1.3 MB
UFC 3-430-01FA
25 July 2003
UNIFIED FACILITIES CRITERIA (UFC)
HEATING AND COOLING
DISTRIBUTION SYSTEMS
APPROVED FOR PUBLIC RELEASE; DISTRIBUTION UNLIMITED
UFC 3-430-01FA
25 July 2003
UNIFIED FACILITIES CRITERIA (UFC)
HEATING AND COOLING DISTRIBUTION SYSTEMS
Any copyrighted material included in this UFC is identified at its point of use.
Use of the copyrighted material apart from this UFC must have the permission of the
copyright holder.
U.S. ARMY CORPS OF ENGINEERS (Preparing Activity)
NAVAL FACILITIES ENGINEERING COMMAND
AIR FORCE CIVIL ENGINEER SUPPORT AGENCY
Record of Changes (changes are indicated by \1\ ... /1/)
Change No.
Date
Location
This UFC supersedes TI 810-32 dated 10 January 2002. The text of this UFC is the text of TI 810-32.
The format of this document does not conform to UFC 1-300-01; however, it will be reformatted at
the next revision.
1
UFC 3-430-01FA
25 July 2003
FOREWORD
\1\
The Unified Facilities Criteria (UFC) system is prescribed by MIL-STD 3007 and provides
planning, design, construction, sustainment, restoration, and modernization criteria, and applies
to the Military Departments, the Defense Agencies, and the DoD Field Activities in accordance
with USD(AT&L) Memorandum dated 29 May 2002. UFC will be used for all DoD projects and
work for other customers where appropriate. All construction outside of the United States is
also governed by Status of forces Agreements (SOFA), Host Nation Funded Construction
Agreements (HNFA), and in some instances, Bilateral Infrastructure Agreements (BIA.)
Therefore, the acquisition team must ensure compliance with the more stringent of the UFC, the
SOFA, the HNFA, and the BIA, as applicable.
UFC are living documents and will be periodically reviewed, updated, and made available to
users as part of the Services’ responsibility for providing technical criteria for military
construction. Headquarters, U.S. Army Corps of Engineers (HQUSACE), Naval Facilities
Engineering Command (NAVFAC), and Air Force Civil Engineer Support Agency (AFCESA) are
responsible for administration of the UFC system. Defense agencies should contact the
preparing service for document interpretation and improvements. Technical content of UFC is
the responsibility of the cognizant DoD working group. Recommended changes with supporting
rationale should be sent to the respective service proponent office by the following electronic
form: Criteria Change Request (CCR). The form is also accessible from the Internet sites listed
below.
UFC are effective upon issuance and are distributed only in electronic media from the following
source:
•
Whole Building Design Guide web site http://dod.wbdg.org/.
Hard copies of UFC printed from electronic media should be checked against the current
electronic version prior to use to ensure that they are current.
AUTHORIZED BY:
______________________________________
DONALD L. BASHAM, P.E.
Chief, Engineering and Construction
U.S. Army Corps of Engineers
______________________________________
DR. JAMES W WRIGHT, P.E.
Chief Engineer
Naval Facilities Engineering Command
______________________________________
KATHLEEN I. FERGUSON, P.E.
The Deputy Civil Engineer
DCS/Installations & Logistics
Department of the Air Force
______________________________________
Dr. GET W. MOY, P.E.
Director, Installations Requirements and
Management
Office of the Deputy Under Secretary of Defense
(Installations and Environment)
2
CEMP-E
TI 810-32
10 January 2002
HEATING AND COOLING DISTRIBUTION SYSTEMS
Table of Contents
Page
CHAPTER 1. GENERAL INFORMATION
Paragraph 1-1. PURPOSE AND SCOPE.............................................................................. 1-1
1-2. APPLICABILITY............................................................................................... 1-1
1-3. REFERENCES............................................................................................... 1-1
1-4. EXCEPTIONS ................................................................................................. 1-1
1-5. DEFINITIONS.................................................................................................. 1-1
CHAPTER 2. SYSTEM SELECTION
Paragraph 2-1. GENERAL .................................................................................................. 2-1
2-2. DISTRIBUTION MEDIA SELECTION ........................................................... 2-1
2-3. SYSTEM TYPES ......................................................................................... 2-1
2-4. SYSTEMS SELECTION ............................................................................... 2-2
CHAPTER 3. GENERAL DISTRIBUTION SYSTEM DESIGN
Paragraph 3-1. GENERAL .................................................................................................... 3-1
3-2. SITE SOIL SURVEY..................................................................................... 3-1
3-3. UTILITY INVESTIGATION ............................................................................. 3-1
3-4. SYSTEM LAYOUT PLAN/PROFILE ............................................................. 3-1
3-5. EXPANSION COMPENSATION ................................................................... 3-2
3-6. VALVE MANHOLES ...................................................................................... 3-3
( Page 3-7 not used)
CHAPTER 4. HEAT DISTRIBUTION SYSTEMS IN CONCRETE TRENCHES
Paragraph 4-1. GENERAL .................................................................................................... 4-1
4-2. SYSTEM DESIGN ........................................................................................ 4-1
4-3. GENERAL CONSIDERATIONS ................................................................... 4-3
CHAPTER 5. PRE-ENGINEERED UNDERGROUND HEAT DISTRIBUTION SYSTEM
Paragraph 5-1. GENERAL..................................................................................................... 5-1
5-2. MANUFACTURER'S RESPONSIBILITY....................................................... 5-1
5-3. PROJECT DESIGNER'S RESPONSIBILITY............................................... 5-2
CHAPTER 6. PREFABRICATED UNDERGROUND HEATING/COOLING DISTRIBUTION
SYSTEM
Paragraph 6-1. GENERAL .................................................................................................... 6-1
6-2. SYSTEM DESIGN......................................................................................... 6-1
CHAPTER 7. ABOVEGROUND HEAT DISTRIBUTION SYSTEM
Paragraph 7-1. GENERAL .................................................................................................... 7-1
7-2. SYSTEM DESIGN........................................................................................ 7-1
i
CEMP-E
TI 810-32
10 January 2002
TECHNICAL INSTRUCTIONS
HEATING AND COOLING DISTRIBUTION SYSTEMS
Any copyrighted material included in this document is identified at its point of use.
Use of the copyrighted material apart from this document must have the permission of the copyright holder.
Approved for public release; distribution is unlimited.
This document reissued 10 January 2002.
Record of Changes (changes indicated \1\…/1/ )
No.
