leak-tight to function properly.

WARNING: TO PREVENT MAJOR RELEASE OF CHLORINE,


REMOVE THE PRESSURE RELIEF SYSTEM WHILE THE

EVAPORATOR IS PRESSURIZED.

Before attempting to service the relief system, follow step a in paragraph

4.12, “In-Place” Cleaning Of Evaporator Cylinder. If, after this step, the pressure switch remains actuated, chlorine under pressure is still present in the pressure relief system. This indicates a leaking (not ruptured) rupture disc.


INHALATION OF CHLORINE, USE AN APPROVED GAS MASK

AND VENTILATION EQUIPMENT WHEN REMOVING THE

RUPTURE DISC.

If the disc is removed and is not ruptured, a leaking disc is the trouble. In this case, a closed valve and/or blockage are not likely to be found. Replace the rupture disc.

CAUTION: When installing the rupture disc, ensure that the groove of disc fits the mating tongue of the safety head to avoid altering the operating level of the rupture disc.

WARNING: TO AVOID THE RUPTURE OF THE EVAPORATOR

PRESSURE CYLINDER OR ITS CONNECTING PIPELINES,

CAUSING POSSIBLE SEVERE PERSONAL INJURY AND

EQUIPMENT DAMAGE, DO NOT ATTEMPT TO DISASSEMBLE

OR REPAIR THE RELIEF VALVE. IF IT MALFUNCTIONS, RE-

PLACE IT.

!

CAUTION: Purge the valve of gas as soon as possible after operation before moisture can combine with the gas to become corrosive.

4.11


Overpressure in the liquid line is usually the result of a valve closed at the supply and at the evaporator at the same time. A contaminant blockage in the inlet line with a valve closed on either side can also cause an overpressure problem. The rupture disc will rupture at 400 psi, activating an alarm.

If the system activates, as indicated by the alarm switch, the cause must

44 IM 50.200AA UA (B/1-01)


!

immediately be determined and corrected. Usually, corrective action will involve opening one or more valves. To restore the liquid line pressure relief system, replace the rupture disc as instructed in the preceding section.

WARNING: TO AVOID MAJOR RELEASE OF CHLORINE,


OPEN THE LIQUID LINE PRESSURE RELIEF SYSTEM WHILE

THE EVAPORATOR IS PRESSURIZED.

!

Before attempting to service the relief system, follow step a in paragraph

4.12, “In-Place” Cleaning Of Evaporator Cylinder.

CAUTION: Do not disturb the threaded joints between the alarm switch and the protective capsule. Any oil loss will result in a faulty pressure-gauge reading.

If this rupture disc is removed and is not ruptured, a leaking disc is the trouble. In this case, closed valves and/or blockage are not likely to be found. Replace leaking rupture disc. If the pressure switch remains actuated after performing step a in paragraph 4.12, “In-Place” Cleaning of the

Evaporator Cylinder, chlorine is still under pressure in the pressure relief system. This indicates a leaking (not ruptured) rupture disc.

!

!



AND VENTILATION EQUIPMENT WHEN REMOVING THE

RUPTURE DISC.

CAUTION: When installing rupture disc, ensure that the groove of the disc fits the mating tongue of safety head to avoid altering the operating level of the rupture disc.

4.12

“In-Place” Cleaning of the Evaporator Cylinder

The rate of residue buildup varies considerably with the type of impurity, the source of chlorine supply, the rate of usage, and various other factors.

The following maintenance cleaning procedure should be implemented every 12 months, or sooner if a loss in superheat or reduction in chlorine capacity is observed. These instructions describe a method for cleaning chlorine residue from the evaporator without removing the cylinder. The special accessories required by this procedure for cleaning and drying are available in kit form in USF/W&T Part No. U20208. The replacement gaskets required for each evaporator are included in parts kit U28839. A water supply line of 3/4-inch pipe size at a minimum pressure of 20 psi

45 IM 50.200AA UA (B/1-01)

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!

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IM 50.200AA UA (B/1-01)


must be available. The hose required is not furnished as part of either kit.

If these instructions are carefully followed, the cylinder should be clean and dry when restored in service.

In some circumstances, it could be desirable to thoroughly review the relative advantages of cleaning versus simply replacing the evaporator cylinder, thereby eliminating the time and necessary complexities of the cleaning process and enjoying the security and full operating capacity provided by a new cylinder. This choice would take into consideration the local cost and availability of personnel, facilities, equipment, and time required for the cleaning process measured against the installed cost of a new cylinder. This comparison can be made only on the basis of individual local circumstances.

Under normal operating conditions, deposits will accumulate in the evaporator cylinder and, over a period of time, will reduce its operating capacity.

For this reason, periodic cleaning is required to remove these deposits.

CAUTION: Refer to the instruction book provided with the equipment for complete details on recommended frequency and procedures to properly accomplish this cleaning.

To clean the evaporator cylinder “In-Place,” perform the following steps.

WARNING: ANY MOISTURE, INCLUDING ATMOSPHERIC, IS

HIGHLY CORROSIVE WHEN COMBINED WITH CHLORINE.

TO AVOID SEVERE PERSONAL INJURY AND EQUIPMENT

DAMAGE AS A RESULT OF EXTREME CORROSION, THE CYL-

INDER MUST BE ABSOLUTELY DRY AFTER CLEANING IS

COMPLETED.

a. With the evaporator controls on, evacuate the chlorine cylinder as follows:

(1) Close the evaporator outlet valve. When the outlet valve is closed, gas will form inside the cylinder, thereby pushing liquid chlorine back to the supply container.

WARNING: IF THE SUPPLY CONTAINER DOES NOT HAVE

ADEQUATE RESERVE CAPACITY TO ACCEPT THE MAXI-

MUM CONTENTS THAT ARE BEING FORCED FROM THE

EVAPORATOR CYLINDER, DO NOT STOP THE CHLORINA-

TOR. INSTEAD, IN ORDER TO PREVENT OVER-FILLING AND

DEVELOPING EXTREME PRESSURES WITHIN THE SUPPLY

CONTAINER, CLOSE THE SUPPLY VALVE AND USE THE

46

!

!

IM 50.200AA UA (B/1-01)


CHLORINATOR OR GAS DISPOSAL SYSTEM TO COM-

PLETELY EVACUATE THE EVAPORATOR AND ITS CON-

NECTING PIPELINES.

(2) If the maximum amount of contents can be forced out of the cylinder to the supply without exceeding the rated capacity of the supply container, the outlet valve can be closed. However, do not shut any valves in the chlorine supply piping.

NOTE: If the evaporator outlet is closed or chlorination is stopped, and if the inlet valve to the evaporator and the valves to the ton container or tank cars are open, the pressure within the evaporator cylinder will not exceed the pressure in the ton container or tank car.

WARNING: TO AVOID AN OVERPRESSURE CONDITION CA-

PABLE OF RUPTURING THE PIPING SYSTEM AND RESULT-

ING IN A DISCHARGE OF GAS FROM THE GAS PRESSURE

RELIEF SYSTEM, CAUSING POSSIBLE SEVERE PERSONAL

INJURY AND EQUIPMENT DAMAGE, DO NOT CLOSE ANY

SUPPLY VALVE WITHOUT FOLLOWING THE EVACUATION

PROCEDURE FOR LONG-TERM SHUTDOWN IN PARAGRAPH

3.2.3B.

NOTE: Liquid chlorine has a high coefficient of thermal expansion.

WARNING: DO NOT CLOSE VALVES IN SUCH A WAY THAT

LIQUID CHLORINE MAY BE TRAPPED, SINCE DANGEROUS

PRESSURES CAPABLE OF RUPTURING THE PIPING SYSTEM

MAY BUILD UP WITH A SMALL INCREASE IN TEMPERA-

TURE.

(3) Leave the evaporator outlet valve shut for approximately 30 minutes. Under these conditions, most of the liquid chlorine will be forced back to the supply tank through the inlet nipple and the remaining liquid will be evaporated by the heat of the water bath.

At the end of this period, shut the valve at the tank car or the ton container, immediately open the evaporator chlorine outlet valve, and run the chlorinator to exhaust the gas in the evaporator and the gas and liquid in the inlet line. When the evaporator pressure gauge reads zero, the chlorine outlet valve may be closed. If the evaporator pressure gauge shows pressure after the outlet valve has been closed for several minutes, repeat the above procedure until the evaporator pressure gauge reads zero with outlet valve closed. Then turn off power to the control system and alarm units.

47

!

!

!


If no standby evaporator is being used, shut down the chlorinator. Remove the enclosure and the associated hardware.

b. Through the port hole located on top of the hot water tank, examine the visible exterior of the chlorine cylinder with a flashlight. Inspect the surface. If signs of pitting or corrosion are evident, proceed to paragraph 4.13, Five-Year Inspection.



AND BE PREPARED TO RECONNECT UNION QUICKLY IF

THERE IS ANY SIGN OF PRESSURE IN THE GAUGE LINE.

CAUTION: Do not disturb the threaded joint between the pressure gauge and the protecting oil-filled capsule. Any loss of oil will result in a faulty indication by the pressure gauge.

c. Remove the temperature gauge bulb, if furnished, from the well in the cylinder flange. Put on an approved-type gas mask before proceeding. Disconnect the pressure gauge and the chlorine inlet and outlet piping through the unions on the top of the cylinder.

d. Remove the upper cylinder flange cover plate and attached parts.

Note the orientation of the chlorine inlet and outlet pipes.

CAUTION: Do not lose or misplace any of the nuts or brackets when disassembling the upper flange.

e. Examine the interior of the cylinder. Because residues vary widely, it is not possible to describe exactly what may be found. However, it may be expected that the upper portion of the cylinder will be lined with a reddish-brown ferric chloride and the lower portion will contain a mixture of ferric chloride and other residue. This mixture may be solid, liquid, or of some intermediate consistency.

f.

Disconnect the ammonia union at the bottom chlorine inlet.

g. Using the flange PC22627 with nipple P6645, run a one-inch hose line from the bottom chlorine inlet connection to a drain, as shown in

Dwg. 50.200.150.010.

h. Loosen any residual buildup from the internal walls of the cylinder.

IM 50.200AA UA (B/1-01) 48

!

!

IM 50.200AA UA (B/1-01)


i.

Remove riser pipe P42718 from the bottom chlorine inlet and flush the cylinder with water at a minimum of flow of 5 GPM. Continue to flush until the discharge water is clean.

j.

Inspect the interior surface for pitting and corrosion. If pitting exceeds 0.125-inch deep, if deep seated corrosion is apparent, or if cylinder seems to be of questionable condition, either proceed with the five-year inspection procedure (paragraph 4.13) or replace the cylinder and the appropriate components.

k. Thoroughly dry all internal surfaces and items within the cylinder, as any residual moisture will accelerate corrosion once combined with chlorine.

WARNING: ANY MOISTURE, INCLUDING ATMOSPHERIC, IS

HIGHLY CORROSIVE WHEN COMBINED WITH CHLORINE.

TO AVOID SEVERE PERSONAL INJURY AND EQUIPMENT

DAMAGE FROM EXTREME CORROSION, AND POSSIBLE

FAILURE OF THE CYLINDER, IT MUST BE ABSOLUTELY DRY

AFTER CLEANING IS COMPLETED.

l.

Unbolt and remove the bottom chlorine inlet pipe and flange. Remove as much water as possible from the bottom of the cylinder with a rag or sponge to reduce drying time. Dry the bottom chlorine inlet pipe thoroughly by baking or other means.

m. After the cylinder and other parts have been dried thoroughly, replace the riser pipe and the cylinder flange cover plate using a new gasket P42293. Tighten the bolts uniformly.

NOTE: When replacing the cylinder flange cover plate, it is necessary to observe the orientation of the inlet and outlet as stamped on the top of the flange and install accordingly.

WARNING: IF USER OUTLET PIPING IS CONNECTED TO THE

EVAPORATOR INLET PIPE, LIQUID CHLORINE WILL DIS-

CHARGE FROM THE EVAPORATOR, CAUSING EQUIPMENT

DAMAGE AND POSSIBLE SEVERE PERSONAL INJURY.

THEREFORE, ENSURE THAT USER PIPING IS CONNECTED

TO THE EVAPORATOR OUTLET PIPE.

n. Replace the bottom chlorine inlet pipe using a new gasket P12470.

Connect the injector U20230 to the bottom chlorine inlet per Dwg.

50.200.150.010. Install vacuum gauge U10264.

49


o. Turn on the evaporator controls and raise the temperature in the tank to 180°F. Pull a vacuum via the injector and maintain for 1/2 hour at a minimum of 22 inches of mercury.

p. Shut off the vacuum line and observe the vacuum gauge. If a vacuum of 22 inches of mercury or more can be held for one minute, and all parts of the system being dried are heated by the 180°F water bath, no further evacuation is necessary. If not, continue to pull a vacuum until 22 inches of mercury can be held for 1/2 hour.

q. Disconnect the injector and restore the bottom chlorine inlet piping.

Use a new gasket P12470 in the ammonia-type union.

r.

Remove the vacuum gauge and reconnect the chlorine pressure gauge using a new O-ring PXA26482.

s. Refer to paragraph 4.14, Operational Inspection of the Pressure Relief Systems, to test both the gas pressure relief system and the liquid line pressure relief system.

t.

Refer to paragraph 3.1, Preparation For Initial Operation, to put the evaporator back into service.

u. Replace the enclosure and put the evaporator into service.

4.13

Five-Year Inspection of Evaporator Cylinder

This inspection is conducted either every five years, after 12 “in-place” cleanings, or when indicated by step j, paragraph 4.12.

NOTE: Canadian owners of evaporators must comply with local regulations governing periodic inspection and testing of the pressure vessel.

a. Complete steps a through l of the “in-place” cleaning of the evaporator cylinder procedure (paragraph 4.12).

b. Open the hot water tank drain valve just above the circulator water pumps and allow the water to fully drain from the tank.

c. Remove the silicone bead surrounding the cylinder and the hot water tank.

IM 50.200AA UA (B/1-01) 50


4.14

d. Install the top flange and lifting brackets back into the evaporator cylinder. Bolt the brackets securely in place, making sure the brackets are 180 degrees apart.

e. Disconnect the four cylinder mounting bolts beneath the evaporator water tank. Remove the cylinder from the hot water, using the two lifting brackets (see Dwg. 50.200.150.060).

f.

Remove the external scale, etc. Verify that the inside of the cylinder is free of residue.

g. Weigh the cylinder. (Exclude the internal riser, top flange, brackets, bolts, nuts, gaskets, and down-drop pipes.) h. If the present weight is 10 or more pounds less than the original tare weight (stamped on the cylinder), scrap the cylinder and replace it with a new one.

NOTE: Exterior corrosion indicates improper maintenance of the cathodic protection system. Interior corrosion usually indicates the presence of moisture in the cylinder.

i.

Clean, inspect, and replace, as necessary, the hot water tank, temperature switch sensing bulb, overflow outlet, and cathodic protection anodes. If there is any doubt about any component, replace it.

j.

Replace the new or re-tested cylinder into the hot water tank with a new bottom gasket (28, Dwg. 50.200.000.011).

k. Reassemble per steps m through n of the “in-place” cleaning of evaporator cylinder procedure (paragraph 4.12).

Operational Inspection of the Pressure Relief Systems

!

Perform an operational inspection of the pressure relief system before completely re-assembling the evaporator exterior piping. Make the following checks on the pressure relief systems during “in-place” cleaning at the five-year inspection of the chlorine cylinder.

WARNING: TO AVOID THE RELEASE OF CHLORINE INTO

THE ATMOSPHERE, DO NOT REMOVE EITHER PRESSURE

RELIEF SYSTEM WHILE THE EVAPORATOR IS PRESSUR-

IZED. BEFORE ATTEMPTING TO SERVICE THE PRESSURE

RELIEF SYSTEM, FOLLOW STEP A IN PARAGRAPH 4.12.

IM 50.200AA UA (B/1-01) 51


4.14.1

Evaporator Gas Pressure Relief System

a. Carefully remove the rupture disc. Do not damage the surfaces or the remove tape that secures the components together. Check the system components for signs of internal or external corrosion. Replace as necessary.

b. Reassemble safety head (union) without the rupture disc.

c. Pressurize the system at rupture disc connection to 150 psi with dry air, carbon dioxide, or nitrogen. Alarm should activate imediately and pressure should hold. Check for leaks.

d. Test Farris relief valve @560 ±17 psi.

e. Reinstall the rupture disc and pressurize to 150 psi. Pressure should hold. If an alarm sounds or pressure does not hold, replace the disc and retest at 150 psi.

4.14.2


a. Carefully remove rupture disc. If any internal or external corrosion is noted, the expansion chamber must be hydrostatically tested at 840 psig (and cleaned and dried) or replaced. Replace other components as necessary.

b. Reassemble the safety head (union) wihout the rupture disc.

c. Pressurizethe system to 150 psi with dry air, carbon dioxide, or nitrogen. An alarm should activate immediately and the pressure should hold. Check for leaks.

d. Reinstall the rupture disc and pressurize to 150 psi. Pressure should hold. If an alarm sounds or pressure does not hold, replace the disc and retest at 150 psi.

4.14.3

Pressure Alarm Switch

If an alarm does not activate during the relief system test, perform the checks detailed in paragraph 4.4, Relief System Pressure Switches, to determine whether the switch requires adjustment or replacement.

IM 50.200AA UA (B/1-01) 52


4.15

Troubleshooting Guide

NOTE: All symptoms in any given group occur concurrently unless otherwise noted.

Table 4.1 - Troubleshooting

S

G

Y

R

M

O

P T

U P

O

1

M P R O B A B L E C A U S E

L e v i q u i d a p o r a c h l o t o r r i n o u e t l e d i t s c h a a s a r g e d r e s u l t f r o m o f a n y o f t h e f o l l o w i n g c o n d i t i o n s :

( a ) D e m a n d o n e v a p o r a t o r e x c e e d s d e s i g n c a p a c i t y .

C O R R E C T I V E A C T I O N

L I Q U I D C H L O R I N E I N

C H L O R I N A T O R

R O T A M E T E R .

C H L O R I N A T O R

M A T E R I A L

P L A S T I C

D E T E R I O R A T I O N .

C H L O R I N A T O R E R R A T I C .

( a ) R e d u c e c h l o r w i t h d r a w a l r a t e .

i n a t o r g a s

( b ) S u p p

P r o b a b l e l y

C p r e s s u r e a u s e i n t o o h

G r o u p i g h

2 ) .

( s e e ( b )

S e e

R e d u c e

C o r r e c c y t i v e l i n d e r

A c t i p o n r e s s f o r u r e .

H i g h

P r e s s u r e i n G r o u p 2 .

O R r

I n e a d e q s u l t u o f a t e c o n h e a t t a m i t r a n n a n t s f e r a s a b u i l d u p o n i n s i d e o b u i l d u p f c y l i n d e r o n o u t s i a n d / o r d e p o s i t d e o f c y l i n d e r .

O R -

C l o s e s y s t e m , s u p p l y a n d v a s h u t l v e d

, o e v a c u a t e w n .

S e e

L o n g T e r m S h u t d o w n i n S e c t i o n

3 e

.

x t

C l e a n e r i o r .

c y l i n d e r

S e e " I n i n t e r i o

P l a c e " r a n d

C l e a n i n g o f E v a p o r a t o r

4 .

C y l i n d e r i n S e c t i o n l

L o w o w w a t e m t e r p e r a b a t h t u r e t e m p e r a t u r e s w i t c h f a i l i n g w i t h t o c l o s e G P R V * s o u n d a l a r m ,

( o r a n d

V R C U a c t i v a t e

) , p a n e l l i g h t .

( S e e P r o b a b l e C a u s e i n

G r o u p 5 .

)

S e e C o r r e c t i v e

S y m p t o m G r o u p

A c t i o n f o r

5 .

( c ) B y -

G P R V * p a s s

( i f o p e n a r o p r o v i d e d ) .

u n d

( d ) G P R V * ( i f p r o v i d e d ) l e a k i n g p r e s s u r e a c r o s s v a l v e .

( c ) C l o s e b y p a s s .

( d ) C l o s e s u p p l y v a l v e , s y s t e m a n d s h u t d o w n .

e v a c u a t e

S e e

L o n g T e r m S h u t d o w n i n S e c t i o n

3 .

S e e G P R V * i n s t r u c t i o n b o o k f o r v a l v e r e p a i r .

*GPRV - Gas Pressure Reducing Valve; VR-CU - Vacuum Regulator-Check Unit

IM 50.200AA UA (B/1-01) 53


Table 4.1 - Troubleshooting (Cont'd)

S

G

Y

R

M

O

P T

U P

O

2


H i g h p r e s s u r e i n s i d e e v a p o r a t o r c y l i n d e r d f o l l o w i n g : u e t o a n y o f t h e

H I G H P R E S S U R E

R E A D I N G F R O N T P A N E L

G A U G E ( A B O V E 1 4 0 P S I ) .

t

( a ) o o

A i r p a d d e d h i g h .

s u p p l y p r e s s u r e

( I F

4 0 0

P

P

R E

S I ,

S S

R

U R

U P

E

T U

R E A C H E S

R E D I S C

W I L L B U R S T A N D R E L I E F

S Y S T E M

A L A R M

P R E S S U

W I L L B E

R E

A C T I V A T E D .

)

( b ) V a l v e c e v a p o r a t o r l i o s e d n l e t a b e t w e e n n d s u p p l y w i t h e v a p o r a t o r o u t l e t c l o s e d o r c h l o r i n a t i o n s t o p p e d .

( c ) t o

B l o c k a g e i n c o n t a m i n a n t s s u p p l y l i n e w i t h e v a p o r d u e a t o r o u t l e t c l s t o p p e d .

o s e d o r c h l o r i n a t i o n

(

(

C

a b

O

)

)

R

R

O e

R

p d u e

E C

n c e a l

T I

l a i v r

V E

a p l v a d

A

e s d i i

C

n

T

n g s

I

u p

O

r e p p

N

s s l y u r l i n e .

e

( c ) O a v o i d p t r e n a p v a l v e s , p i n g l i a s q u i d r e q u i r e d , i n s u p p l y t o l i n e , e d o w n .

v a c

F o u a t e l l o w s y s t e m a n d

L o n g T e r m s h u t

S h u t d o w n i n S e c t i o n 3 .

s u p p l y l i n e .

C l e a n

G R O U P 3

S U P P L Y L I N E P R E S S U R E

G A U G E ( W H E R E

P R O V I D E D )

M A X I M U M

I S P I N N E D

R E A D I N G .

A T

S U P P L Y L I N E P R E S S U R E

R E L I E F S Y S T E M

A L A R M

P R O V I

*

D E

*

D

( W H E R E

) A C T I V A T E D

W H E

B U R

N

S T

R U P T U R E

S ( A T 4 0 0

D I S C

P S I ) .

E x c e s s i v e p r e s s u r e d u e t o a n y o f t h e c o n d i t i o n s : i n s u p p f o l l o w i n g l y l i n e

( a ) L i q u i d t r a c l o s e d v a l v e s .

p p e d b e t w e e n t w o

( b ) L i q u i d t r a p p e d i n e v a p c y l i n d e r b y c l o s i n g v a l v e a t o r a t o r s u p p l y a n d s t o p p i n g c h l o r i n a t i o n .

C H L O R I N E

F R O M

M A Y

F I T T I N G S

L E A K

A S

P R E S S U R E I N C R E A S E S .

( c c l

) o s

L i e d q u v i d a l v t r a p p e d e a n d a b e t w e e n b l o c k a g e a i n t h e l i n e .

( a ) O p e n a l l v a l v e s i n s u p p l y l i n e .

( b ) E v a c u a t e s y s t e m a n d d o w n .

R e p l a c e r u p t u r e s h u t d i s c .

( c ) a n d

O p e n v a l v e , s h u t d o w n .

e v a c u

F o l l o w a t e

L s y o n s g t e m

T e r m S h u t d o w n i n S e c t i o n 3 .

C l e a n l i n e s .

.

**Alarms will not activate if customer power fails.

IM 50.200AA UA (B/1-01) 54



S Y M P T O M P R O B A B L E C A U S E

G R O U P 4

E V A P O R A T O R P R E S S U R E


P R E S S U R E A L A R M * *

A C T I V A T E S B U T F

P A N E L P R E S S U R E

R O N T

G A U G E

R E A D S

1 4 0 P S I .

B E T W E E N 3 0 A N D

O R -

L I Q U I D L I N E P R


E S S U R E

A L A R M * * A C T I V A T E S B U

L I Q U I D

G A U G E

L I N E P

R E A D S

R

B

E S S

E T

U R E

W E E N

T

3 0 A N D 1 4 0 P S I .

R u p t u r e d i s c l e a k s .


F o l l o w L o p r o c e d u r e n i g n

T e r m

S e c t i

S h u t d o w n o n 3 .

R e p l a c e d i s c .


IM 50.200AA UA (B/1-01) 55



S Y M P T O M P R O B A B L E C A U S E C O R R E C T I V E A C T I O N

G R O U P 5

L O W T E M P E R A T U R E

P A N E L L I G H T O N .

L

A L A R M

A C T I V A T E S .

L

1

T

O W

O W

6 0 ° F )

E M

T E M

R E A D I N

O

P E R

* *

N

P E R A T U R E

P

( I F

A N

P R O V I D E D )

G

E

A T U R E

( B

L

M

E L O W

E T E R .

(

(

(

L o w t a n k w a t e r t e m p e r a t u r e a s a r e s u l t o f a n y o f t h e c o n d i t i o n s : f o l l o w i n g e r a ) v a b ) o t c )

( W

G p o

C a t

S a d m i t a s e s w r o n g o l e n o i d t i n g a t e r r a o v e r f l o w d e t i n g i n w i c l l m a n d c o o c i r c u l a t o r l d b e n v a p p u a l n e w f l v e a t o c t e x c a c d i i t m p w r e c t s e r i y .

t u n i o n .

e e d s s

) i n g t o i o n .

c k p s t o o p o u t t a o n o f r e n k .

( a ) R e d u c e g a s w i t h d r a w a l r a t e .

( b ) C h e c k p u m p m o t o r a n d f w i r i n g .

a u l t y

C o r r e c t w e q u i p m e n t .

i r i n g o r r e p l a c e

( c ) C h e c k s o l e n o i d v a l v e f o r f o r e i g n m a t t e r j a m m i n g v a l v e .

C a n h e d c k w a t c o n t r o l e r c i r l e v e l c u i t .

p r o b e w i r i n g

R e p l a c e e q u i p m e n t , i f f a u l t y .

( d ) C o r r e c t l e a k s .

G P R V * ( O R

C L O S E D .

V R C U )

P

S

O

Y

S

M

S I B

P T

L E

O M

A

S :

D D I T I O N A L

(

( p o d i e ) r

) p i

W n g

H e

.

a c o n t t e r a t e r a c t s l e a k i n g o c o n t a c t o w o r n o u u t r t .

o f t a n k f a i l u r e : o c o i l r

( e ) C h e c k c o i l a n d c o n t a c t s .

R e p l a c e f a u l t y e q u i p m e n t .

L O W

A L A R

W

M

A T

* *

E R L E V E L

( I F P R O V I D E D )

A N D L O W W A T E R L E V E L

P A N E L L I G H T O N ;

N E X T C O L U M N .

S E E ( H )

( f )

1 , 2

H e a t o r e x a l l 3 c h a e l n g e r e m e n m t s a b l f u n c t i o n : u r n o u t o r h e a t e r i s v o l t a g e o r n o p t o o f w e t r h e r a p t i r n o p g .

e r

( f ) C h e c k n a m e p l a t e e l e m e n r a t i n g s .

t s

R a n d e p l a c e e q u i p m e n t .

f a u l t y

( g ) o n c

T e m i r c u p e i t r a t u r e b o a r d c o n t r o l c i r c u i t r y o r t e m p e r a t u r e s e n s o r i n p r o b e h o u s i n g f a i l s i n c o r r e c t l y w i r e d .

o r i s

( g ) C h e c k w i r i n g f a u l t y e q u i p m e n t .

o r r e p l a c e

( h ) s e e

L o w w a t e r

P r o b a b l e C l e v e l c o n d i t i o n , a u s e i n G r o u p 8 .

N O T E : c o n d i t i o n

A f a l s e w o u l d a l a r m e x i s t i f t h e l o w t e m p e r a t u r e i s n o t s e t t o t e m p e r a t u r e

1 6 0 ° F o r a a l a r m s w i t c h f a i l s .

a l a r m s w i t c h

( h ) S e e C o r r e c t i v e A c t i o n f o r

S y m p t o m , G r o u p 8 .

R e p l a c e a s s e m b l y .

t e m p e r a t u r e s w i t c h



IM 50.200AA UA (B/1-01) 56



S

G

Y

R

M

O

P T

U P

O

6


H i g h t a n k r e s u l t o f : w a t e r t e m p e r a t u r e a s a


H I

P A

G H

N E L

T E M P E R A T U R E

L I G H T O N .

H I G H T E M P E R A T U R E

A L A R M * * (

A C T I V A T E S .

I F P R O V I D E D )

( a ) T e b o a r d m f a p e r a t u r e i l s o r i s c o n t r o l o n i n c o r r e c t l y c i r c u i t w i r e d .

( a ) R e p l a c e f a u l t y e q u i p m e n t o r c o r r e c t w i r i n g .

( b ) T e m p e r a t u r e c o n t r o l s e n s o r i n p r o b e h o u s i n g f a i l s o r i s i n c o r r e c t l y w i r e d .

( b ) R e p l a c e f a u l t y e q u i p m e n t o r c o r r e c t w i r i n g .

H E A T E X C H A N G E R O F F .

N O T E : c o n d i t i o n

A f a l s e w o u l d a l a r m e x i s t i f t h e h i g h t e m p e r a t u r e i s n o t s e t t o t e m p e r a t u r e

2 0 0 ° F o r a a l a r m s w i t c h f a i l s .

a l a r m s w i t c h

R e p l a c e a s s e m b l y .

t e m p e r a t u r e s w i t c h

( A L A R M A N D P A N E L

L I G H T M A Y S W I T C H O N

A N D O F F P E R I O D I C A L L Y

D U E T O

A N D

T H E C O O L I N

R E H E A T I N G O F

G

T H E

W A T E R A B O U T T H E

S W I T C H S E T P O I N T .

)

G R O U P 7

L O W W A T E R L E V E L

P A N E L L I G H T O N .

L O W W A T E R L E V E L

A L A R M * * (

A C T I V A T E S .


H E A T E X C H A N G E R

C I R C U L A T O R O F F .

A N D

(

(

( a ) f f

L o w w a t e r l e v e l c o n d i t i o n a s a r e s u l t o f a n y o f t h e f o l l o w i n g : a b a c i

)

) u l l e t

W d

S

L y .

.

a t o l e e a e r k ( s s ) u n o i d i p p n v a l y t a l v e b n k l o c o c k l o r e d g g e d p i p o r o i n g .

r (

(

( s a u b c

)

)

) p

C p

C

C l l e y .

l e o r a n a n r e o o c t u t r l e r p a k i p e p

( s i n l a

) .

g .

c e f

R a e u l s t t y o r v e

G P R V * ( O R

C L O S E D .

V R C U )

W A T E R L E V E L I N S I G H T

G L

V I S

A S

I B

S

L

L

E

O W

A T

O R

A L L .

N O T

( d ) D r a i n v a l v e i s o p e n o r l e a k i n g .