Date
Location
1
7 March 2002
Pages 4-1, 4-2, 5-1, and C-1
Table 4-2
Figures (editorial – changes not marked) 3-1 thru 3-28, 4-1, and 4-3
2
30 Sept 2002
Page 1-1
Figures (editorial – changes not marked) 3-14, 3-28, 4-4, 4-5, 4-17,
and 7-7
CEMP-E
TI 810-32
30 August 1999
Reissued 10 January 2002
FOREWORD
These technical instructions (TI) provide design and construction criteria and apply to all U.S. Army Corps
of Engineers (USACE) commands having military construction responsibilities. TI will be used for all Army
projects and for projects executed for other military services or work for other customers where
appropriate.
TI are living documents and will be periodically reviewed, updated, and made available to users as part of
the HQUSACE responsibility for technical criteria and policy for new military construction. CEMP-ED is
responsible for administration of the TI system; technical content of TI is the responsibility of the
HQUSACE element of the discipline involved. Recommended changes to TI, with rationale for the
changes, should be sent to HQUSACE, ATTN: CEMP-ED, 20 Massachusetts Ave., NW, Washington, DC
20314-1000.
TI are effective upon issuance. TI are distributed only in electronic media through the TECHINFO Internet
site http://www.hnd.usace.army.mil /techinfo/index.htm and the Construction Criteria Base (CCB) systems
maintained by the National Institute of Building Sciences at Internet Site http://www.nibs.org/ccb/. Hard
copies of these instructions produced by the user from the electronic media should be checked against
the current electronic version prior to use to assure that the latest instructions are used.
FOR THE COMMANDER:
DWIGHT A. BERANEK, P.E.
Chief, Engineering and Construction Division
Directorate of Military Programs
CEMP-E
TI 810-32
10 January 2002
HEATING AND COOLING DISTRIBUTION SYSTEMS
Table of Contents
Page
CHAPTER 1. GENERAL INFORMATION
Paragraph 1-1. PURPOSE AND SCOPE.............................................................................. 1-1
1-2. APPLICABILITY............................................................................................... 1-1
1-3. REFERENCES............................................................................................... 1-1
1-4. EXCEPTIONS ................................................................................................. 1-1
1-5. DEFINITIONS.................................................................................................. 1-1
CHAPTER 2. SYSTEM SELECTION
Paragraph 2-1. GENERAL .................................................................................................. 2-1
2-2. DISTRIBUTION MEDIA SELECTION ........................................................... 2-1
2-3. SYSTEM TYPES ......................................................................................... 2-1
2-4. SYSTEMS SELECTION ............................................................................... 2-2
CHAPTER 3. GENERAL DISTRIBUTION SYSTEM DESIGN
Paragraph 3-1. GENERAL .................................................................................................... 3-1
3-2. SITE SOIL SURVEY..................................................................................... 3-1
3-3. UTILITY INVESTIGATION ............................................................................. 3-1
3-4. SYSTEM LAYOUT PLAN/PROFILE ............................................................. 3-1
3-5. EXPANSION COMPENSATION ................................................................... 3-2
3-6. VALVE MANHOLES ...................................................................................... 3-3
( Page 3-7 not used)
CHAPTER 4. HEAT DISTRIBUTION SYSTEMS IN CONCRETE TRENCHES
Paragraph 4-1. GENERAL .................................................................................................... 4-1
4-2. SYSTEM DESIGN ........................................................................................ 4-1
4-3. GENERAL CONSIDERATIONS ................................................................... 4-3
CHAPTER 5. PRE-ENGINEERED UNDERGROUND HEAT DISTRIBUTION SYSTEM
Paragraph 5-1. GENERAL..................................................................................................... 5-1
5-2. MANUFACTURER'S RESPONSIBILITY....................................................... 5-1
5-3. PROJECT DESIGNER'S RESPONSIBILITY............................................... 5-2
CHAPTER 6. PREFABRICATED UNDERGROUND HEATING/COOLING DISTRIBUTION
SYSTEM
Paragraph 6-1. GENERAL .................................................................................................... 6-1
6-2. SYSTEM DESIGN......................................................................................... 6-1
CHAPTER 7. ABOVEGROUND HEAT DISTRIBUTION SYSTEM
Paragraph 7-1. GENERAL .................................................................................................... 7-1
7-2. SYSTEM DESIGN........................................................................................ 7-1
i
CEMP-E
TI 810-32
10 January 2002
CHAPTER 8. SPECIAL CONSIDERATIONS
Paragraph 8-1. GENERAL .................................................................................................... 8-1
8-2. STEAM SYSTEMS ....................................................................................... 8-1
8-3. HTHW SYSTEMS ........................................................................................ 8-3
8-4. LTHW and CW SYSTEMS .......................................................................... 8-3
APPENDIX A.
APPENDIX B.
APPENDIX C.
APPENDIX D.
REFERENCES ................................................................................................... A-1
PRESSURE DROP vs. FLOW CHART .............................................................B-1
CONDENSATION LOAD CALCULATIONS (NORMAL) .....................................C-1
CONDENSATION LOAD CALCULATIONS (STARTUP)....................................D-1
List of Figures
Title
Page
Figure 3-1. Typical valve manhole plan........................................................................... 3-8
3-2. Access Ladder detail..................................................................................... 3-9
3-3. Typical isolation flange detail....................................................................... 3-10
3-4. Typical valve/piping support detail............................................................... 3-11
3-5. Valve manhole elevation and section .......................................................... 3-12
3-6. Raised cover plate design .......................................................................... 3-13
3-7. Section A-A of raised cover plate ................................................................ 3-14
3-8. Section B-B of raised cover plate................................................................ 3-15
3-9. Section C-C of raised cover plate ............................................................... 3-16
3-10. Detail of raised cover plate......................................................................... 3-17
3-11. Lifting lug detail ........................................................................................... 3-18
3-12. Handle detail ............................................................................................... 3-19
3-13. Notes for raised cover plate ....................................................................... 3-20
3-14. Typical support cover plan (grate support) ............................................... 3-21
3-15. Detail of angle support for grating ............................................................. 3-22
3-16. Detail of structural support for grating....................................................... 3-23
3-17. Grating support steel locations.................................................................. 3-24
3-18. Detail of checker plate cover..................................................................... 3-25
3-19. Typical concrete cover plan ...................................................................... 3-26
3-20. Concrete cover details .............................................................................. 3-27
3-21. Gooseneck detail....................................................................................... 3-28
3-22. Valve manhole floor drain detail................................................................. 3-29
3-23. Remote sump basin.................................................................................. 3-30
3-24. Sump basin cover detail............................................................................ 3-31
3-25. Sump basin electrical details .................................................................... 3-32
3-26. Sump pump wiring diagram ...................................................................... 3-33
3-27. Valve manhole sump electrical details ...................................................... 3-34
3-28. Casing wall penetration detail.................................................................... 3-35
(Page 3-36 not used)
4-1. Free pipe support detail................................................................................. 4-4
4-2. Guided pipe support detail............................................................................. 4-5
4-3. Pipe anchor detail.......................................................................................... 4-6
4-4. Pipe support channel..................................................................................... 4-7
4-5. Trench dimension section............................................................................. 4-8
ii
CEMP-E
TI 810-32
10 January 2002
4-25
CEMP-E
TI 810-32
10 January 2002
CHAPTER 1
GENERAL INFORMATION
1-1. PURPOSE AND SCOPE. This document provides criteria and guidance for the design and
construction of heating and cooling distribution systems and supplements information in the "Notes to
the Designer" of the guide specifications. These distribution systems include Heat Distribution
Systems in Concrete Trenches, Pre-engineered Underground Heat Distribution Systems, Prefabricated
Underground Heating/Cooling Distribution Systems, and Aboveground Heat Distribution Systems. The
mediums used in these distribution systems, as defined by the Department of Defense (DoD), include:
a. High temperature hot water (HTHW) (251 deg. F to 450 deg. F)
b. Low temperature hot water (LTHW) (150 deg. F to 250 deg. F)
c. Low pressure steam systems (up to 15 psig)
d. High pressure steam systems (over 15 psig)
e. Condensate return systems (up to 200 deg. F)
f. Chilled water systems.