( e ) C o n t r o l f o r a u t o m a t i c w a t e r r e f i l l f a i l s a r e i n c o r o r e r w c t l y a t e r l e w i r e d .

v e l p r o b e s

(

( c d e h

)

) e

C

R c k l o e p s w e l a i r o c e i n r g .

f r a e p u l l a t y c e c o

P O S S I B L E A D D I T I O N A L

S Y M P T O M : L O W W A T E R

T E M P E R A T U R E A L A R M * *

( I F P R O V I D E D )

P A N E L L I G H T

A N D

A C T I V A T E .



IM 50.200AA UA (B/1-01) 57

v a l v e .

n t r o l s o r a l v e .



S Y M P T O M P R O B A B L E C A U S E

G R O U P 8

H i g h w a t e r l e v e l a s a r e s u l t o f a n y o f t h e f o l l o w i n g c o n d i t i o n s :

W A T E R C O M I N G O U T O F

O V E R F L O W C O N N E C T I O N

A N D / O R S P I L L I N G O V E R

T A N K T O P O N T O F L O O R .

( a ) F o r e i g n m a t e r i a l j a m m i n g s o l e n o i d v a l v e o p e n .

( b ) F a u l t y s o l e n o i d v a l v e .

S I G H T G L A S S I N W A T E R

L E V E L

F U L L O

I N

R

D I C A T O R I S

N E A R L Y F U L L .

P O S S I B L E A D D I T I O N A L

S Y M P T O M S : L O W W A T E R

(

T E M P E R A T U R E


A L A R M * *

A N D

P A N E L L I G H T A C T I V A T E .

( f c a i w

) i r l u i

A r e n g u t

.

o m o r a t i c i n c o r w a t r e c t e r l r e e v f i l l e l p c i r r o c u i t b e


( a ) C l e a n s o l e n o i d v a l v e .

( b ) R e p l a c e v a l v e .

( c ) R e p l a c e f a u l t y c o n t r o l s o r c h e c k w i r i n g .


IM 50.200AA UA (B/1-01) 58


WARNING LABELS AND TAGS

The following warning labels and tags are attached to the equipment.

------------------------------------------------------------------------------------

L1967: HAZARDOUS GAS IS PRESENT IN THIS EQUIPMENT

DURING NORMAL OPERATION. TO AVOID POSSIBLE

SEVERE PERSONAL INJURY OR DAMAGE TO THE

EQUIPMENT, READ THE WALLACE AND TIERNAN

INSTRUCTION BOOK AND THE APPROPRIATE GAS

MANUAL BEFORE CONNECTING THIS EQUIPMENT

TO A SUPPLY OF GAS. OPERATION AND MAINTE-

NANCE OF THIS EQUIPMENT MUST BE RESTRICTED

TO TRAINED, QUALIFIED PERSONNEL WHO ARE

COMPLETELY FAMILIAR WITH THESE INSTRUC-

TIONS.

------------------------------------------------------------------------------------

L2716: DO NOT REMOVE THIS TAG. FACTORY ASSEMBLED

UNITS INCLUDE EITHER A PRESSURE RELIEF DE-

VICE OR EXPANSION CHAMBER TO SATISFY THE

REQUIREMENTS OF ASME CODE, CHLORINE INSTI-

TUTE AND/OR RECOMMENDED PRACTICES OF THE

COMPRESSED GAS ASSOCIATION. TO MAINTAIN

PROPER OPERATION OF THESE ASSEMBLIES IT IS

ESSENTIAL THAT THE FOLLOWING PRECAUTIONS

BE OBSERVED.

A. Do not disassemble the protective diaphragm (3) from pressure switch (4).

B. The rupture disc (5) is pressure rated for its particular service. Should replacement be necessary, an identical unit must be ordered & installed.

C. See the USF/W&T Instruction Book furnished for parts ordering information and for further detailed operating instructions.

------------------------------------------------------------------------------------

L2016: TO AVOID POSSIBLE SEVERE PERSONAL INJURY

FROM ELECTRICAL SHOCK TURN POWER OFF BE-

FORE SERVICING.

------------------------------------------------------------------------------------

L2257: TO AVOID POSSIBLE PERSONAL INJURY FROM

ELECTRICAL SHOCK, TURN POWER OFF BEFORE

SERVICING.

------------------------------------------------------------------------------------

IM 50.200AA UA (B/1-01) 59


WARNING LABELS AND TAGS (CONT'D)

IM 50.200AA UA (B/1-01)

------------------------------------------------------------------------------------

L3397: LINE VOLTAGE PRESENT AT THIS LOCATION EVEN

WHEN THE PANEL POWER SWITCH IS IN THE OFF

POSITION. TO AVOID POSSIBLE SEVERE PERSONAL

INJURY DUE TO ELECTRICAL SHOCK, DISCONNECT

EXTERNAL POWER SUPPLY BEFORE SERVICING.

------------------------------------------------------------------------------------

L2833: TO AVOID POSSIBLE SEVERE PERSONAL INJURY

DUE TO HIGH TEMPERATURE CAUSING BURNS,

DISCONNECT POWER AND ALLOW TO COOL BE-

FORE HANDLING.

------------------------------------------------------------------------------------

L2720: CHLORINE, WHICH IS A HAZARDOUS CHEMICAL,

IS PRESENT IN THIS EQUIPMENT DURING NORMAL

OPERATION. TO AVOID POSSIBLE SEVERE PER-

SONAL INJURY OR DEATH, YOU MUST OBSERVE

THE FOLLOWING PRECAUTIONS:

1. When changing chlorine supply containers you must be completely familiar with your local plant operating and emergency procedures including the location and use of a gas mask. Recommended emergency procedures can be obtained from your chlorine supplier, the Chlorine

Institute, Inc., or similar organization.

2. Do not open the chlorine supply container valve more than one complete turn. This will permit maximum discharge and can be turned off quickly in the event of a leak.

3. On a routine daily basis, starting at the chlorine supply container(s), thoroughly check all joints, connections and equipment for possible chlorine leaks and immediately correct any found. Do not tolerate any chlorine leaks.

4. Chlorine leaks never get better. Chlorine leaks always get progressively worse, if they are not promptly corrected.

5. Never re-use gaskets in chlorine piping systems. Always have an adequate supply on hand and always use new gaskets of the correct size and material as identified on the equipment parts drawings.

6. Except in cases of leak detection or calibration adjustments, the chlorine supply must be shut off at the supply container valve(s) and the chlorine in the system completely exhausted before servicing the equipment.

60


WARNING LABELS AND TAGS (CONT'D)

7. It is recommended practice to have an approved gas mask available, which you have been trained to use, when making chlorine leak checks and when changing chlorine supply containers.

8. The USF/W&T instruction book provided with this equipment furnishes complete and detailed instructions for its installation, operation and maintenance and must be referred to for that detailed information.

9. The USF/W&T instruction book provided with this equipment also furnishes technical information on the characteristics, storage and handling of chlorine, and must be referred to for that information. Contact your chlorine supplier, the Chlorine Institute, Inc., or similar organization to obtain more detailed information.

10. Operation and maintenance of this equipment must be restricted to trained, qualified personnel who are completely familiar with these instructions.

11. Liquid chlorine has a high temperature coefficient of expansion. Do not close valves in such a way that liquid chlorine may be trapped since dangerous pressures capable of rupturing the piping system may build up with a small increase in temperature.

To avoid possible severe personal injury from electrical shock, turn power off before servicing this equipment.

DO NOT REMOVE THIS SIGN FROM THIS EQUIP-

MENT

------------------------------------------------------------------------------------

IM 50.200AA UA (B/1-01) 61


CAUTION LABELS AND TAGS

The following caution labels and tags are attached to the equipment.

------------------------------------------------------------------------------------

L2558: FOR CHLORINE USE ONLY.

------------------------------------------------------------------------------------

L2717: UNDER NORMAL OPERATING CONDITIONS DEPOS-

ITS WILL ACCUMULATE IN THE EVAPORATOR CYL-

INDER AND OVER A PERIOD OF TIME WILL REDUCE

ITS OPERATING CAPACITY. FOR THIS REASON PE-

RIODIC CLEANING IS REQUIRED TO REMOVE THESE

DEPOSITS. THE INSTRUCTION BOOK PROVIDED

WITH THIS EQUIPMENT PROVIDES COMPLETE DE-

TAILS ON RECOMMENDED FREQUENCY AND PRO-

CEDURES TO PROPERLY ACCOMPLISH THIS

CLEANING AND MUST BE REFERRED TO FOR THAT

GUIDANCE.

------------------------------------------------------------------------------------

L2135: DO NOT DISCONNECT THIS SEAL ASSEMBLY FROM

GAUGE. SEAL PROOF PRESSURE 840 P.S.I.

------------------------------------------------------------------------------------

L2137: DO NOT DISCONNECT THIS SEAL ASSEMBLY FROM

PRESSURE SWITCH. SEAL PROOF PRESSURE 840

P.S.I.

------------------------------------------------------------------------------------

L3222: TO PREVENT DAMAGE TO EQUIPMENT, ALWAYS

REPLACE COVER AFTER SERVICING.

------------------------------------------------------------------------------------

IM 50.200AA UA (B/1-01) 62


IM 50.200AA UA (B/1-01) 63

SERIES 50-200 EVAPORATOR - WIRING

Cathodic Protection

50.200.140.010

ISSUE 1 1-90


NOTE: X


!

PART OF U28839 SPARE PARTS KIT.

"

PART OF CYLINDER & NOT INCLUDED IN U20208.

"

PART OF INJECTOR ASSEMBLY U20230, WHICH MAY BE ORDERED SEPARATELY.

IM 50.200AA UA (B/1-01)

U20208 DRYING KIT FOR SERIES 50-200 EVAPORATOR - SERVICE

50.200.150.010

ISSUE 1 12-91

64


WARNING:

"

TO AVOID POSSIBLE SEVERE PERSONAL INJURY AND EQUIPMENT DAMAGE, DO NOT

NOTE:

ATTEMPT TO LIFT EVAPORATOR BY INLET AND OUTLET CONNECTIONS.

X


LIFTING METHOD - SERVICE

50.200.150.060

ISSUE 0 4-88

IM 50.200AA UA (B/1-01) 65

50-200 EVAPORATOR FOR CHLORINE 50-200 EVAPORATOR FOR CHLORINE

IM 50.200AA UA (B/1-01) 66 IM 50.200AA UA (B/1-01) 67

LEVEL AND TEMPERATURE CONTROL

- SCHEMATIC WIRING

50.200.155.020

ISSUE 2 4-91

50-200 EVAPORATOR FOR CHLORINE 50-200 EVAPORATOR FOR CHLORINE

IM 50.200AA UA (B/1-01) 68 IM 50.200AA UA (B/1-01)

SERIES 50-200 EVAPORATOR - SCHEMATIC WIRING

Controls and Equipment

50.200.155.010

ISSUE 3 4-91

69


IM 50.200AA UA (B/1-01) 70


SECTION 5 - ILLUSTRATIONS


DRAWING NO.

Parts

Evaporator - Basic Components ........................ 50.200.060.010A-E

Water Level and Temperature Control Probes .. 50.200.000.020A&B

AAA8723 Controls Enclosure ........................... 50.200.060.020A-C

AAA9083 Enclosure .......................................... 50.200.060.030A&B

U27615 Liquid Line Pressure Relief System .... 50.202.007.011

U25471 Gas Pressure Relief System ................. 50.202.008.011

Line Valves ........................................................ 50.150.005.011

IM 50.200AA UA (B/1-01) 71


NOTES:

FOR DETAILS, SEE DWG. 50.200.060.010B.

FOR PARTS LIST, SEE DWGS. 50.200.060.010C,D&E.

AAA8693 - STANDARD CYLINDER;

AAA8651 - "L" CERTIFIED CYLINDER

SERIES 50-200 EVAPORATOR - PARTS

50.200.060.010A

ISSUE 1 1-01

IM 50.200AA UA (B/1-01) 72


NOTES:

FOR PARTS LIST, SEE DWGS. 50.200.060.010C,D&E.

AAA8693 - STANDARD CYLINDER; AAA8651 - "L" CERTIFIED CYLINDER

SERIES 50-200 EVAPORATOR - PARTS

50.200.060.010B

ISSUE 1 1-01

IM 50.200AA UA (B/1-01) 73


4 0

4 1

4 2

4 3

4 4

4 5

4 6

4 7

3 5

3 6

3 7

3 8

3 9

3 1

3 2

3 3

3 4

4 8

5 0

5 1

U 2 2 4 1 8

P 5 9 1 9 1

U C

P C

4 9 8 4

4 7 3 2 9

P 5 9 1 1 3

P 5 7 5 7 8

P X A 5 8 1 5 0

P

P

5 1 2 4 7

1 2 4 7 0

P C 8 5 5

P C

P 4

1 0

2 2

9 1

3 4

U 2 9 0 9 8

U 2 5 4 5 1

O R

P A R T N O .

P

P

5 9 1 8 6

5 9 1 8 8

P X D 5 2 5 9 2

P

P

1 7 1 3 3

5 0 1 7 2

P 5 3 7 0 6

U 2 8 6 2 5

P 4 7 5 9 6

P 2 3 9 9

U 2 3 0 1 2

P 1 5 4 8 3

P 6 8 3

U 2 3 0 1 3

U 2 3 9 0 7

P 4 7 5 9 9

U 2 3 0 2 2

U 2 7 6 1 9

P 4 7 5 2 9

P C

P C

8 6 9

1 0 9 0

P 8 3 3 4

P C

P 3

8 8

5 6

8

7 0

U 2 4 9 1 3

U 2 8 6 6 9

P C 4 7 1 9

P C

P 6 3

1 0 8

3 7

9

P 4 4 8 2 0

U 2 2 7 6 3

P 4 8 2 5 8

P C

P 4

5 9

8 2

4 9

9 5

1

P C 1 3 5 7 3

P C 1 0 6 2

U 2 2 4 4 3

P C 4 7 6 3

2 2

2 3

2 4

2 5

2 6

1 7

1 8

1 9

2 0

2 1

2 7

2 8

2 9

3 0

9

1 0

1 1

1 2

1 3

1 4

1 5

1 6

K E Y N O .

1

2

3

4

5

6

7

8

Q T

2

1

2

1

1

1

1

1

1

2

2

2

1

5

1

3

4

3

1

2

1

2

1

1

1

3

1

1

2

1

1

4

4

1

1

1

1

1

4

8

8

2

2

2

6

4

2

2

2

2

1

0

6

0

6

0

2

0

Y .

I N S U L A T I O N

I N S U L A T I O N S U P P O R T

S

U

9

T R

9 0 °

N I P

E

P

L B

L E

O

( I

W

R O

( I R O N )

N ) 1 ¼ "

1 ¼

S C

"

H

N P T

.

4 0 P I P E x ¾ "

C O U P L I N G ( I R O N ) 1 ¼ " N P T

U N I O N , 1 ¼ "

T E E

C L O S E

N

9 0 ° E L B O W

½ " S O L E N O

A D A P T E R

I D

( B R

V A L V E

A S S ) ½ " S O L D E R C U P

U N I O N , ¾ " N P T ( I R O N ) x ¾ "

S E L F T H R E A D I N G N U T

W A S H E R

G A S K E T

E V A P O R A T O R

C Y L I N D E R ( U S E D

C Y L I N

0 °

I O

A P

E

( C O P P E R ) 1 ¼ "

N

L

,

D E R ,

B

N I

1

O

"

P

N P T

W

'

P

( C O P P E R ) 1 "

L

(

N P T ( I R O N ) x 1 ¼ "

L

'

B

E

( I

( I R O N ) x 1 "

R O N

T A N K

)

O N A A A 8 6 3 9 )

C E R T I F

R A S S )

S O L D E R

I x

1

E

"

1

D

"

( U S E

S O L D E R C U P

D

L G .

O N A A A 8 6 5 1 )

F T G x 1 " C

B O L T ( H E X .

H D .

, S T E E L ) 3 / 8 " 1 6 x 1 " L G .

3 / 8 " W A S H E R ( S T E E L )

3 / 8 " L O C K W A S H E R ( S T E E L )

C L A M P I N G N U T ( S T E E L ) 3 / 8 " 1 6

9 0 ° S T R E E T E L B O W ( I R O N ) ¼ " M P T x ¼ " F P T

C O N N E C T O R ( P O L Y ) ½ "

C O N N E C T O R ( P O L Y ) ½ "

T U B E

T U B E x ¼ " x 1 / 8 "

N P T

N P T

B O L T ( H E X .

H D .

, S T E E L ) ¼ " 2 0 x ¾ " L G .

¼ "

¼ "

W A S H E R ( S T E E L )

L O C K W A S H E R ( S T E E L )

L O C K N U T , 1 ¼ " C O N D U I T

S

B

E A L

U S H I

R

N

I N

G ,

G , 1 -

1 ¼ "

¼ " C O N D U I T

C O N D U I T

N I P P L E , 1 ¼ " C O N D U I T

C O U P L I N G ( C O N D U I T ) 1 ¼ " N P T

N I P P L E 1 " N P T

5 / 1 6 " W A S

C L A M P I N G

H E R

N U T

( S T E E L )

( S T E E L ) 5 / 1 6 " 1 8

5 / 1 6 " L O C K W A S H E R ( S T E E L )

D E S C R I P T I O N

( C O P P E R )

S

S O L D E R C U P

O L D E R C U P

( B R A S S )

( B R A S S )

S O L D E R

C L O S E

U N I O N ,

N I

½ "

P P L E

N P T ( I

( I R O N ) ½ "

R O N ) x ½ "

S C H .

4 0 P I P E

S O L D E R x 2 " L G .

x ½ " N P T

S O L D E R C U P ( B R A S S )

¾ " V

T E E

A

(

L V E ,

C O P

C

P E

O M

R )

P R E S

1 ¼ " C

S I x

O N

¾ " C

S T O P x 1 ¼ " C

U N

9 0 °

I O

E

N ,

L B

1

O

" A M M O N I A

W ( S T E E L ) 1 "

K I C K P L A T E

N P T

B O L T ( H E X .

H D .

, C A D .

P L A T E S T E E L ) 5 / 8 " 1 1 x 3 ½ " L G .

E L B O W B L O C K

G A S K E T

B O L T ( H E X .

H D .

, C A D .

P L A T E S T E E L ) ½ " 1 3 x 1 ¼ " L G .

WHEN ORDERING MATERIAL, ALWAYS SPECIFY MODEL AND SERIAL NUMBER OF APPARATUS.

IM 50.200AA UA (B/1-01)


SERIES 50-200 EVAPORATOR - PARTS LIST

50.200.060.010C

ISSUE 0 12-97

74


8 8

8 9

9 0

9 1

9 3

9 4

9 5

9 6

9 7

# !

9 8

# !

9 9

# !

1 0 0

8 3

8 4

8 5

8 6

"

8 7

7 8

7 9

8 0

8 1

8 2

"

6 6

"

6 7

"

6 8

6 9

7 0

7 1

7 2

7 3

7 4

7 5

7 6

K E Y N O .

5 3

5 5

5 6

5 7

5 8

5 9

6 1

6 2

6 3

6 4

6 5

P A R T N O .

P C 8 7 4

P C 2 9 9 8

P 5 9 9 9 7

P 5 9 1 7 1

P 4 2 2 7 9

P C 4 2 2 8 1

A A A 8 6 4 8

P 5 9 1 9 5

P 5 9 1 4 5

U 2 8 6 7 3

P X A 2 6 4 8 2

"

P

O R

2 6 4 8 2

P 3 1 8 0 3

P 4 5 1 8 8

P E 2 5 8 7

P 5 9 0 2 4

P E 2 5 8 7

P 4 5 1 8 8

A A A 8 6 4 5

-

L 2 0 9 7

U 2 8 6 5 1

U 2 8 9 9 3

P

P

1 5 3 5 6

2 7 3 8 3

P

P

4 7 6 6 2

5 9 1 1 4

P 5 9 2 2 4

P C 3 4 0 3 8

U 2 8 5 8 6

P

L

4 8 7 2

2 0 9 8

6

U 2 5 9 1 2

O R

U X A 2 5 9 1 2

P

P

5 9 1 7 8

5 9 1 7 5

P 5 9 1 7 3

U 2 9 0 0 7

A A A 8 7 2 6

A A A 5 7 2 9

A A A 5 7 3 5

P 5 8 2 1 5

U 1 9 8 1 2

L 2 0 2 2

L 3 2 2 2

L 2 8 3 3

1

2

1

7 F T .

1

1

1

1

1

2

2

1

2

2

2

1

1

1

1

1

2

1

1

4

1

1

2

1

2

Q T Y .

1 4

4

4

1

B O L T

B O L T

C A P L

U N I O N

( H E X .

H D .

, S T E E L )

( H E X .

H D .

, S T E E L )

S U P P O R T

U G

C H A N N E L

A D A P T E R ,

L E F T H A N D

I N S U L A T O R

O R I N G

G A U G E

G A U G E

N U T

# 1 0

( B R

B R A C K E T

B R A C K E T

A S S )

¼

L O C K W A S H E R

I N L E T L A B E L

H E A T E R B O D Y

P U M P G U A R D

"

S U P P O R T C H A N N E L

( 0 1 2 ) B U N A N ,

N U T ( B R A S S ) # 1 0 3 2

# 1 0 3 2

N P

5 / 1 6 " 1 8

3 / 8 "

T E M P E R A T U R E S W I T C H

T

# 1 0 L O C K W A S H E R ( S .

S .

)

( S .

S .

)

9 0 °

N I P

E

P

L B

L E

O W

( I R O

( I R O N )

N ) 1 ¼ "

1 " N P T

N P T

9 0 ° E L B O W ( C O P

P I P E I N S U L A T I O N

P E R ) 1 " C

1 6 x x 1 "

3 / 8 " x 5 / 8 " 1 8

D

9 0 ° S T R E E T E L B O W ( S T E E L ) ¼ " M P T

S U P P O R T A N G L E

T U B E U N I T

O R I N G ( 0 1 2 ) V I T O N , 3 / 8 " I D x 1 / 2 " O D

3 / 8 " I D

E

L

L

S C

G .

G .

R I P T

x ¼ " F P T

I O N

x 1 / 2 " O D ( F O R A M M O N I A

R I G H T H A N D S U P P O R T A N G L E

W A T E R L E V E L C O N T R O L C O M P O N E N T S

U S E O N L Y )

( R E F .

D W G .

5 0 .

2 0 0 .

0 0 0 .

0 2 0 )

M A C H .

S C R E W ( S T E E L , R D .

, H D .

) 1 0 2 4 x 3 / 8 " L G .

C E N T R I F U G A L P U M P

4 5 ° E L B O W ( C O

O U T L E T L A B E L

P P E R ) 1 ¼ " C

G A S P R E S S U R E G A U G E ( C H L O R I N E U S E O N L Y )

1

2

1

8 ' 7 1 3 / 1 6 "

1

1

1

1

1

1

2

1

1

G A S P R E S S U R E G A U G E ( A M M O N I A & S U L F U R D I O X I D E U S E O N L Y )

G A S K E T

N A M E P L A Q U E

" U " C H A N N E L , E X T R U D E D R U B B E R

P U R G E M E T E R

C O N T R O L E N C L O S U R E ( R E F .

D W G .

5 0 .

2 0 0 .

0 6 0 .

0 2 0 )

L O G O ,

F R O N T

F R O N T

P A N E L ,

P A N E L , U P P E R

L O W E R

M A S K

G A S T E M

W A R N I N G

P E R A T U R E

L A B E L

G A U G E

C A U T I O N L A B E L

W A R N I N G L A B E L




50.200.060.010D

ISSUE 0 12-97

IM 50.200AA UA (B/1-01) 75


K E Y N O .

"

1 0 1

!

1 0 2

!

1 0 4

#

1 0 5

#

1 0 6

#

1 0 7

#

1 0 8

#

1 0 9

1 1 0

1 1 1

U X H 2 8 6 3 8

O R

U X J 2 8 6 3 8

O R

U X K 2 8 6 3 8

O R

U X L 2 8 6 3 8

O R

U X M 2 8 6 3 8

P

P

4

5

8

2

2

8

5

1

7

7

U 2 8 9 7 8

P 5

P C

9 7

2 9

9 4

7 7

P

P

5

5

3

9

0

7

9

9

9

3

P 3 0 7 6 0

U 1 9 9 6 7

P A R T N O .

U X A 2 8 6 3 8

O R

U X B 2 8 6 3 8

O R

U X C 2 8 6 3 8

O R

U X D 2 8 6 3 8

O R

U X E 2 8 6 3 8

O R

U X F 2 8 6 3 8

O R

U X G 2 8 6 3 8

O R

Q T Y .

1

1

1

1

1

1

1

1

1

1

1

4

4

1

1

1

1

1

1

1

1

H E A T E X C H A N G E R ( 2 0 8 V O L T S ,


6 0 A M P )

H E A T E X C H A N G E R ( 2 2 0 / 2 4 0 V O L T S , 6 0 A M P )

H E A T E X C H A N G E R ( 3 8 0 V O L T S , 3 0 A M P )


H E A T E X C H A N G E R ( 5 5 0 V O L T S , 3 0 A M P ) 8 , 0 0 0 P C D





H E A T E X C H A N G E R ( 5 5 0 V O L T S , 3 0 A M P ) 1 0 , 0 0 0 P C D


H E A T E X C H A N G E R ( 3 0 8 V O L T S ,

1 " C O N D U I T B U S H I N G

3 0 A M P )

G A S K E T

H E A T E R C O V E R

H E A T E R C O N N E C T O R A N G L E

B O L T ( H E X .

H D .

, S T E E L )

S H E E T M E T A L

C O V E R P L A T E

S C R E W

½ " 1 3 x ¾ "

( O V A L H D .

L G .

S T E E L )

G R O M M E T

K N O B

# 1 0 X 1 / 2 " L G .

1 2 0

1 2 1

1 2 2

1 2 3

1 2 4

1 2 5

1 2 6

1 2 7

1 1 2

1 1 3

1 1 4

1 1 5

1 1 6

1 1 7

1 1 8

1 1 9

1 2 8

1 2 9

1 3 0

P

P

P

P

P C 5 6 6 5

3 0 7 5 8

3 0 7 6 4

5

5

9

9

0

0

5

5

4

3

P 5

P C

9 0

1 2

5 5

6 1 5

P C

P 5

1 8

9 4

1 4

7 7

1

P C 5 9 1 9 2

P

P

4

4

8

8

2

2

1

2

8

0

U 1 6 1 1 6

U 2 2 7 6 0

U 2 0 6 3 3

U 1 9 9 7 4

P

P

4 8 2 0 4

2 7 1 8 6

P 4 8 2 5 7

5

5

1

1

2

2

3

1

2

1

1

2

1

2

1

1

1 4

4

4

¼ " W A S H E R ( S T E E L )

W A S H E R ( B R A S S )

A N O D E

T A N K I N S U L A T I O N ( R E A R )

T A N K

T A N K I

I N

N

S

S

U

U

L

L

A

A

T

T

I

I

O

O

N

N

(

(

R

L

I G

E F

H

T

T

)

)

# 1 0 L O C K W A S H E R ( S T E E L )

# 1 0 W A S H E R ( S T E E L )

G R O M M E T

N I P P L E ( S T E E L ) 1 " S C H .

8 0 P I P E 9 ¼ " L G .

C O N D U I T C O V E R

C O N D U L E T G A S K E T

½ " S E A L

O R I N G

T I T E

A N D

U N I O N

R E T A I N E R C O N D U I T

4 5 °

½ "

½ "

C O N N E C T O R

B

E L

O

B O

D Y

W

O

,

U

½ "

T L

F L E X I B L E

E T C O N D U I

C O N D U I T

T

N I P P L E (

B U S H I N G

G A L V A

C O N D

N I Z E

U I T

D )

1 "

½ " C O N D U I T 1 1 / 8 " L G .

1 3 2 U 2 1 8 6 6 2 4 5 ° E L B O W , 1 " F L E X I B L E C O N D U I T

NOTE:

"

PART OF G678.

!

PART OF G2343.

#

PART OF G2344.

"

NOT PART OF AAA8639 OR AAA8651.

ALL STEEL PIPING IS 1” (SCHEDULE 80) AS PER ASTM 1-106, GRADE B.

ALL POLYPROPYLENE TUBING IS 1/2” O.D. x 1/16” WALL (WORKING PRESSUE: 250 PSI).

ALL COPPER TUBING IS ½”, ¾”, 1”, OR 1-¼” (SEAMLESS, TYPE M) AS PER ASTM B-88 OR EQUIVALENT.

ALL FLEXIBLE CONDUIT IS ½” OR 1” (STEEL, LIQUID TIGHT) WITH APPROPRIATE CONNECTORS AND FITTINGS (MEETS JIC REQUIRE-

MENTS).


IM 50.200AA UA (B/1-01)


50.200.060.010E

ISSUE 0 12-97

76


NOTE: FOR PARTS LIST, SEE DWG. 50.200.000.020B.

IM 50.200AA UA (B/1-01)

WATER LEVEL AND TEMPERATURE CONTROL PROBES - PARTS

For Series 50-200 Evaporator

50.200.000.020A

ISSUE 0 4-88

77



WATER LEVEL AND TEMPERATURE CONTROL PROBES - PARTS LIST

For Series 50-200 Evaporator

50.200.000.020B

ISSUE 0 4-88

IM 50.200AA UA (B/1-01) 78


NOTES:

FOR PARTS LIST, SEE DWGS. 50.200.060.020B&C.

AAA8723 CONTROLS ENCLOSURE - PARTS

50.200.060.020A

ISSUE 0 12-97

IM 50.200AA UA (B/1-01) 79


K E Y N O .

1

"

2

3

5

8

9

6

7

1 0

1 1

1 2

1 3

1 4

1 5

1 6

1 7

"

1

1

2

2

2

2

2

2

8

9

0

1

2

3

4

5

P 5 9 1 5 9

P 3 7 5 4 6

P 2 2 6 1 6

P 1 5 3 6 3

U 2 8 5 8 4

O R

"

U 2 8 5 8 3

P 4 0 5 9 5

P 5 9 1 6 0

P 5 9 1 8 1

L 3 2 9 5

O R

L 3 2 9 9

O R

L 3 3 3 0

O R

L 3 2 9 6

O R

L 3 3 0 1

O R

L 3 2 9 4

O R

L 3 2 9 7

U 2 8 6 2 0

P 4 2 9 4 2

P 1 9 8 8 8

P 1 4 6 3 5

P A R T N O .

U 2 8 6 2 6

U 2 8 6 2 9

U 2 8 6 2 7

U 2 8 5 9 2

P 5 9 1 7 9

U 2 8 5 9 3

U 2 8 6 2 8

U 2 5 7 2 0

U 2 8 6 1 9

U 2 0 8 9 4

A A A 8 7 2 6

1

6

6

1

1

6

1

1

1

4

1

1

1

1

1

1

1

1

8

8

1

4

1

Q T Y .

2

4

2

1

1

1


I N D I C A T O R L I G H T , R E D

L A M P

I N D I C A T O R L I G H T , A M B E R

T E M P M E T E R

G A S K E T

A M M E T E R

I N D I C A T O R L I G H T , G R E E N

O P E R A T I N G H A N D L E

P O T E N T I O M E T E R

K N O B

C O N T R O L B O X

T R A N S F O R M E R M O U N T I N G P A N E L

M A C H .

S C R E W ( R D .

H D .

, S .

S .

) 5 / 1 6 " 1 8 x 1 / 2 " L G .

5 / 1 6 " W A S H E R ( S .

S .

)

5 / 1 6 " L O C K W A S H E R ( S .

S .