1-2. APPLICABILITY. These instructions are applicable to all \2\ DoD agencies /2/ and their
contractors involved in the design and construction of heating and cooling distribution systems.
1-3. REFERENCES. Appendix A contains a list of references used in these instructions.
1-4. EXCEPTIONS. Generally, this document covers heating and cooling distribution systems most
typically installed on United States military installations. However, deviations from the recommendations
of this manual may be necessary when unusual site conditions are present or specific using service
requirements are encountered. For example, the manual does not discuss design problems associated
with arctic and subarctic construction, in which case, the designer should refer to the "Cold Climate
Utilities Manual", 1986, Canadian Society of Civil Engineers, Montreal, Quebec.
1-5. DEFINITIONS. The term "designer" used throughout this manual refers to the person or persons
responsible for preparing contract drawings and specifications for a heating or cooling distribution
design. The main engineering discipline areas of the "designer" are:
a. Mechanical. Includes expansion compensation, stress analysis, piping system design (fittings,
valves, insulation), equipment selection and sizing, and pipe sizing and routing.
b. Structural. Includes reinforced concrete design, pipe supports, and valve manhole cover
design.
c. Electrical. Includes cathodic protection, electrical service and controls (e.g. sump pumps).
d. Civil. Includes earth work, road crossings (for buried systems), system plans and profiles, and
area drainage designs .
1-1
CEMP-E
TI 810-32
10 January 2002
8-4. LTHW and CW systems.
a. Pipe Sizing. The most efficient method of determining pipe size for LTHW and CW systems is to use
head loss vs. flow rate charts such as those found in ASHRAE Fundamentals, Chapter "Pipe Sizing". These tables
are based on 60 deg. F water so for chilled water pipe sizing there is little error introduced using these charts. For
LTHW systems, the use of the charts does introduce some error. However, the error is on the conservative side
(the charts overstate the pressure drop of LTHW).
b. LTHW and CW Material Selection.
(1) Valves. Typically, valves on either LTHW or CW systems will be 150-pound class and will be
located in the valve manholes. Ball valves provide a good means for line isolation. Although nonmetallic valves
are sometimes allowed for these systems, metallic valves should be used for durability.
(2) Piping. The most common piping materials used for LTHW and CW systems are steel, copper
tubing, reinforced thermosetting resin pipe (fiber- glass) and, for CW only, polyvinyl chloride and polyethylene.
However, do not include nonmetallic piping in the same valve manholes with HTHW and steam systems. Chilled
water lines using PVC piping must be installed in separate valve manholes since PVC can be thermally
damaged at relatively low temperatures. Outside the valve manholes, a separation of 15 feet (minimum) must be
maintained between pre-engineered underground HTHW and steam systems and PVC encased, prefabricated
underground heating/cooling distribution systems to avoid thermal degradation of the PVC.
8-4
CEMP-E
TI 810-32
10 January 2002
Table 8-1. Pipe sizing guidelines for condensate return systems.
TWO-PIPE SYSTEM SIZING GUIDELINES
_____________________________________________________________________________
?? DETERMINE CONDENSATE LINE PRESSURE (AS OBSERVED FROM ON-SITE
PRESSURE GAGES).
?? DETERMINE CONDENSATE LOAD (lbm/hr) FROM CENTRAL PLANT LOGS AND OTHER
INPUT.
?? ASSUME CONDENSATE AT TRAP DISCHARGE IS A COMBINATION OF CONDENSATE
AND FLASH STEAM.
?? SIZE LINE TO ACCOMMODATE 5,000 ft/min STEAM AND CONDENSATE MIXTURE
VELOCITY AND TO ENSURE MIXTURE PRESSURE IS HIGH ENOUGH TO OVERCOME
LINE LOSSES.
THREE-PIPE SYSTEM SIZING GUIDELINES
____________________________________________________________________________________
GRAVITY LINE
??
SLOPE AT 1 inch/20 feet (MINIMUM) TOWARD RECEIVER.
??
??
TOTAL PRESSURE DROP LESS THAN 0.25 psi.
LINE SIZE WILL BE TWO (2) INCHES.
PUMPED LINE
??
SIZE PUMPS TO MOVE CONDENSATE TO THE CENTRAL PLANT AT THE REQUIRED
HEAD AT 200 deg. F.
8-10
TI 810-32
10 January 2002
Technical Instructions
HEATING AND COOLING
DISTRIBUTION SYSTEMS
Headquarters
U.S. Army Corps of Engineers
Engineering Division
Directorate of Military Programs
CEMP-E
TI 810-32
10 January 2002
TECHNICAL INSTRUCTIONS
HEATING AND COOLING DISTRIBUTION SYSTEMS
Any copyrighted material included in this document is identified at its point of use.
Use of the copyrighted material apart from this document must have the permission of the copyright holder.
Approved for public release; distribution is unlimited.
This document reissued 10 January 2002.
Record of Changes (changes indicated \1\…/1/ )
No.
Date
Location
1
7 March 2002
Pages 4-1, 4-2, 5-1, and C-1
Table 4-2
Figures (editorial – changes not marked) 3-1 thru 3-28, 4-1, and 4-3
2
30 Sept 2002
Page 1-1
Figures (editorial – changes not marked) 3-14, 3-28, 4-4, 4-5, 4-17,
and 7-7
CEMP-E
TI 810-32
30 August 1999
Reissued 10 January 2002
FOREWORD
These technical instructions (TI) provide design and construction criteria and apply to all U.S. Army Corps
of Engineers (USACE) commands having military construction responsibilities. TI will be used for all Army
projects and for projects executed for other military services or work for other customers where
appropriate.