)

T R A N S F O R M E R ( 2 4 0 / 4 8 0 V O L T S )

T R A N S F O R M E R ( 2 0 8 , 3 8 0 , 5 5 0 , 2 2 0 , & 4 4 0 V O L T S )

M A C H .

S C R E W ( H E X

M O U N T I N G P L A T E

H D .

, S .

S .

) 5 / 1 6 " 1 8 x 1 " L G .

C O N N E C T O R , L O C K T I T E

M A R K E R ( 2 0 8 V )

1

1

M

M

A R

A R

K E

K E

R

R

(

(

2

2

2 0

4 0

V )

V )

M

M

M

A R

A R

A R

1 / 4 "

1 / 4 "

K E

K E

K E

R

R

R

(

(

(

3

4

4

8 0

4 0

8 0

W A S H E R

V )

V )

V )

M A R K E R ( 5 5 0 V )

D I S C O N N E C T S W I T C H

M A C H .

S C R E W ( H E X

( S .

S .

)

H D .

, S .

S .

)

L O C K W A S H E R ( S .

S .

)

1 / 4 " 2 0 x 5 / 8 " L G .

NOTE:

"

PART OF KEY NUMBERS 1, 3 OR 8.

"

NOT PART OF AAA8723.


IM 50.200AA UA (B/1-01)

AAA8723 CONTROLS ENCLOSURE - PARTS LIST

50.200.060.020B

ISSUE 0 12-97

80


3 9

4 0

4 1

4 2

4 3

4 4

4 5

4 6

4 7

4 8

4 9

5 0

K E Y N O .

2 6

2 7

2 8

!

2 9

!

3 0

3 1

"

3 2

"

"

!

"

3

3

3

3

3

3

3

4

5

6

7

8

U 2 8 6 2 2

O R

U 4 7 0 5 7

O R

P 5 2 6 7 8

U 2 8 6 4 7

O R

U 2 8 6 4 6

O R

U 2 8 6 4 5

U 2 8 6 4 8

P 1 3 6 1 9

U 2 8 6 2 3

O R

U 2 8 5 8 7

P 2 9 6 9 3

P 5 0 4 5 0

P 5 9 1 9 0

U 2 0 9 3 2

P C 7 1 6 9

P A R T N O .

P 4 0 3 3 5

P 3 8 7 4 0

P 1 3 6 1 9

P 4 0 3 3 5

P 3 8 7 4 0

P 3 5 1 4 8

U 2 8 5 8 1

O R

U 2 8 5 8 2

U 2 8 5 8 8

P C 9 5 8 1

U 2 8 4 1 9

P 5 8 1 9 1

P 5 1 3 5 9

L 3 3 9 7

P 4 5 1 9 5

P 3 8 8 9 3

1

2

2

1

3

8

1

4

3

2

2

1

1

1

2

3

1

1

3

1

1

Q T Y .

6

3

3

4

4

6

1

M A C H .

S C R E W ( R D .

H D .

, S .

S .

)


# 1 0 2 4 x 3 / 8 " L G .

# 1 0 W A S H E R ( S .

S .

)

# 1 0 L O C K W A S H E R ( S .

S .

)

M A C H .

S C R E W ( R D .

H D .

, S .

S .

)

# 1 0 W A S H E R ( S .

S .

)

# 1 0 2 4 x 3 / 8 " L G .

M A C H .

S C R E W ( R D .

H D .

, S .

S .

)

3 0 A M P F U S E C L I P K I T ( U S E D

# 1 0 2 4 x 3 / 4 " L G .

F O R 3 8 0 , 4 4 0 / 4 8 0 , 5 5 0 V O L T S )

1

1

1

6 0 A M P F U S E C L I P K I T ( U S E D

F U S E B L O C K

F O R 2 0 8 , 2 2 0 / 2 4 0 V O L T S )

4 5 A M P H E A T E R F U S E ( U S E D F O R 2 0 8 , 2 2 0 / 2 4 0 V O L T S )

3 0 A M P H E A T E R F U S E ( U S E D F O R 3 8 0 , 4 4 0 / 4 8 0 , 5 5 0 V O L T S )

6 0 A M P H E A T E R F U S E ( U S E

7 A M P T R A N S F O R M E R F U S E

D

(

F O R 2 0 8 , 2 2 0 / 2 4 0 V O L T S )

U S E D F O R 3 0 8 , 2 2 0 / 2 4 0 V O L T S )

3 1 / 2 A M P T R A N S F O R M E R F U S E ( U S E D F O R 3 8 0 V O L T S )

3 A M P T R A N S F O R M E R F U S E

F U S E B L O C K

( U S E D F O R 4 4 0 / 4 8 0 , 5 5 0 V O L T S )

# 1 0 L O C K W A S H E R ( S .

S .

)

6 0 A M P C O N T A C T O R ( U S E D F O R 2 0 8 , 2 2 0 / 2 4 0 V O L T S )

3 0 A M P C O N T A C T O R ( U S E D F

M A C H .

S C R E W ( R D .

H D .

, S .

S .

)

O R

1 / 4

3 8 0 , 4 4 0 / 4 8 0 , 5 5 0 V O L T S )

" 2 0 x 1 / 2 " L G .

G R O U N D C O N N E C T O R

C I R C U I T B O A R D S U P P O R T

T E R M I N A L B L O C K

M A C H .

S C R E W ( R D .

H D .

, B R A S S ) # 8 3 2 x 1 " L G .

# 8 W A S H E R ( B R A S S )

L E V E L C O N T R O L B O A R D

W I R E C L A M P

A R R O W L A B E L

W A R N I N G L A B E L

3 / 8 " L O C K W A S H E R ( S .

S .

)

M O U N T I N G N U T ( B R A S S ) 3 / 8 " 3 2 x 1 / 2 "

NOTE:

!

PART OF G2343.

"



IM 50.200AA UA (B/1-01)

AAA8723 CONTROLS ENCLOSURE - PARTS LIST

50.200.060.020C

ISSUE 0 12-97

81


NOTES:

FOR PARTS LIST, SEE DWG. 50.200.060.030B.

IM 50.200AA UA (B/1-01) 82

AAA9083 ENCLOSURE - PARTS

50.200.060.030A

ISSUE 0 12-97


K E Y N O .

1

2

6

!

7

3

4

5

8

"

9

"

1 0

"

1 1

!

1 2

1 3

1 4

1 5

1 6

!

1 7

!

1

1

2

8

9

0

2 1

!

2 2

2

2

2

2

3

4

5

6

L 2 5 5 8

O R

L 3 3 0 8

A A A 7 1 3 9

A A A 8 6 4 2

P 4 7 8 4 9

P C 4 7 1 9

L 2 7 2 0

O R

L 2 7 2 1

L 1 9 6 7

L 2 7 1 7

P 5 9 1 8 4

P 3 6 6 7

P A R T N O .

P 1 2 4 7 0

P 5 7 5 9 5

P 5 9 9 6 6

P 4 2 7 5 7

P 3 8 7 4 0

P 1 3 6 1 9

A A A 7 1 2 1

L 3 2 2 2

L 3 2 2 2

P 5 7 5 9 5

A A A 7 1 2 4

A A A 7 1 1 8

A A A 7 1 1 5

P 5 9 9 9 0

P 5 9 1 8 5

P 5 9 1 8 2

L 2 4 9 9

O R

4

2

4

2

4

1

1

8

4

2

1

1

2 5

1

1

1

6

2

1

1

1

1 4

1 4

4

Q T Y .

3

6

1

2

2


L E A D G A S K E T

P U S H C L I P

C O V E R

M A C H .

S C R E W ( P A N .

H D .

, S .

S .

) # 1 0 2 4 x 7 / 8 " L G .

# 1 0 W A S H E R ( S .

S .

)

# 1 0 L O C K W A S H E R ( S .

S .

)

R I G H T H A N D S I D E E N C L O S U R E

L A B E L

L A B E L

P U S H C L I P

R E A R P A N E L

L E F T H A N D S I D E E N C L O S U R E

R E A R B R A C E

R E C E P T A C L E

S T U D

R E T A I N E R

L A B E L ( A M M O N I A U S E O N L Y )

L

S

L

L

R

A B

L A B E L

T O P

B R A C

W

W

E

A

A

E

L

B

B

C

A S

E

F

A R

E

E

E N C L O S U R E

E

-

L

K E T

T

N I

L

L

P

H E

(

( S U L F U R D I O X I D E

A

T

C H

P

N G

A

R ,

C

L

L O

S

C

L

C

A

O

E

R I

R

R

C K

N E

E

D

,

W

(

(

U

T

S

Y

E

P

O

E

N L Y )

U S E O N L Y )

F , S T L .

) # 1 0 2 4 x ½ " L G .

B O L T H E X .

H D .

, ¼ 2 0 x ¾ " L G .

W A R N I N G C A R D ( C H L O R I N E U S E O N L Y )

H

¼ "

A Z A R D O U S C H E M I C A L )

NOTE:

!


"

PART OF AAA8624 OPTIONAL PARTS GROUP FOR OUTDOOR USE.


AAA9083 ENCLOSURE - PARTS LIST

50.200.060.030B

ISSUE 0 12-97

IM 50.200AA UA (B/1-01) 83


NOTE: X


USE LITHARGE AND GLYCERIN CEMENT OR OTHER CEMENT APPROVED BY THE CHLORINE

INSTITUTE.


U27615 LINE PRESSURE RELIEF SYSTEM - PARTS

50.202.007.011

ISSUE 3 12-97

IM 50.200AA UA (B/1-01) 84


NOTE: USE LITHARGE AND GLYCERIN CEMENT OR OTHER CEMENT APPROVED BY THE CHLORINE INSTI-

TUTE.


IM 50.200AA UA (B/1-01)

U25471 GAS PRESSURE RELIEF SYSTEM - PARTS

50.202.008.011

ISSUE 2 7-85

85



LINE VALVE - PARTS

50.150.005.011

ISSUE 9 6-88

IM 50.200AA UA (B/1-01) 86


SECTION 6 - SPARE PARTS LIST

1

1

1

1

1

1

3*

3*

3*

QTY.

1

1

5

2

1

1 lb.

1

1

1

1

DESCRIPTION

Spare Parts Kit (replacement gaskets)

Cylinder Gasket

Gaskets for Ammonia Type Union

O-ring for Gauge Line (Chlorine gas pressure)

Gasket for Water Tank

Sodium Sulfate

Drying Kit

Rupture Disc (Liquid Line 400 psi)

**Fuse, 600V, 30 amp



Fuse, Transformer, 3 amp

Fuse, Transformer, 3-1/2 amp

Fuse, Transformer, 7 amp

Wrench

Bottle of Ammonia Solution for Chlorine Leak Detection U409

Complete Pump Repair Kit

(minus shaft seal and seat)

Shaft Seal and Seat Kit

U28665

U28664

Lamp (replacement bulb) U28629

*Minimum order.

**Used for heat exchanger and 3-phase power supply.

°Part of Spare Kit U28839.

U24910

P47057

U28622

P52678

U28645

U28646

U28647

P8200

PART NO.

U28839

°P42293

°P12470

°PXA26482

°P42234

U23934

U20208

IM 50.200AA UA (B/1-01) 87


IM 50.200AA UA (B/1-01) 88

IM 25.000AA UA ISSUE B

Taking care of the world’s water.

Wallace & Tiernan Products

1901 West Garden Road

Vineland, NJ 08360

856.507.9000 tel.

856.507.4125 fax

http://www.wallaceandtiernan.usfilter.com

CHLORINE HANDLING MANUAL


WARNING:

CHLORINE IS A HAZARDOUS CHEMICAL THAT CAN CAUSE INJURY

AND DEATH IF NOT HANDLED PROPERLY. THIS MANUAL CONTAINS

ONLY GENERAL INFORMATION ON THE PHYSICAL PROPERTIES, STOR-

AGE, AND HANDLING OF CHLORINE. IT IS NOT INTENDED TO REPLACE

OR LIMIT SAFETY PROCEDURES IN YOUR FACILITY.

SAFETY PROCEDURES IN AN INDUSTRIAL SETTING MUST BE DESIGNED

IN ACCORDANCE WITH ALL GOVERNMENTAL REGULATIONS AND

NATIONAL SAFETY CODES, AFTER GIVING FULL CONSIDERATION TO

THE SPECIFIC NEEDS OF THE INDUSTRIAL FACILITY INVOLVED.

U.S. FILTER/WALLACE & TIERNAN (USF/W&T) CANNOT ANTICIPATE

THE SPECIFIC SAFETY PROCEDURES REQUIRED AT EVERY INDUS-

TRIAL FACILITY. ACCORDINGLY, USF/W&T DOES NOT GUARANTEE

THAT SAFETY PROCEDURES DESIGNED IN ACCORDANCE WITH THIS

MANUAL WILL COMPLETELY ELIMINATE HAZARDS AND THUS AS-

SUMES NO LIABILITY FOR ACCIDENTS THAT MAY OCCUR IN YOUR

FACILITY.

READ THIS ENTIRE MANUAL AND BE FULLY FAMILIAR WITH YOUR

EQUIPMENT AND YOUR ENTIRE INDUSTRIAL SYSTEM SO THAT THE

SAFETY PROCEDURES YOU ESTABLISH WILL MEET THE NEEDS OF

THE EMPLOYEES IN YOUR FACILITY. READING ONLY PART OF THE

MANUAL WILL NOT HELP YOU ANALYZE THE NEEDS OF YOUR FACIL-

ITY. CONTACT YOUR CHLORINE SUPPLIER, THE CHLORINE INSTITUTE,

INC., OR SIMILAR ORGANIZATION TO OBTAIN A MATERIAL SAFETY

DATA SHEET (MSDS) AND MORE DETAILED INFORMATION ON CHLO-

RINE. INFORMATION IS AVAILABLE FROM: THE CHLORINE INSTITUTE,

INC., 2001 L STREET, NW, WASHINGTON, D.C. 20036.

PLEASE NOTE THE PUBLICATION DATE AND POSSIBLE OBSOLESCENCE

OF THIS MATERIAL AS A RESULT OF SCIENTIFIC AND MEDICAL DEVEL-

OPMENTS AFTER THE DATE OF PUBLICATION. THIS APPLIES TO ALL

MATERIALS YOU REVIEW IN THE COURSE OF DEVELOPING SAFETY

PROCEDURES FOR USE AT YOUR FACILITY.

Table Of Contents

IM 25.000AA UA (B/6-00)

PARA. NO.

Introduction ............................................................................... 1

Technical Data and Characteristics of Chlorine ....................... 2

Supply Containers ...................................................................... 3

Maximum Gas Withdrawal Rates ........................................... 3.1

Manifolding for Gas Withdrawal .......................................... 3.1.1

Maximum Liquid Withdrawal Rate ........................................ 3.2

Manifolding for Liquid Withdrawal ..................................... 3.2.1

Container Valves ..................................................................... 3.3

Pressure Relief Devices ........................................................... 3.4

Storage of Containers .............................................................. 3.5

PAGE 1


Table Of Contents (Cont’d)

Handling Containers ............................................................... 3.6

Using Containers ..................................................................... 3.7

Piping ......................................................................................... 4

Piping Materials and Joints ..................................................... 4.1

Gas Piping Installation Requirements .................................... 4.2

Liquid Piping Installation Requirements ................................ 4.3

Pressure Relief and Vent Piping Requirements ...................... 4.4

Valves ...................................................................................... 4.5

Pressure Gauges and Switches ................................................ 4.6

Pressure Relief Devices ........................................................... 4.7

Preparation for Use .................................................................. 4.8

Personnel Safety ......................................................................... 5

General ..................................................................................... 5.1

Health Hazards ........................................................................ 5.2

Safety Precautions .................................................................... 5.3

Emergency Action Plans ......................................................... 5.4

Chemical Disposal Facilities ................................................... 5.5

1 INTRODUCTION

This manual discusses the characteristics, storage and handling of chlorine used with USF/W&T equipment. Chlorine is used with USF/W&T equipment primarily as a disinfectant in water or wastewater treatment.

WARNING:

IN CASES OF ACCIDENT:

USE SAFETY EQUIPMENT TO PROTECT THE RES-

CUER AND MOVE VICTIM TO FRESH AIR. IF

BREATHING HAS STOPPED, START ARTIFICIAL

RESPIRATION IMMEDIATELY.

IF HEART HAS STOPPED, START CPR (CARDIOP-

ULMONARY RESUSCITATION) IMMEDIATELY. IN

ALL CASES, OBTAIN MEDICAL ATTENTION AS

SOON AS POSSIBLE.

CHLORINE IS HAZARDOUS. TO AVOID SEVERE

PERSONAL INJURY OR DEATH BY SUFFOCATION,

READ THIS MANUAL AND THE CHLORINE

SUPPLIER’S PRECAUTIONS BEFORE HANDLING

OR CONNECTING CHLORINE TO USF/W&T EQUIP-

MENT.

WHEN WORKING WITH CHLORINE:

ENSURE THAT APPROVED, SELF-CONTAINED

BREATHING APPARATUS IS ALWAYS AVAILABLE

AND PERSONNEL ARE PROPERLY TRAINED IN ITS

USE.

ENSURE THAT SAFETY EQUIPMENT, SUCH AS

VENTILATION FANS AND BREATHING APPARA-

TUS, IS INSPECTED AND MAINTAINED IN ACCOR-

DANCE WITH THE MANUFACTURER’S INSTRUC-

TIONS.

ENSURE THAT APPROPRIATE PLACARDS AND

WARNING SIGNS ARE IN PLACE AND PROMI-

NENTLY DISPLAYED IN THE AREAS WHERE THE

GAS IS STORED.

TO AVOID ACCIDENTAL GAS RELEASE:

KNOWLEDGEABLE DESIGN PERSONNEL SHOULD

OVERSEE AND APPROVE EQUIPMENT INSTALLA-

TION AND SUITABILITY OF THE SYSTEM FOR

WHICH IT IS INTENDED.

QUALIFIED PERSONNEL SHOULD PERFORM PE-

RIODIC INSPECTION TO ENSURE PROPER MAIN-

TENANCE OF THE EQUIPMENT.

MONITOR SAFETY PROGRAMS AND CONDUCT

PERIODIC TRAINING PROGRAMS, ESPECIALLY

ON EMERGENCY SITUATIONS. SAFETY PRO-

GRAMS ARE AVAILABLE FROM YOUR GAS SUP-

PLIER.

LOCAL LAWS:

UNDER NO CIRCUMSTANCES SHOULD THE IN-

FORMATION IN THIS BOOK BE CONSTRUED AS

SUBSTITUTING FOR OR SUPERSEDING ANY LO-

CAL, STATE, OR FEDERAL LAWS AND REGULA-

TIONS CONCERNING THE STORAGE, HANDLING,

OR USE OF CHLORINE.

IM 25.000AA UA (B/6-00) PAGE 2


2 TECHNICAL DATA AND CHARACTERISTICS OF

CHLORINE

Specific Gravity, Dry Gas

2.48 at 32° F and 1 atm referred to air.

The following general information on chlorine may be useful in planning a chlorinator installation; however, a specific application may require more information than that included here. For further information, consult your chlorine supplier, the Chlorine Institute, Inc., or similar organization.

Specific Gravity, Liquid

1.47 at 32° F and 53 . 5 psia.

Liquid to Gas volume Ratio

1:456.5 at 32° F and 1 atm.

Chlorine in commerce is a liquefied gas under pressure. It is a clear, amber-colored liquid. The gas has a greenish-yellow color and a strong, pungent odor. It is an irritant to the skin and respiratory system. In the moisture-free state at ordinary temperatures, it is relatively non-corrosive. In the presence of moisture, however, it is highly corrosive. Accordingly, every precaution should be taken to avoid leaks, to stop them promptly if they occur, and to keep moisture out of valves, tubing, etc., not specifically designed to handle moist chlorine. Among the important physical properties of chlorine are:

Latent heat of Vaporization

123.9 Btu per lb at boiling point, -29.2° F.

Specific Volume, Dry Gas

1 lb = 4.99 of at 32° F and 1 atm.

Specific Volume, Liquid

1 lb = 0.0109 cf at 32° F and 53.5 psia.

Weight, Dry Gas

1 cf = 0.2006 lb at 32° F and 1 atm.

IM 25.000AA UA (B/6-00)

Figure 1 – Chlorine Pressure vs Temperature

PAGE 3


Weight, Liquid

1 cf = 91.56 lb at 32° F.

3.1 RATES

Solubility in Water*

6.93 lbs./100 gals at 60° F and 1 atm.

Pressure vs Temperature

See Figure 1

*NOTE: Theoretical values shown. Actual solubility in water based on chlorinator performance has proven to be

3500 ppm or 2.92 lbs/100 gals maximum.

Chlorine is an oxidizing agent and will support combustion but is not explosive or flammable. Many organic chemicals will react with chlorine, some violently. Steel will ignite spontaneously in the presence of chlorine at 483° F.

In general, using a remote vacuum type chlorinator, the maximum sustained gas withdrawal rate at which chlorine may be taken from a 100 or 150 pound cylinder is one pound per day per degree Fahrenheit (1.0 lb/24 hrs/°F). The corresponding rate for ton containers is about 8.0 lbs/24 hrs/°F. At an assumed liquid temperature of 70° F (and using a remote vacuum type chlorinator) the above figures translate into 70 lbs/24 hrs for cylinders and 560 lbs/24 hrs for ton containers. For a direct feed cylinder pressure operated chlorinator these rates become 42 and 336 lbs/24 hrs respectively. These rates can be increased substantially for brief periods. Do not place containers in a water bath or apply direct heat in order to permit higher withdrawal rates.

It is not practical to withdraw chlorine as a gas from tank cars

(or tank trailers).

3 SUPPLY CONTAINERS

3.1.1

MANIFOLDING FOR GAS WITHDRAWAL

Table 1 gives details on the supply containers most commonly used with USF/W&T equipment.

Some large installations that would normally use single unit tank cars but are not serviced by railroad facilities use tank motor vehicles (tank trailers) which usually range in capacity from 15 to 22 tons.

When higher gas withdrawal rates are required, cylinders or the gas valves (upper) of ton containers may be manifolded.

A typical arrangement for manifolding cylinders is shown in

Figure 2.

All supply containers must conform to appropriate Department of Transportation (DOT) and Canadian Transport

Commission (CTC) regulations. It is the responsibility of the supply container manufacturer and the chlorine supplier to meet these requirements.

If cylinders or ton containers are manifolded, it is essential that all supply containers be at the same temperature to prevent the transfer of liquid chlorine from a warmer container to a cooler container, possibly resulting in a container becoming overfilled through reliquefaction of chlorine in the cooler container.

T Y P E O F

C O N T A I N E R

N E T W

T A B L E 1 C H L O R I N E C O N T A I N E R I N F O R M A T I O N

E I G H T T A R E W E I G H T G

W

R

E

O

I G

S S

H T

O

D I

U T

A M

S I D E

E T E R

C Y L I N D E R S

1 0 0

1 5 0 l b l b

2 0 0 0 l b

6 3

8 5 -

1 1 5

1 4 0 l b l b

1 3 0 0 1 6 5 0 l b

1

2

6

3

3

5

-

-

2 1

2

5

9 0 l l b b

8 ¼ " -

1 0 ¼ " -

1 0 ¾ "

1 0 ¾ "

2 ' 6 "

T O N

C O N T A I N E R

S I

T

N

A

G

N

L

K

E

C

U

A

N

R

I

S

T

1 6

3 0

5 5

8 5

9 0 t t o n s t o n s o n s t o n s t o n s

-

-

-

-

-

3 3 0 3

-

-

-

-

-

6 5 0 l b

1 0 ' 5 "

D i m e n s i o n a l d a t a f r o m C h l o r i n e M a n u a ,l F i f t h E d i t i o n , p u b l i s h e d b y t h e C h l o r i n e I n s t i t u t e , I n c .

-

1 2 ' 4 ½ " -

1 4 ' 3 " -

1 4 ' 1 1 " -

1 4 ' 1 1 " -

1 2 ' 0 "

1 3 ' 7 "

1 5 ' 1 "

1 5 ' 1 "

1 5 ' 1 "

3 3 '

L

1

E

0 "

N

3 ' 3 ½ "

4 ' 5 "

6 ' 7 ¾ " -

3 2 ' 2 "

-

-

4 3 ' 7 " -

4 5 ' 8 " -

-

2 9 ' 9 " -

G

-

T H

4 ' 1 1 "

4 ' 8 "

6 ' 1 0 ½ "

3 3 ' 3 "

3 5 ' 1 1 ½ "

4 3 ' 0 "

5 0 ' 0 "

4 7 ' 2 "

( 1 ) T h e 1 5 0 t r u c k o r r a i l i l b n c y l i n d e r s m a l l l o t s i s g e n e r a l l y m o o r i n f u l l t r u c k s t o r r e a d i l y a v a i l a b l e .

c a r l o a d s .

E i t h e r t h e 1 0 0 l b o r 1 5 0 l b s i z e m a y b e s h i p p e d f u l l o r e m p t y v i a

( 2 ) C h l o r i n e f r o m S i n g l e U n e c e s s i t y o f s t o r a g e t a n k s .

n i t T a n k

C a r s a r e

C a r s l e a s e i s d g t e n o e r a l l y u n l o a d t h e c o n s u m e r e d d u d i r e c t l y f r o m t h e r i n g t h i s p e r i o d a c a r n d a s a r e c n e e d e d o n s i g n e i n o r d e r t o d t o p r i v a t e e l i m i n a t s i d i n g s e t h e o n l y .

T w o p a r a l l e l t r a c k s a r e p e r i o d s w h i l e c a r s r e c o a r e m m e n d e d t o f a b e i n g s w i t c h e d .

c i l i t a t e t h e h a n d l i n g o f c a r s a n d t o p e r m i t c o n t i n u o u s o p e r a t i o n w i t h o u t s h u t d o w n

IM 25.000AA UA (B/6-00) PAGE 4


Figure 3 – Standard Cylinder Valve

Figure 2 – Manifolding Cylinders

3.2 MAXIMUM LIQUID WITHDRAWAL RATE

The generally accepted alternate to manifolding ton containers is to withdraw liquid chlorine from the lower valve and use an evaporator. By this means, a ton container can be emptied in approximately five hours, which is equivalent to

9600 lbs/24 hrs.

Liquid can be withdrawn from tank cars at up to nearly 8,000 pounds per hour, or 192,000 pounds per 24 hours.

3.2.1

MANIFOLDING FOR LIQUID WITHDRAWAL

WARNING: IN ACCORDANCE WITH CHLORINE IN-

STITUTE RECOMMENDATIONS, DO NOT MANI-

FOLD TON CONTAINERS FOR SIMULTANEOUS

LIQUID CHLORINE WITHDRAWAL. THIS

MANIFOLDING CAN CAUSE OVER-PRESSURIZA-

TION AND RUPTURE.

3.3 CONTAINER VALVES

Standard cylinder and ton container valves are identical in design, except that the cylinder valve includes a pressure relief device. Cylinder valves are shown in Figure 3 and ton container valves in Figure 4.

See Figure 5 for captive yoke type auxiliary container valves

(valve connection style #820, recognized by the Compressed

Gas Association as the only acceptable means of connecting to container valves). The external threads on the container valve are used only for securing the protective cap.

IM 25.000AA UA (B/6-00) PAGE 5

Figure 4 – Standard Ton Container Valve

Figure 5 – Auxiliary Ton Container Valve


Cylinders are equipped with one valve that is normally used for gas withdrawal. Ton containers are equipped with two valves, as shown in Figure 6.

creases to 158-165° F to relieve pressure and prevent rupture of the cylinder.

Ton containers are equipped with six fusible metal plugs (see

Figure 8), three of which are in each end, spaced 120 degrees apart.

Figure 6 – Ton Container Valves

Figure 8 – Standard Fusible Plug for Ton Containers

The upper valve is used for gas withdrawal and the lower valve for liquid withdrawal. Tank cars are equipped with four standard angle valves, as shown in Figure 7.

Tank cars have an excess-flow valve (see Figure 9) located under each liquid valve. While this valve may close during a catastrophic pipe line failure, its main function is to close automatically if the angle valve is broken off in transit. Tank cars also have a pressure relief device (see Figure 10) located in the center of the manway. The relief level varies with the type of car or tank.

Figure 7 – Standard Angle Valve

Outlet is one-inch female ANSI Standard taper pipe thread.

The liquid withdrawal valves are located on the longitudinal center line of the tank car. The valves on the transverse center line are connected to the vapor space and are used to obtain chlorine gas under pressure for testing the piping or for air padding the tank car.

3.4 PRESSURE RELIEF DEVICES

Figure 9 – Excess-Flow Valve

3.5 STORAGE OF CONTAINERS

All chlorine supply containers are equipped with some type of device for relief of pressure. Cylinder valves have a fusible metal plug screwed into the body of the valve, as shown in

Figure 3. The fusible metal melts when the temperature in-

IM 25.000AA UA (B/6-00) PAGE 6

Store chlorine containers of any type under cover and in cool, well ventilated locations protected from fire hazards and adequately protected from extreme weather conditions. During the summer months, full containers should be shielded from the direct rays of the sun, otherwise a dangerous buildup of pressure might result (see Figure 1 and Paragraph 3.3).

If stored out of doors, keep containers in fenced-off areas for protection. Avoid storage in subsurface areas because chlorine is heavier than air and will not readily rise from subsur-


The chlorine inventory depends to a large extent on local availability. Consult with chlorine suppliers in the area; review appropriate fire code requirements concerning storage of oxidizing materials and other applicable laws and regulations.

When planning space for stored containers, sufficient space must be allowed for empty containers. The best way to determine the amount of chlorine remaining in a container is to weigh the container continuously on a scale. This also makes it possible to record the amount of chlorine used. Portable or dormant scales in beam, dial, or digital types and with varying platform sizes are available.

WARNING: ALWAYS REMOVE WHEELS AND AX-

LES OF PORTABLE SCALES SO THAT THE SCALE

CANNOT MOVE WHEN CYLINDERS ARE ON THE

PLATFORM.

Figure 10 – Standard Safety Relief Device

Preferably, scales for cylinders should be installed with their platform flush with the floor to eliminate the necessity of lifting the cylinders. Some low profile scales such as the

USF/W&T Two Cylinder Scale (platform 1-1/2 inches above floor) are low enough that cylinders can be placed on the scale without lifting. Others are installed with ramps. If scales are pit mounted, a trapped drain should be provided.

face locations should leaks occur. Do not store or use chlorine containers near other chemicals or gases.

WARNING: STORE CYLINDERS IN AN UPRIGHT

POSITION. TO AVOID SEVERE PERSONAL INJURY

OR EQUIPMENT DAMAGE, SUPPLY CYLINDERS

MUST BE SECURED IN SUCH A MANNER (E.G.,

CHAIN) AS TO PREVENT THEIR BEING KNOCKED

OVER. TON CONTAINERS MUST BE SECURED IN

SUCH A MANNER (E.G., CROCKS) TO PREVENT

THEIR ROLLING OUT OF PLACE.

Scales for ton containers are usually installed above the floor, since ton containers are usually handled by overhead conveyor. Many of these scales do not have platforms since the ton containers are usually supported by cradles or trunnions.

Special high-capacity scales are provided at some installations using tank cars. These scales are usually pit mounted below the railroad siding with the dial or digital unit housed above ground beside the track.

Do not remove the protective cap or hood from cylinders or ton containers until they are ready to be put in actual use. Do not store containers in a heavily traveled area where physical contact damage could occur.

Some of the dial or digital scales are equipped with loss-ofweight recording systems providing a permanent record of chlorine usage.