TI are living documents and will be periodically reviewed, updated, and made available to users as part of
the HQUSACE responsibility for technical criteria and policy for new military construction. CEMP-ED is
responsible for administration of the TI system; technical content of TI is the responsibility of the
HQUSACE element of the discipline involved. Recommended changes to TI, with rationale for the
changes, should be sent to HQUSACE, ATTN: CEMP-ED, 20 Massachusetts Ave., NW, Washington, DC
20314-1000.
TI are effective upon issuance. TI are distributed only in electronic media through the TECHINFO Internet
site http://www.hnd.usace.army.mil /techinfo/index.htm and the Construction Criteria Base (CCB) systems
maintained by the National Institute of Building Sciences at Internet Site http://www.nibs.org/ccb/. Hard
copies of these instructions produced by the user from the electronic media should be checked against
the current electronic version prior to use to assure that the latest instructions are used.
FOR THE COMMANDER:
DWIGHT A. BERANEK, P.E.
Chief, Engineering and Construction Division
Directorate of Military Programs
CEMP-E
TI 810-32
10 January 2002
HEATING AND COOLING DISTRIBUTION SYSTEMS
Table of Contents
Page
CHAPTER 1. GENERAL INFORMATION
Paragraph 1-1. PURPOSE AND SCOPE.............................................................................. 1-1
1-2. APPLICABILITY............................................................................................... 1-1
1-3. REFERENCES............................................................................................... 1-1
1-4. EXCEPTIONS ................................................................................................. 1-1
1-5. DEFINITIONS.................................................................................................. 1-1
CHAPTER 2. SYSTEM SELECTION
Paragraph 2-1. GENERAL .................................................................................................. 2-1
2-2. DISTRIBUTION MEDIA SELECTION ........................................................... 2-1
2-3. SYSTEM TYPES ......................................................................................... 2-1
2-4. SYSTEMS SELECTION ............................................................................... 2-2
CHAPTER 3. GENERAL DISTRIBUTION SYSTEM DESIGN
Paragraph 3-1. GENERAL .................................................................................................... 3-1
3-2. SITE SOIL SURVEY..................................................................................... 3-1
3-3. UTILITY INVESTIGATION ............................................................................. 3-1
3-4. SYSTEM LAYOUT PLAN/PROFILE ............................................................. 3-1
3-5. EXPANSION COMPENSATION ................................................................... 3-2
3-6. VALVE MANHOLES ...................................................................................... 3-3
( Page 3-7 not used)
CHAPTER 4. HEAT DISTRIBUTION SYSTEMS IN CONCRETE TRENCHES
Paragraph 4-1. GENERAL .................................................................................................... 4-1
4-2. SYSTEM DESIGN ........................................................................................ 4-1
4-3. GENERAL CONSIDERATIONS ................................................................... 4-3
CHAPTER 5. PRE-ENGINEERED UNDERGROUND HEAT DISTRIBUTION SYSTEM
Paragraph 5-1. GENERAL..................................................................................................... 5-1
5-2. MANUFACTURER'S RESPONSIBILITY....................................................... 5-1
5-3. PROJECT DESIGNER'S RESPONSIBILITY............................................... 5-2
CHAPTER 6. PREFABRICATED UNDERGROUND HEATING/COOLING DISTRIBUTION
SYSTEM
Paragraph 6-1. GENERAL .................................................................................................... 6-1
6-2. SYSTEM DESIGN......................................................................................... 6-1
CHAPTER 7. ABOVEGROUND HEAT DISTRIBUTION SYSTEM
Paragraph 7-1. GENERAL .................................................................................................... 7-1
7-2. SYSTEM DESIGN........................................................................................ 7-1
i
CEMP-E
TI 810-32
10 January 2002
4-6. Construction joint detail ................................................................................. 4-9
4-7. Typical trench section ................................................................................. 4-10
4-8. Trench corner detail .................................................................................... 4-11
4-9. Typical lifting devices................................................................................... 4-12
4-10. Typical trench road crossing..................................................................... 4-13
4-11. Trench crossing with curb and gutter ....................................................... 4-14
4-12. Trench crossing with drain pan................................................................. 4-15
4-13. Parking lot crossing; exposed top ............................................................. 4-16
4-14. Parking lot crossing; covered top.............................................................. 4-17
4-15. Sidewalk transverse section detail............................................................ 4-18
4-16. Expansion loop detail................................................................................. 4-19
4-17. Trench cover joint detail ............................................................................ 4-20
4-18. Access cover detail ................................................................................... 4-21
4-19. Vent and drain details ................................................................................ 4-22
5-1. Two-casing system detail ............................................................................. 5-4
5-2. Single casing system detail........................................................................... 5-5
5-3. Casing, vent, and drain detail ........................................................................ 5-6
7-1. Typical low profile support detail ................................................................... 7-3
7-2. Typical anchor pipe support .......................................................................... 7-4
7-3. Typical free pipe support ............................................................................... 7-5
7-4. Typical guided pipe support........................................................................... 7-6
7-5. Typical high profile base detail ...................................................................... 7-7
7-6. Typical pipe guide detail ................................................................................ 7-8
7-7. Typical pipe anchor detail.............................................................................. 7-9
7-8. Valve manhole top penetration detail........................................................... 7-10
8-1. Trap station layout schematic ....................................................................... 8-5
8-2. Accumulator detail......................................................................................... 8-6
8-3. Duplex condensate pump set connection detail ........................................... 8-7
8-4. Condensate cooling system for non-metallic pipe detail .............................. 8-8
8-5. Non-metallic pipe system anchor detail ........................................................ 8-9
List of Tables
Title
Table 3-1.
3-2.
3-3.
4-1.
4-2.
4-3.
4-4.
8-1.
Page
Valve manhole clearances......................................................................... 3-37
Valve manhole reinforcing steel sizes ....................................................... 3-38
Sump pump checklist................................................................................ 3-39
Channel support schedule......................................................................... 4-23
Support spacing schedule ......................................................................... 4-24
Trench dimension schedule ...................................................................... 4-25
Expansion loop schedule........................................................................... 4-25
Pipe sizing guidelines for condensate return systems.............................. 8-10
iii
CEMP-E
TI 810-32
10 January 2002
3-4. SYSTEM LAYOUT PLAN/PROFILE. All distribution systems require a layout plan and profile be
provided by the designer.
a. Layout plans will include, but not be limited to:
(1) system routing (including expansion loops and bends, manhole locations and anchor
locations).