3.6 HANDLING CONTAINERS

It is essential that areas used to house chlorine containers or equipment be continuously monitored for the presence of chlorine in the air. This may be a requirement of applicable laws and/or regulations.

Always handle chlorine containers with utmost care. To prevent injury or damage, do not drop chlorine containers and do not permit containers to strike each other or other objects. To prevent damage to the valve, valve protecting caps or hoods must always be in place when containers are moved.

When containers are moved from a storage area to an area where they will be used, allow sufficient time to stabilize the temperature, and therefore the pressure, of the container and the chlorine before it is used.

IM 25.000AA UA (B/6-00)

Handle cylinders with a simple two-wheel hand truck of the barrel pattern. Hand trucks should be well balanced and equipped with chains or clamps to prevent the cylinders from falling off the truck.

PAGE 7


WARNING: NEVER LIFT CYLINDERS BY THE

VALVE PROTECTING HOOD. THE HOOD MAY

SEPARATE FROM THE CYLINDER, CAUSING THE

CYLINDER TO FALL.

POSITION WITH THE TWO VALVES IN A VERTI-

CAL LINE. TON CONTAINERS MUST BE SECURED

IN SUCH A MANNER (E.G., CHOCKS) TO PREVENT

THEIR ROLLING OUT OF PLACE.

Never lift cylinders by sling or magnetic devices. If lifting is necessary, use a specially designed cradle. Contact your chlorine supplier for recommendations or information.

When withdrawing gas from a ton container, connection is made to the upper valve (see Figure 6). Liquid withdrawal is accomplished by connecting to the lower valve.

When moving ton containers, due consideration must be given to the fact that the liquid in the container represents a live load in addition to the dead load of the container and the liquid. The most accepted way of moving ton containers is by overhead conveyor and lifting beam (see Figure 11).

THIS DIMENSION

DETERMINED BY

REQUIREMENTS OF

LIFTING DEVICE

LIFTING BAR

OVERHEAD MONORAIL

HOIST

(4000 LB. MIN.)

2’-7”

CLEARANCE

It is recommended that special 3/8-inch square box wrenches, rather than adjustable wrenches, be used for opening cylinder and ton container valves. Length of the wrench should not exceed eight inches. It is good practice to leave the wrench in place so the valve can be closed quickly in case of an emergency. Maximum discharge can be accomplished with one full turn of the valve. Excessive force must not be used in opening valves. Never strike the wrench with anything other than the heel of the hand. Loosening the packing nut a maximum of 1/2 turn is acceptable, provided the packing nut is tightened after the valve is operated. Contact your chlorine supplier if these procedures do not permit operation of the valve.

13”

6’-10” 2’-6”

Angle valves on tank cars must be opened fully to aid the operation of the excess flow valve.

2’-8”

Always test for leaks before putting new containers in service. The system can be pressurized by opening the container valve and then closing it. The valve can be opened again after it is determined that there are no leaks.

1/2”±

Figure 11 – Ton Container Handling

Rails or roller conveyors have also been used. Fork lift trucks, in addition to having adequate capacity, must have the containers restrained and be sufficiently stable to prevent tipping.

WARNING: ALWAYS WEAR PROTECTIVE CLOTH-

ING WREN CHECKING FOR LEAKS. REFER TO

“PERSONNEL SAFETY” FOR INFORMATION ON

HEALTH HAZARDS AND SAFETY PRECAUTIONS.

3.7 USING CONTAINERS

If containers have been stored in an area other than that in which they will be used, they should be allowed to stabilize at the new temperature before being used. Containers should always be used in the order in which they are received to avoid unnecessarily long storage and possible difficulty with valves that have not been opened or closed for too long a period.

It is not unusual during humid conditions for condensation to collect on the outside of the container. A buildup of frost on the container indicates that withdrawal rates are too high to permit the surrounding air to supply the heat necessary to evaporate the liquid chlorine. Increasing the circulation of room temperature air past the container may correct the condition. Do not apply direct heat to the container in any way. It may be necessary to shut off the container valve and permit it to warm up again before putting it back in service.

WARNING: CYLINDERS ARE NORMALLY USED IN

AN UPRIGHT POSITION FOR GAS WITHDRAWAL.

TO AVOID SEVERE PERSONAL INJURY OR EQUIP-

MENT DAMAGE, SUPPLY CYLINDERS MUST BE

SECURED IN SUCH A MANNER (E.G., CHAIN) AS

TO PREVENT THEIR BEING KNOCKED OVER. TON

CONTAINERS MUST BE USED IN A HORIZONTAL

IM 25.000AA UA (B/6-00) PAGE 8

After emptying the container, the valve must be closed before disconnecting to prevent the entry of moisture. After disconnecting, the valve cap and the valve protecting cap or hood must be replaced before the container is moved. Empty containers should be segregated from full containers and should be tagged.


Tank cars are unloaded by means of one of the liquid valves.

One of the gas valves can be connected to the system to permit pressure testing with gaseous chlorine rather than liquid. The flexible connection used for tank car unloading must be designed for and installed in such a manner to allow for the significant increase in height as the car unloads. Since tank car pressure is the only force causing the chlorine to discharge, many cars are padded with dry air by the producer or the user. Reference to Chlorine Institute Pamphlet 66,

Chlorine Tank Car Loading, Unloading, Air Padding, Hydrostatic Testing, should be made for information on user air padding. It is essential that air padding pressure be kept as low as possible for satisfactory operation of the chlorination equipment since excessive air padding pressures can have a negative impact on evaporator performance. The depletion of the liquid chlorine supply in the car is accompanied by a sharp drop in tank car pressure.

To facilitate maintenance, the number of line valves should be kept to a minimum. Insulation is required only in those cases where it is necessary to prevent chlorine gas lines from becoming chilled, or liquid lines from becoming overheated.

More complete details, along with ASTM and ANSI specifications, can be obtained by referring to Chlorine Institute

Pamphlet 6, Piping Systems For Dry Chlorine.

WARNING: TWO COMMON CAUSES OF CHLO-

RINE PIPING LEAKS ARE:

1. RE-USE OF GASKETS. THIS SHOULD NEVER BE

DONE. ALWAYS HAVE AN ADEQUATE SUPPLY ON

HAND AND ALWAYS USE NEW GASKETS OF THE

CORRECT MATERIAL AND SIZE AS IDENTIFIED

ON THE EQUIPMENT PARTS DRAWING.

2. IMPROPERLY MADE-UP THREADED PIPE

JOINTS. SEE CHLORINE INSTITUTE MANUAL OR

PAMPHLET 6 FOR RECOMMENDED PROCEDURE.

After the angle valve is closed and the discharge line emptied, the piping may be disconnected. The valve outlet plugs should be replaced and the discharge piping capped immediately.

4.2 GAS PIPING INSTALLATION REQUIREMENTS

4 PIPING

4.1 PIPING MATERIALS AND JOINTS

If the chlorinator capacity is low enough, the vacuum regulator or the complete chlorinator may be mounted directly on a cylinder or ton container valve, totally eliminating pressure piping. In this case, reference to the equipment instruction book provides all necessary details.

Reliquefaction of a gas should be avoided. If liquid chlorine is carried downstream to the chlorinator or vacuum piping, it may soften the plastic components and affect their structural strength. Liquid can wash any collected contaminants into the vacuum regulator and can also cause erratic surging, freezing, and pressure release, which can damage the diaphragm and control valves. Cold conditions in a gas pipe line

(cold to the touch, dripping of water condensed from the atmosphere, frost, ice) are an indication that liquid chlorine is present in the line and is flashing to gas. Refer to the proper guidelines that follow.

Pressure connections from all chlorine containers are normally made by means of flexible connections made of copper tubing. Use yoke type connections at container valves. The chlorinator or vacuum regulator instruction book should be referred to for details for use of flexible connections along with the required auxiliary cylinder or ton container valves, header valves, and auxiliary header valves (if required).

It is important to observe the correct temperature conditions in conducting chlorine gas under pressure from the location of the containers to the point of use. To avoid difficulty with reliquefaction of chlorine, pressure piping and control equipment receiving gas under pressure should be at a higher temperature than that of the chlorine containers. In general, a difference of 5° to 10° F is recommended.

WARNING: ALWAYS REPLACE FLEXIBLE CON-

NECTIONS ANNUALLY (OR SOONER IF THERE IS

EVIDENCE OF DETERIORATION).

Pitch pressure lines uphill from the gas source toward the chlorinators if possible.

The usual practice for chlorine liquid or gas pressure lines, at the commonly encountered pressures and temperatures at chlorinator installations, is the use of 3/4 or 1.0 inch schedule 80 carbon steel seamless pipe with Class 3000 forged steel fittings; two-bolt flanges (commonly referred to as oval ammonia unions) are also often used. Both screwed and socket welded construction are common. Threaded joints should be made up using litharge and glycerine for permanent joints, white lead or TFE tape for others.

IM 25.000AA UA (B/6-00)

Install a pressure reducing valve or the chlorinator vacuum regulator close to, but higher than, the source of gas. The use of a chlorine pressure reducing valve is also recommended in those localities where severe temperature changes are likely to be encountered during a 24-hour period.

It is preferable to run chlorine pressure gas lines overhead through relatively warm areas rather than along the floor or through basement areas where lower temperatures may be

PAGE 9


encountered. Do not run these gas lines along exterior walls that may be cold in winter months. Do not run pressure gas lines under windows from which cold air descends in winter months.

A liquid line pressure relief system (which includes a rupture disc and an expansion chamber) is required where liquid may be trapped in the line or where it is necessary to run lines a considerable distance. The relief system is detailed in Figure 13.

If the source of gas is one or more ton containers connected to a manifold, install a drip leg of 1.0-inch schedule 80 seamless steel pipe approximately 18 inches long in a tee in the manifold with the lower end capped. Locate the drip leg immediately downstream of the last container connection to intercept the liquid that comes from the ton containers’ gas eduction tubes when initially opened.

1/2” FEMALE NPT FOR

115 V ELECTRICAL

CONNECTION

PRESSURE

SWITCH

DIAPHRAGM SEAL

UNIT

6-5/8”

Gas may be withdrawn from two or more containers simultaneously provided all containers are at the same temperature. Refer to Paragraph 3.1.

EXPANSION

CHAMBER

SUPPORT BRACKET

The installation of chlorine gas strainers in pipe lines upstream from pressure reducing valves or vacuum regulators is a common practice. These strainers can also serve as traps for a small amount of liquid chlorine. Figure 12 illustrates a typical strainer.

WARNING LABEL

30”

46-1/4”

RUPTURE

DISC

HOUSING

LENGTH OF LIQUID LINE

PROTECTED PER EXPANSION

CHAMBER SYSTEM

P I P E

S

1

I Z

"

E

3 / 4 "

C H L

3

6

O

7

2

R I

5

5

'

'

N E UNION

HEAD

GASKET

1” CHLORINE

LINE

Figure 13 – Liquid Line Pressure Relief System

SCREEN

AND COVER

BOLT

Figure 12 – Chlorine Gas Strainer

The expansion chamber provides an area for expansion in the event that valves at both ends of the line are closed.

Relief system placement must be based not only on length of line but also placement of valves.

4.3 LIQUID PIPING INSTALLATION REQUIRE-

MENTS

4.4 PRESSURE RELIEF AND VENT PIPING RE-

QUIREMENTS

It is important to avoid conditions that will encourage vaporization. Thus it is important to keep liquid chlorine lines as cool as, or cooler than, the containers themselves by eliminating restrictive fittings and always operating with fully opened line valves. Avoid running liquid chlorine lines through overheated areas where gasification is likely.

All pressure relief vent line systems must be treated as though they contain chlorine. Use the same materials for pressure relief vent lines as used for chlorine gas piping, unless the vent line is a combination pressure relief/vacuum relief line in which case the material must be suitable for moist chlorine gas (PVC or polyethylene tubing).

Valves in liquid chlorine lines should be kept to a minimum.

It is particularly important to avoid situations where it is easy to close two valves in a line thus trapping liquid that, upon an increase in temperature, will expand and develop higher than acceptable pressures.

IM 25.000AA UA (B/6-00)

Vent lines must be run in such a way that moisture collecting traps are avoided. A continuous gradient is preferred. The end of all vent lines must be turned down and screened.

Manifolding of vent lines is an acceptable practice provided only like vents are manifolded (i.e., evaporator water vapor

PAGE 10


vents must be separate from gas pressure reducing valve pressure vents, etc.). The interior cross sectioned area of a common vent or pressure relief line should be approximately equal to the sum of the cross sectional areas of the individual vent lines.

BONNET PLATE

STEM BEARING

STEM SEAL

STEM NUT

HANDLE

RETAINING RING

INDICATOR STOP

STEM

SEAT

BODY SEAL

WARNING: THE VENT LINE AND RELIEF LINE

MUST TERMINATE IN AN AREA GAS FUMES CAN-

NOT CAUSE INJURY TO PERSONNEL OR DAMAGE.

DO NOT TERMINATE THE VENT LINE AND RE-

LIEF LINE AT A LOCATION ROUTINELY USED BY

PERSONNEL, SUCH AS WORK AREAS OR PATH-

WAYS NOR NEAR ANY WINDOWS OR VENTILA-

TION SYSTEM INTAKES. IF AN AREA MEETING

THESE REQUIREMENTS IS NOT AVAILABLE,

REFER TO THE CHLORINE INSTITUTE’S CHLO-

RINE MANUAL AND PAMPHLET NO. 9 FOR AL-

TERNATE METHOD OF RELIEF DISPOSAL.

BALL

BODY CAP

BODY

Figure 15 – Gas and Liquid Ball Valve

4.6 PRESSURE GAUGES AND SWITCHES

4.5 VALVES

Yoke type auxiliary cylinder, yoke type auxiliary ton container, and header valves are described adequately in the chlorinator or vacuum regulator instruction book.

Whenever pressure gauges and switches are used in chlorine liquid or gas lines, they must be of the type protected by a flanged diaphragm seal specifically designed for chlorine service to prevent the entry of chlorine into the gauge or switch mechanism. The fill material must be suitable for chlorine service. The connection between the seal and the gauge or switch must not be broken. If the connection is inadvertently broken, the complete assembly must be discarded and replaced, unless it can be returned to the manufacturer for repair.

Line valves are used to isolate alternate sources of supply

(manifolded banks of ton containers or tank cars), individual evaporators or pressure type chlorinators. Sufficient line valves should be provided for flexibility of system operation consistent with the recommended practice of eliminating redundant or unnecessary valves.

Frequently, valves are installed between chlorine lines and the gauge or switch diaphragm seal to permit removal without taking the line out of service. A means of relieving the pressure in the isolated piping, gauge, or switch is strongly recommended.

Valves are usually of approximately globe pattern as shown in Figure 14 or ball type as shown in Figure 15.

Care should be taken that only valves designed by the manufacturer specifically for chlorine service are used. Ball valves must include a provision for venting the cavity in the closed position to the upstream side.

WARNING: RELEASING EVEN A SMALL AMOUNT

OF LIQUID CHLORINE IS DANGEROUS AND RE-

QUIRES EXTREME CAUTION TO AVOID SEVERE

PERSONAL INJURY. ALWAYS USE PROTECTIVE

EQUIPMENT WHEN RELIEVING PRESSURE, EVEN

IN ISOLATED CHLORINE GAS PIPING.

MACH. SCREW

WASHER

PACKING NUT

PACKING GUARD

PACKING BOX

GAP

LEAD GASKET

STEM UNIT

LEAD GASKET

HANDLE

PACKING

PACKING RING

CAP SCREW (4)

SEAT

VALVE BODY

Since small size line valves for chlorine are not readily available, many times a header valve is used as shown in Figure 16.