(2) stationing numbering for the system (one dimensional coordinates from the point of origin of
the distribution system).
(3) all utilities within 25 feet of the system.
(4) all roads and buildings clearly labeled.
(5) types of surface conditions (asphalt, concrete, seeding, gravel, etc.).
(6) grade contour lines (new and existing).
(7) all dimensions and clearances to ensure accurate routing.
b. A profile of the system will also be drawn and, as a minimum, show:
(1) all system stationing numbering.
(2) system slope drawn to scale (1-inch to 20 feet minimum for all systems) to all low points.
(3) new and existing grade.
(4) all existing or new utilities shown at their actual burial depths.
3-5. EXPANSION COMPENSATION. All expansion systems, loops, and bends, will be sized in order to
prevent excessive pipe stresses (due mainly from thermal expansion) from exceeding those allowed by the
Power Piping Code, ASME B31.1. Mechanical expansion joints are not recommended for absorbing system
expansion. Mechanical expansion joints greatly increase the maintenance requirements of the distribution
systems. In the unlikely event that expansion joints must be used, they must be placed in an adequately
sized valve manhole. The designer is responsible for expansion calculations for Heat Distribution Systems in
Concrete Trenches, Prefabricated Underground Heating/Cooling Distribution Systems, and Aboveground
Heat Distribution Systems. The designer is also responsible for the expansion and stress determinations in
all the valve manholes, including the location of the equipment/pipe support locations. Even though the
manufacturer is responsible for the expansion calculations for Pre-Engineered Underground Heat Distribution
Systems, the calculations will be thoroughly reviewed by the designer at the shop drawing review. It is
recommended that a three dimensional finite element computer program be used for determining system
stresses. Many finite element software packages are available which operate on desktop computers. The
temperature differential used in the stress analysis will be the maximum temperature of the media less the
minimum temperature the system will encounter during a shutdown. All loops and bends will be sized based
on zero percent cold springing. Cold springing effects lessen over time and are difficult to maintain in the
event the system is ever cut, and shall therefore not be included in the analysis. However, loops may be
installed with cold springing as an added conservative measure.
3-6. VALVE MANHOLES. For all distribution systems, valve manholes will be designed by the
project designer. A valve manhole is required for all buried system lateral connections, all below
3-2
CEMP-E
TI 810-32
10 January 2002
CHAPTER 4
HEAT DISTRIBUTION SYSTEMS IN CONCRETE TRENCHES
4-1. GENERAL. The concrete shallow trench (CST) is a system, which allows insulated carrier pipes to
be routed underground but yet not have the piping in contact with the soil. The system also provides
comparatively easy access for maintenance and repair by means of removable concrete tops. These
exposed tops can be used as sidewalks since the system is installed at grade.
4-2. SYSTEM DESIGN. The designer is responsible for conducting a site investigation, designing the
distribution system plan and profiles, and designing the valve manholes, as described in chapter 3 of this
manual. In addition, the designer will use details and descriptions presented here to design a concrete
shallow trench system at a particular site.
a. Trench Systems - General.
(1) Piping and fittings. All carrier piping and pipe fittings will be carbon steel and will be designed
to satisfy the temperature and pressure requirements of the system. Materials will conform
to the
requirements in the guide specification.
(2) Pipe supports. Pipe supports will typically consist of three types: free, guided, and anchor.
These supports are detailed in figure 4-1, figure 4-2, and figure 4-3. All of these pipe supports will be
mounted on channel supports mounted to the trench walls as detailed in figure 4-4. Supports may be
mounted by other means, such as on concrete pedestals, provided that paths for water flow are
maintained. Table 4-1 provides guidance for the sizing of the channel supports. Note that the channels
for anchor supports in the table are designed for more substantial loads than required for free and guided
supports. The anchor support channel in this table is adequate for approximately 1,000 pounds force
axially. The designer will determine axial force requirements at all anchor points and design the channels
to accommodate these forces. \1\ Maximum distance between support channels shall be as listed in
table 4-2. /1/ These spacings are applicable to long, straight runs of piping only and must be reduced at
elbows, vertical risers, valving, and equipment. The actual spacings, in these instances, will be
determined by analyzing the pipe stresses with the pipe stress analysis, as described in chapter 3 of this
manual. The designer should note that there are other types of supports (such as roller type) that may
also be used. However, all supports must be capable of withstanding the thermal stresses and forces
exerted on them.
(3) Clearances. Clearances in the trench will be adequate to provide room for expansion,
movement, and a sufficient amount of access for cleaning and maintenance. There must also be
minimum of 4 inches clearance under the support channels to ensure ground water drainage along
trench floor. Figure 4-5 provides a trench cross-section, which corresponds to the table 4-3 trench
dimension schedule, which must be filled in by the designer.
air
a
the
(4) Insulation and jacketing. Insulation will be selected in accordance with insulation thickness
tables in the guide specification. These insulation thicknesses were developed using a life cycle cost
analysis. All insulations used have passed the Federal Agency Committee's boiling test
and are listed
in the guide specifications. All insulation in the trench will be covered with jacketing material in
conformance to the guide specification.
b. Trench System - Structural. The concrete trench will be field constructed of reinforced concrete
conforming to the current criteria. Trench walls and floors will be poured in place-they will not be precast.
Trench tops will be poured in place or precast. Walls, floors, and tops will be constructed with 4,000 psi
minimum compressive strength concrete. Reinforcing bars will conform to ASTM A 615, grade 60. Wall,
4-1
CEMP-E
TI 810-32
10 January 2002
floor, and top thicknesses shall be 6 inches, minimum. However, thicker sections may be required to
accommodate site specific loadings or to prevent flotation. Concrete trench floors shall be sloped at a 1
inch in 20 feet slope toward all low points to ensure proper drainage. Doweled or keyed joints and water
stops shall be provided at all construction joints and shall be detailed as shown in figure 4-6. Trench
reinforcing details will be provided and will be similar to the section shown in figure 4-7. Note that actual
concrete thicknesses and reinforcing bar sizes will be verified by the designer for each project. Trench
corners will be constructed as detailed in figure 4-8. Trench tops will be no longer than eight feet to allow
easy removal and placement.
c. Trench Top Removal Devices. The most common type of removal devices for the trench tops
will be the sling type as detailed in figure 4-9. Four lifting devices are required to lift a trench top. One set
of lifting devices will accommodate all trench tops for each contract. In some instances, sling type lifting
devices will not be convenient to use (eg. when the trench top butts up against a parallel sidewalk or when
the trench is routed through a parking area). In these instances, the designer shall require coil inserts to
be cast into the trench cover in four locations that will accommodate threaded lifting eye bolts. When not
being used, threaded plugs are inserted into the coil inserts. The lifting devices are also detailed in figure
4-9.
d. Road and Parking Lot Crossings. Road crossing requirements will be designed on a case by
case basis and must take into account pavement materials, soils, and frost characteristics of the design
site. A typical road crossing is shown in figure 4-10. Figure 4-11 details a concrete trench to curb and
gutter system transition and figure 4-12 details a concrete trench to drain pan system transition. In all
instances, the crown of the road crossing will be matched and the thickness of the trench top will be
designed to accommodate worst case loadings. Parking lot crossings typically will have the trench top
exposed at grade as shown in figure 4-13. Exposed tops allow for easier trench top removal over
extended lengths of paved areas. If appearance of the crossing is critical, black pigments may be added
to the concrete tops at the road crossing to match the surrounding pavement. In rare instances, the
trench tops may be covered with asphalt surfacing, as detailed in figure 4-14.
e. Sidewalk Intersections. In the event the trench system intersects an existing sidewalk, the
trench system will match the sidewalk as detailed in figure 4-15.
f. Expansion Compensation. Expansion loop and bend design is the responsibility of the designer,
and is covered in chapter 3 of this manual. The expansion loop design is critical. Sufficient space needs
to be provided in the expansion loop area to ensure that no pipe or insulation interference will occur due to
pipe movement as shown in figure 4-16. This detail indicates location of supports and also shows how the
piping system will be offset to allow for expansion movement in the trench. Table 4-4 is a typical loop
schedule, which corresponds to figure 4-16. The locations of the supports in the expansion loops will be
determined from the designer's piping stress analysis and then entered in Table 4-4. All piping stresses
will be less than ASME B31.1 allowables for each application. The designer will require inspection ports
be provided in the trench tops at each bend in the trench system routing for the purpose of observing pipe
movement at the bends during system startup. The inspection port is similar to the access cover detailed
in figure 4-18, except the nominal diameter of the lid will be 12 inches.
g. Sealants. The trench will be sealed to minimize the influx of ground water. A 1/4 inch thick
neoprene pad will be used between trench tops and tops of trench walls. The pad will have a minimum width
of 2 inches. All trench joints must be sealed with elastomeric sealants, which are available as a one or two
component system. Asphaltic sealants have not performed as reliably for this application. The elastomeric
sealant should be able to resist 50 percent total joint movement. The nonsagging type must be used for
vertical joints. The self-leveling type must be used for trench top butt joints as shown in figure 4-17. Other
horizontal joints may be sealed with either type of elastomeric sealant, but the sealant used in trench
bottoms must finish flush with the floor.
4-2
CEMP-E
TI 810-32
10 January 2002
L2
VERT. BARS
W2
W1
2'-4"
HORIZ. BARS
8" (typ.)
L1
PLAN IN SECTION
NO SCALE
L2
2" COVER
(TYP)
H1
(GRATE COVER SHOWN, FOR CONCRETE COVER SEE DETAIL A ON C-24)
VERT. BARS
HORIZ. BARS
4" CLEAR
(TYP)
TOP SECONDARY
REINFORCEMENT
TOP PRINCIPAL
REINFORCEMENT
#[email protected] VERTICAL BAR,
EMBED 24"(MIN.)
IN WALL
2" COVER
6"(TYP)
W.S.(TYP)
1'
W.S.
(TYP)
6"(TYP)
3" COVER(TYP)
BOTTOM PRINCIPAL REINFORCEMENT
BOTTOM SECONDARY REINFORCEMENT
*
VALVE MANHOLE SECTION*
NO SCALE
Figure 3-5. Valve Manhole Elevation and Section.
3-12
NOTE
SEE TABLE 3-2
FOR REINFORCEMENT
BAR SIZES.
CEMP-E
TI 810-32
10 January 2002
OUTSIDE PIT DIM. (LENGTH + 1")-(SEE
NOTE 1) FIG. 3-13
C 12X25
3"X2"X 5/16 "
A
Fig 3-7
3/8 " ALUMINUM PLATE
CONFORMING TO
ANSI H35.1
SLOPE
SLOPE
3"X2"X 5/16 "
(SEE NOTE 6
ON FIG. 3-16)
FLAT BAR 5/16 "LP X1"XLG
OF C12X25 (SEE NOTE 5
ON FIGURE 3-13
SUPPORT LP (TYP.)
5/16 " THICK ALUM.
HINGED CHECKER
TOP (TYP.)
2'-6"
OUT SIDE PIT DIM. (WIDTH + 1")-(SEE
NOTE 1) FIG. 3-13
HINGE (TYP.)
SLOPE
CORNERLP (TYP.)
B
Fig 3-8
HANDLE (TYP.)
SUPPORT LP (TYP.)
LADDER
C
Fig 3-9
RAISED COVER PLATE
NO SCALE
NOTE TO DESIGNER:
PLATE COVER SHOWN IS DESIGNED FOR LOADINGS UP TO 40 psf WHEN SPACING
BETWEEN SIDWALL AND CENTER SUPPORTS IS LESS THAN 3'6". LOADINGS OR
SPACINGS GREATER THAN THESE MUST BE DESIGNED FOR ON A CASE BY CASE BASIS.
Figure 3-6. Raised Cover Plate Design.
3-13
CEMP-E
TI 810-32
10 January 2002
6"
DETAIL - 1
(FIG. 3-10)
GRADE
CONC. PIT WALL
(TYP.)
SECTION A-A
NO SCALE
Figure 3-7. Section A-A of Raised Cover Plate.
3-14
CEMP-E
TI 810-32
10 January 2002
4-25
CEMP-E
TI 810-32
10 January 2002
Table 4-3. Trench dimension schedule.
TRENCH DIMENSION SCHEDULE
STANDARD
TRENCH
INTEM NO.
[PIPE
SIZES
(INCHES)
A
B1
B2
C*
D1
D2
6”
6”
6”
6”
6”
6”
6”
6”
E*
F
MIN.
Hw
MIN.
NOTES TO THE DESIGNER:
1. CLEARANCES BASED ON THE THICKEST INSULATION, IF LESS INSULATION (LOWER
“k”) IS PROVIDED. DIMENSIONS C, D, E AND F WILL BE DIFFERENT THAN SCHEDULED.
HOWEVER, OVERALL TRENCH DIMENSIONS SHSALL REMAIN THE SAME. C* & E*
DIMENSIONS MUST BE MAINTAINED THROUGHOUT ALL STRAIGHT SECTIONS OF
TRENCH TO ALLOW PROPER CLEARANCES FOR EXPANSION.