PRESSURE GAUGE

(OR SWITCH) AND

DIAPHRAGM

UNION ADAPTER

UNION NUT

LEAD GASKET

HEADER VALVE

3/4” CONNECTION

IN GAS LINE

INLET

Figure 14 – 3/4- and 1-Inch Line Valves

Figure 16 – Chlorine Pressure Gauge or

Switch Mounted on Header Valve

IM 25.000AA UA (B/6-00) PAGE 11


4.7 PRESSURE RELIEF DEVICES

fore essential that all piping be thoroughly cleaned and dried prior to exposure to chlorine.

There are two types of pressure relief devices in use in chlorine piping systems. The first, as shown in Figure 13, is usually employed in liquid chlorine piping to protect the piping from rupture due to high pressure from thermal expansion of the liquid chlorine. It consists of a rupture disc that ruptures before the pipe line itself can rupture, an expansion chamber that allows for relief of the over-pressure condition without releasing chlorine to the atmosphere, and a pressure switch to warn of the disc rupture.

WARNING: INCOMPLETE CLEANING CAN RE-

SULT IN VIOLENT REACTIONS BETWEEN CHLO-

RINE AND THESE MATERIALS.

Steam cleaning is an acceptable method for removal of the above materials. Provision must be made for removal of condensate and foreign materials. For alternate methods if steam is not available, refer to Chlorine Institute Pamphlet

6, Piping Systems for Dry Chlorine.

The second type, as shown in Figure 17, is usually used in gas piping at the evaporator discharge. This system consists of a rupture disc that keeps chlorine out of the valve during normal operation, a pressure relief valve, and a pressure switch to warn of disc rupture.

GAS PRESSURE RELIEF VALVE 500 PSIG

1/2” FEMALE NPT FOR 115V

ELECTRICAL CONNECTION

PRESSURE SWITCH

1” FEMALE NPT INLET

DIAPHRAGM SEAL UNIT

RUPTURE DISC 400 PSI

UNION HEAD

After proper cleaning, all chlorine piping should be hydrostatically tested to one and one half times the expected maximum operating pressure. Prior to testing, all gauges, switches, rupture discs, etc., that could be damaged during testing must be removed and connections plugged. Any moisture absorbing packing or gaskets left in the system during hydrostatic testing must be removed and replaced with new packing or gaskets. After hydrostatic testing, it is essential that all piping be thoroughly dried with inert gas (e.g., nitrogen) or dry air having a dew point of -40° F or below. The dew point of the air or gas leaving the piping must be checked and drying continued until the dew point is at or below -40° F, which may require quite some time.

1-1/2” FEMALE NPT RELIEF CONNECTION

Figure 17 – Evaporator Pressure Relief System

WARNING: THE RELIEF LINE MUST TERMINATE

IN AN AREA WHERE GAS FUMES CANNOT CAUSE

DAMAGE OR INJURY TO PERSONNEL. DO NOT

TERMINATE THE RELIEF LINE AT A LOCATION

ROUTINELY USED BY PERSONNEL, SUCH AS

WORK AREAS OR PATHWAYS, NOR NEAR WIN-

DOWS OR VENTILATION SYSTEM INTAKES. IF AN

AREA MEETING THESE REQUIREMENTS IS NOT

AVAILABLE, REFER TO THE CHLORINE

INSTITUTE’S CHLORINE MANUAL AND PAM-

PHLET NO. 9 FOR AN ALTERNATE METHOD OF

RELIEF DISPOSAL.

WARNING: MOISTURE MUST BE REMOVED FROM

ANY PART OF THE EQUIPMENT THAT IS NOR-

MALLY EXPOSED TO DRY CHLORINE ONLY.

WHILE DRY CHLORINE IS NON-CORROSIVE,

MOIST CHLORINE IS EXTREMELY CORROSIVE

TO COMMON METALS, SUCH AS BRASS OR STEEL,

POSSIBLY RESULTING IN A LEAK AND SEVERE

PERSONAL INJURY. ALSO, IF WATER IS TRAPPED

IN A SECTION OF PIPING OR EQUIPMENT, SUBSE-

QUENT HEATING OR FREEZING OF THE WATER

MAY RESULT IN HIGH ENOUGH PRESSURE TO

RUPTURE THE PIPING OR EQUIPMENT, POSSIBLY

CAUSING SEVERE PERSONAL INJURY.

A very acceptable alternate to hydrostatic testing, if proper facilities do not exist for drying, is to test with nitrogen or dry air having a dew point of -40° F or below. The same provision of removing equipment that could be damaged by test pressure applies.

4.8 PREPARATION FOR USE

Normal plumbing practices will result in the entry of cutting oils, greases, and other foreign materials into the piping.

In addition, the line will have been open to the atmosphere during construction, allowing moisture to enter. It is there-

IM 25.000AA UA (B/6-00) PAGE 12

WARNING: TO AVOID SEVERE PERSONAL IN-

JURY, BEFORE PLACING THE PIPING SYSTEM

INTO SERVICE, PRESSURE TEST WITH CHLORINE

GAS, NOT LIQUID. EACH VOLUME OF CHLORINE

LIQUID THAT LEAKS AND THEN EVAPORATES

RESULTS IN APPROXIMATELY 460 VOLUMES OF

CHLORINE GAS.


The chlorine container valve should be opened only slightly during this phase of testing or preferably closed again after pressurizing the system. The piping should be tested in the smallest sections permitted by the existing valves to minimize the discharge of chlorine through any leaks.

can provide cross circulation; however, ventilation by means of a proper type electric fan is always recommended.

In all cases, installations must comply with appropriate regulations.

WARNING: IT IS ESSENTIAL THAT PROPER

BREATHING APPARATUS BE AVAILABLE BEFORE

CHLORINE IS ADMITTED TO ANY PIPING SYSTEM

OR EQUIPMENT. THIS APPARATUS WILL BE DIS-

CUSSED FURTHER UNDER “PERSONNEL

SAFETY”.

Chlorine leaks are best located using a dauber moistened with commercial 26° Baume’ aqueous ammonia (household ammonia is not strong enough) . A white cloud will be formed at the site of any leak. A plastic squeeze bottle that directs ammonia vapor, not liquid, at the joint being tested may also be used.

5.2 HEALTH HAZARDS

Exposure to a sufficiently high concentration of chlorine can result in difficulty in breathing and, if prolonged, finally death through suffocation. Chlorine’s strong pungent odor may result in detection at levels as low as 1.0 ppm and most people will detect it by the time the concentration reaches 3.5

ppm. Concentrations of 5 ppm or more are so objectionable that only those who are unconscious or trapped will normally remain in the area. Increasing concentrations will produce eye irritation, coughing, throat irritation, vomiting, and labored breathing.

When a leak is detected, the system must be depressurized before corrective action is taken. The best method of depressurizing the system is through one of the chlorinators. At least one chlorinator must be readily available for this purpose before testing with chlorine begins.

Even concentrations below the threshold of smell can result in minor eye and throat irritation if the exposure is long enough.

Liquid chlorine can cause burns and/or irritation when it is in contact with the skin or eyes.

5 PERSONNEL SAFETY

5.1 GENERAL

Proper consideration of personnel safety begins with the provision of properly sized and arranged housing so that operating personnel have adequate room to perform their duties. It is preferable that any room used for chlorine storage or equipment have two doors that open outward and that are equipped with panic bars.

Medical attention should be obtained immediately for personnel who have sufficient exposure to result in any symptoms beyond minor irritation. Properly trained and equipped first aid personnel are usually the first line of defense. While waiting for their arrival, the exposed individual must be removed to a safe area and be placed in a comfortable position. If breathing has stopped, artificial respiration must be started immediately. CPR administered by properly trained personnel is required if the heart has stopped.

If the exposed individual has difficulty breathing, oxygen should be administered only by those adequately trained in the procedure and the equipment used.

Rooms housing chlorination equipment, and chlorine containers that are “in service” or “in reserve”, should be heated when the room temperature falls below 50° F. Comfortable working temperatures of 65° to 75° F are recommended for the chlorine equipment room. The temperature of the chlorine container room (if separate) should normally be 5° to

10° F lower. All common methods of heating are acceptable, provided that care is taken to prevent overheating of chlorine containers. Radiators should not be located adjacent to containers. If space heaters are used, the warm air should be deflected away from the containers. Outside windows should be located or screened so that the rays of the sun do not fall directly on chlorine containers.

Natural ventilation may be adequate for a small chlorinator installation in a separate building when windows and doors

The proper procedure for emergency treatment of clothing or skin contaminated by chlorine is to flush the area with large quantities of water under a shower for at least 15 minutes.

While still under the shower, affected clothing should be removed. No medical treatment or neutralization of the chlorine should be attempted except as directed by a physician.

Immediate flushing with tepid water should be administered if even small quantities of chlorine enter the eye or if the eye has been exposed to strong concentrations of chlorine. The eyelids must be parted and thorough flushing continued for at least 15 minutes. As mentioned previously for skin exposure, no medical treatment or neutralization should be attempted except as directed by a physician.

IM 25.000AA UA (B/6-00) PAGE 13


The attending physician may wish to refer to a Material

Safety Data Sheet on chlorine as well as to the Chlorine

Institute’s Chlorine Manual and/or Pamphlet 63, First Aid and Medical Management of Chlorine Exposures.

WARNING: REPLACE FLEXIBLE CONNECTIONS

ANNUALLY, OR SOONER IF THERE IS EVIDENCE

OF DETERIORATION.

5.3 SAFETY PRECAUTIONS

The first steps to be taken in providing proper safety precautions at any facility are the selection of safety equipment to be on hand, the proper location of the equipment, and the training of all personnel in proper procedures to avoid unnecessary chlorine releases and to deal with releases that occur.

Emergency kits (meeting Chlorine Institute requirements) are available that can seal off most leaking areas of chlorine containers (i.e., valves, fusible plugs, or container wall). If these are on hand they must be used only by personnel thoroughly familiar with their use. The chlorine supplier should be contacted immediately for information, assistance, and advice on the disposition of the leaking container. The container should always be repositioned, if possible, so the leak is gas rather than liquid.

Proper respiratory equipment is essential for all facilities regardless of size. For maximum safety, it is preferable to use air tank type pressure demand masks that have a self-contained air supply and, therefore, are suitable regardless of chlorine concentration.

WARNING: NEVER UNDER ANY CIRCUMSTANCE

SPRAY WATER ON A CHLORINE LEAK. THIS WILL

ONLY MAKE IT WORSE.

Wall charts are available from most chlorine suppliers that provide much of the information contained in this manual.

All respiratory equipment must meet the requirements of the

National Institute for Occupational Safety and Health. Following the respiratory equipment manufacturer’s recommendation regarding maintenance and periodic testing is essential. This equipment should be stored outside the area containing chlorine or chlorine equipment in a manner protecting it from damage of any kind and so as to be readily available.

5.4 EMERGENCY ACTION PLANS

The best emergency plan includes routine practices that are designed to minimize emergencies. Proper maintenance of all equipment associated with the storage, handling, and use of chlorine in accordance with the manufacturer’s instructions is essential.

WARNING: DO NOT LOCK CABINETS OR CLOS-

ETS IN WHICH RESPIRATORY EQUIPMENT IS

STORED, AS THE EQUIPMENT MUST BE READILY

AVAILABLE.

All personnel with no assigned responsibility for dealing with a chlorine release should be instructed to leave the area.

Those responsible for correcting the situation should don respiratory equipment before doing so.

All equipment and piping containing chlorine under pressure must be tested periodically for leaks following procedures covered in Paragraph 4.8. Since it is not unusual for areas used for chlorine storage and chlorine equipment to be relatively unattended, it is important for the air in these areas to be monitored continuously with chlorine detectors, so that warning of leaks is given as early as possible. As with most emergencies, the earliest detection helps to minimize the damage to equipment and personnel. In addition to warning of leaks when the areas are unattended, chlorine detectors should warn of the presence of minor amounts of chlorine that may not be detected by personnel in the area.

Protective clothing is recommended for handling even routine operations involving chlorine. In the event of a substantial release, protective clothing is required. Anyone desiring further information on protective clothing should refer to the

Chlorine Institute Pamphlet 65, Protective Clothing for

Chlorine.

Some chlorine leaks are minor but all require immediate attention.

Safety shoes, hard hats, and safety glasses should be used in accordance with standard plant practice.

Most leaks will occur in piping, valves, connections, and the pressurized portions of chlorine equipment. These leaks will usually be eliminated by tightening packing, replacing gaskets, or repairing the equipment.

In the event of a major release of chlorine, there should be no delay in contacting the agency in the community that is responsible for handling hazardous material releases. Appropriate names and telephone numbers must be prominently posted.

The chlorine supplier is probably the best source of assistance for most chlorine users. In addition, the Chlorine Institute’s

Chlorine Emergency Plan (CHLOREP) can provide vital as-

IM 25.000AA UA (B/6-00) PAGE 14


sistance. In the United States this plan is activated through

CHEMTREC (toll free 800-4249300). In Canada, contact

CANUTEC (call collect 613-996-6666). These names and numbers must also be posted prominently.

The person responsible for making any of the calls listed above must be sure to give the agency contacted complete details including facility name, address, telephone number, and the names(s) of personnel to contact for further information. The description of the emergency should include size of container, corrective action already taken, local weather conditions, injuries, proximity to populated areas, and directions for easiest access to the site.

At some large installations, scrubbers have been installed so that areas containing chlorine or chlorine equipment can be sealed off and the air removed to a process that will absorb the chlorine. The design of such a system is complex and should only be attempted by those thoroughly familiar with the process.

Absorption systems have been provided at some facilities to permit a leaking container to be emptied quickly if this is deemed essential. One pound of chlorine can be absorbed by

1. 4 pounds of sodium hydroxide (caustic soda), 3.7 pounds of sodium carbonate (soda ash), or 1.3 pounds of calcium hydroxide (hydrated lime).

It is vital that the emergency plan include use of the “buddy system”, i.e., no personnel should be allowed to work alone in an area with a chlorine leak even if the second person is only standing by. As indicated earlier, all personnel not involved in locating and correcting the leak should leave the area travelling in a crosswind direction to an area that is upwind and above the leak. Since it may not be possible for all personnel to be equipped with respiratory equipment, they should be instructed to use a wet cloth or handkerchief over the nose and mouth while leaving the area.

No emergency plan should be implemented until it is reviewed by the chlorine supplier and the agency in the community having responsibility for hazardous material handling and disposal.

WARNING: TO AVOID SEVERE PERSONAL INJURY

WHEN USING CORROSIVE CHEMICALS, OBSERVE

ALL SAFETY PRECAUTIONS RECOMMENDED BY

THE CHEMICAL MANUFACTURER/ SUPPLIER.

In each case, one pound of the material should be dissolved in one gallon of water. Lime will actually be suspended in, rather than dissolved in, the water and requires constant agitation.

Chlorine Institute Pamphlet 64, Emergency Control Planning Checklist for Chlorine Facilities, may be of assistance in preparing the emergency plan. A Material Safety Data

Sheet for Chlorine, available from the Institute or the supplier, should also be consulted.

The tank and other equipment provided for an absorption system must be fabricated of materials suitable for the chemicals involved.

Provision must be made for dissolving the chlorine in the alkaline solution in such a way that the solution cannot be sucked back into the container.

Actually the safest way of disposing of the chlorine in the leaking container might be through the chlorination process, particularly if the process can absorb the chlorine at higher than normal rates without creating damage.

If it is apparent that fire will threaten or is present in a chlorine storage area, it is preferable to remove the containers. If this is not possible, the containers must be protected from the heat of the fire by spraying them with water. Do not spray water on any leaking container, however, since water will react with the chlorine, forming acids that will make the leak worse.

It is not generally permissible to ship a container damaged by leak or fire if it contains chlorine. If for some reason this seems necessary, the chlorine supplier must be contacted.

5.5 CHEMICAL DISPOSAL FACILITIES

Part of the planning for emergencies entails provision for disposal of any released chlorine. In most cases little can be done about the chlorine already released to the atmosphere except to try to prevent its dissipation into areas where damage to equipment and personnel will result.

IM 25.000AA UA (B/6-00) PAGE 15

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