2. SCHEDULE DESIGNATIONS ARE ASSOCIATED WITH TRENCH DIMENSION SECTION,
FIGURE 4-5.
Table 4-4. Expansion Loop Schedule*
Loop
Name
Line
Sizes
X
Y
YY
Z
ZZ
W
H
U
REMARKS
*See Expansion Loop Detail for Designations (Figure 4-16).
NOTE TO THE DESIGNER:
If only one support is required along parallel leg of loop, ZZ =0. If only one
support is required along perpendicular legs of loop, YY = 0.
4-26
W
CEMP-E
TI 810-32
10 January 2002
CHAPTER 5
PRE-ENGINEERED UNDERGROUND HEAT DISTRIBUTION SYSTEM
5-1. GENERAL. Unlike Heat Distribution Systems in Concrete Trenches, which are totally designed by
the designer, Pre-engineered Underground Heat Distribution Systems are designed by the system
manufacturer. These pre-engineered systems are factory fabricated in lengths, which are transported
to the site for field assembly. Other types of systems and materials are continuously being evaluated
and will be included in guide specifications and this manual when deemed acceptable. There are two
types of these systems. The DDT type is allowed for severe, bad and moderate site conditions. In
severe sites allow only drainable-dryable-testable type systems. In bad and moderate sites allow DDT
and water spread limiting systems. These \1\ site /1/ conditions (or classifications) are described in
detail in the guide specifications. Although the manufacturer is responsible for the pre-engineered
system design, the project designer also has design responsibilities which include establishing the site,
soil, and groundwater conditions, pipe sizes, proposed routing (including construction limits) estimated
length, elevations, profiles of the system along with existing and finished earth surfaces and
obstructions \1\ within /1/ 8m (25 feet) of the system centerline including adjacent or crossing utilities.
The project designer also provides information on location and design of manholes and entrances to
buildings and manholes.
5-2. MANUFACTURER'S RESPONSIBILITY.
a. Pre-engineered Underground Heat Distribution System design. The manufacturer is responsible
for the Pre-engineered Underground Heat Distribution System. This responsibility includes any or all of
the following: insulation types, guided and anchor supports, end seals, casing and piping joint closure,
casing type and thickness, and carrier pipe depending on
the type of Pre-engineered Underground
Heat Distribution System provided. There are two types of Pre-Engineered Underground Heat Distribution
Systems. The drainable-dryable-testable system is a factory fabricated system, which includes a watertight outer protective casing of steel, an air space, and an insulated carrier steel pipe. Casing drains and
vents
are provided in end plates, which are installed in valve manholes. DDT systems can be used for
any heating medium including HTHW, high and low pressure steam, and condensate return and in any
site condition (severe, bad or moderate). The water spread limiting
systems is also a factory fabricated
system, which includes an outer protective casing and
an insulated carrier pipe. The system is
fabricated in sections, which are independent from each other. Ground water or condensate, which leaks
from or into one section, cannot travel into the next section. Field-assembly of the sections requires no
welding; the sections are pushed together and are sealed with a system of couplings and seals. WSL
systems can
be used only in bad and moderate site conditions. The designer must determine the
site conditions before a system type is selected. The site conditions will be considered severe, bad or
moderate based on the site investigation results. For DDT and WSL systems, steam and condensate
lines must always be installed in separate casings, as shown for a DDT system in figure 5-1, due to the
corrosion problems associated with condensate return systems. Water systems may use just one
casing for both supply and return pipes as detailed for a DDT system in figure 5-2, although installing the
pipes in separate casings is preferred by most users because it is less difficult to isolate leaks. The tops
of the casings will typically be buried between 2 and 6 feet below grade. However, note that excessive
burial depths increase the installation and repair costs and should be avoided where possible.
b. Expansion compensation. The manufacturer is responsible for the system expansion
compensation. A detailed stress analysis will be submitted for review as part of the contract requirements.
The manufacturer will normally make use of expansion loops and bends to absorb system expansion in DDT
systems. For WSL systems, field joints may be used to accommodate expansion. Except in rare
instances, expansion joints will not be permitted.
5-1
CEMP-E
TI 810-32
10 January 2002
c. Pre-engineered system's representative. The manufacturer is required to ensure that a qualified
direct employee of the system manufacturer is present to guarantee proper installation when the following
types of work are performed:
(1) inspection, unloading and storage of materials.
(2) inspection of trench prior to laying of casing.
(3) inspection of concrete thrust blocks.
(4) hydrostatic test of all service lines.
(5) field joint closure work.
(6) air test of casing.
(7) coating patch work.
(8) holiday test of casing coating.
(9) initial backfill up to 10 inches above the top of the casing.
(10) radiographic weld examination.
(11) startup and operation tests.
5-3. PROJECT DESIGNER’S RESPONSIBILITY.
a. Site information. As with all buried distribution systems, the site investigation is the responsibility of
the designer. As described in chapter 3 of this manual, the designer will obtain soil borings, be responsible for
designing the grading in the area, investigate all utilities for possible conflicts, and design for utility relocation as
necessary. The designer must then determine the site conditions (severe, bad, or moderate) before a system
type (DDT or WSL) is selected. The designer will then provide plans and profiles of the Pre-engineered system
routing. The designer will show approximate slope of the system (1 inch in 20 feet is required to ensure
drainage). This slope must be maintained in the entire system including through each leg of each expansion
loop to ensure proper system drainage.
b. Valve manholes. The designer will design all valve manholes for the system as described in chapter 3
of this manual. The manholes will be no further apart than 500 feet to minimize excavation if a leak in the
system must be found. The manholes will also be provided at all high (vent) points and low (drain) points in the
system. The valve manholes will include ground water drainage capabilities as explained in chapter 3. Casing
vents and drains will be included for maintenance of the casing air space in DDT systems as shown in figure
5-3.
c. Insulation. The insulation types used on the Pre-engineered Underground system will only be those
that are listed in the guide specification. The insulation thickness tables in the guide specification will be used
in determining required insulation thickness. These insulation thicknesses were developed using life cycle cost
analyses.
d. Cathodic protection. The designer will be responsible for the cathodic protection design for all
systems with coated steel casings. The designer shall also require that dielectric flanges be provided to isolate
the system’s cathodic protection system from non protected systems. These dielectric flanges shall always
be installed inside valve manholes.
e. Review. The designer will provide a detailed review of the manufacturer's shop drawings to ensure the
5-2
CEMP-E
TI 810-32
10 January 2002
system meets the requirements of the contract. As a minimum, the following items are required in this review
process:
(1) carrier pipe size and thickness.
(2) insulation thickness, type and K-value.
(3) casing material and thickness.
(4) casing coating material and thickness.
(5) verification of constant system slope to all low points (proposed elevations at all casing joints
on submitted shop drawing layouts).
(6) cathodic protection design.
(7) manufacturer’s system stress analysis.
5-3
CEMP-E
TI 810-32
10 January 2002
GRATING SUPPORT STEEL
L-LENGTH
(FT.)
W-WIDTH
(FT.)
VALVE
M.H.PLAN
REMARKS
A
4 OR LESS
AS REQ'D
NO MEMBER
REQ'D
B
GREATER
THAN 4 NOT
TO EXCEED 12
AS REQ'D NOT
TO EXCEED
12
ONE MEMBER
REQ'D
C
GREATER
THAN 12 NOT
TO EXCEED 16
GREATER
THAN 12 NOT
TO EXCEED 16
THREE
MEMBERS
REQ'D
NOTE: 1. FOR VALVE MANHOLE WITH DIMENSIONS L & W
GREATER THAN 16 FEET REQUIRES STEEL MEMBERS
AND GRATING TO BE DESIGNED FOR UNIFORM
LOADING OF 145 psf.
2. INTERSECTION OF STEEL MEMBERS MUST BE
DESIGNED FOR LOADING AND DIMENSIONS
INDICATED.
W
L
SEE NOTE 2
PLAN A
L
1/2 W
W10x26 TYP.
W
1/2 W
W
L
PLAN B
1/2 L
PLAN C
GRATING SUPPORT STEEL LOCATIONS
NO SCALE
Figure 3-17. Grating Support Steel Locations.
3-24
CEMP-E
NOTE:
TI 810-32
10 January 2002
PROVIDE A MINIMUM OF 4
CONNECTIONS PER PANEL.
CONNECTIONS SHALL BE 4 1/2 "
FROM EDGES OF PANELS AND
10" FROM ENDS OF PANELS.
3/8 " NUT-TACK WELD TO PLATE
1/8 " CHECKERED PLATE
2" SQ.X4" GALV. WASHER
GALV. STEEL GRATING
3/8 "0X1 1/2 " GALV. BOLT
CONNECTION FOR ATTACHING
CHECKERED PLATE TO GRATING
VARIES
VARIES
5/16 " ALUMINUM CHECKERED
PLATE IN CONFORMANCE
WITH ANSI H35.1.
PLATE WILL BE SAME
DIMENSION AS GRATING
SECTION IT COVERS
EXTEND ALUMINUM
CHECKERED PLATE
TO COVER BEAM
BLOCKOUTS
CHECKERED PLATES SHALL BE
PROVIDED WITH 12"X12"
VENTILATION OPENINGS AT
CORNERS (TYP.)
NOTE: SPACING BETWEEN PANELS AND BETWEEN
PANELS AND ANGLES SHALL BE 1/4 "
OPEN GRATE COVER W/CHECKER PLATE
CHECKER PLATE COVER DETAILS
NO SCALE
DESIGNER NOTE: CHECKERED PLATE TO BE USED TO COVER GRATING IN COLD CLIMATES
AND AREAS WHERE TRASH ACCUMULATION IS A CONCERN.
Figure 3-18. Detail of Checker Plate Cover.
3-25
CEMP-E
TI 810-32
10 January 2002
#[email protected] 9"O.C. EACH
WAY,TYP.
6" GOOSENECK
1'-2 1/2 "
IF CONCRETE TRENCH USED, THIS
PORTION OF CONCRETE MANHOLE LID'S
LIP TO BE DELETED TO ALLOW
TRENCH WALLS TO BUTT DIRECTLY
UP TO MANHOLE WALLS. TYPICAL OF
ALL MANHOLE TO TRENCH TRANSITIONS
C
(M
A
N
H
OL
E
C
O
VE
R)
F
4'(
A
C
C.
D
O
O
R)
1
A
(M
A
N
H IN
OLSI
E D
WE
ALFA
LSC
- E)
*
CONCRETE SHALLOW
TRENCH,(IF USED)
HINGES
(TYP.)
TWO
ADDITIONAL #5
EACH SIDE OF
OPENING
4'-0"X4'-0" ALUMINUM ACCESS
DOOR,"BILCO" MODEL JD-2AL
OR EQUAL W/SLIP RESISTANT
FINISH
LADDER
E
SECOND 6" GOOSENECK FOR
DIRECT BUIRIED SYSTEMS ONLY
B (MANHOLE WALLSINSIDE FACE)
1'-2 1/2 "
1'-2 1/2 "
4'(ACC. DOOR)
G
H
D (MANHOLE COVER)
(11'-0" max.)
CONCRETE COVER PLAN
NO SCALE
NOTE TO DESIGNER:
CONCRETE COVER DETAILED IS DESIGNED FOR LOADINGS UP TO 150 psf.
LOADINGS GREATER THAN THESE MUST BE DESIGNED FOR ON A CASE BY CASE BASIS.
Figure 3-19. Typical Concrete Cover Plan.
3-26
* SEE FIGURE 3-20
FOR SECTION
1
CEMP-E
TI 810-32
10 January 2002
CHAPTER 8
SPECIAL CONSIDERATIONS
8-1. GENERAL. Although it is impractical to cover all special considerations, which arise in heating and
cooling distribution designs, this chapter presents typical design problems and solutions associated with
steam, high temperature hot water, low temperature hot water and chilled water systems.
8-2. STEAM SYSTEMS.
a. Trap Selection. Steam traps are used to separate the condensate and non-condensable gases
from the steam. Many types of traps are used on drip legs for steam distribution systems. Those trap
types include float and thermostatic (F&T), inverted bucket, thermostatic and thermodynamic (disc).
However, for buried heat distribution drip leg applications, inverted bucket or thermostatic (bimetallic type)
should be the trap types selected. For drip leg applications where freezing is a consideration,
thermodynamic type (installed vertically) or bimetallic thermostatic type should be selected.
b. Trap Sizing and Location. Trap sizing is important for obtaining an efficient steam distribution
system. Condensation in the steam line is caused by heat loss from the steam line. Trap life will be
shortened, function affected and excessive energy will be wasted if traps are oversized to handle the higher
initial startup condensate flows. Therefore, the traps should be sized for the condensate load seen during
the distribution system normal operation. Because the traps are not sized for startup loadings, the bypass
must be opened at startup to allow condensate to pass until the steam line has reached normal operating
temperatures (see figure 8-1). The designer will calculate heat loss and condensate flow for that particular
design using the methods presented in appendix D for determining condensate loads during normal
operation. It is critical that the designer calculate trap capacity using the Appendix D method for each trap
station in the design to ensure proper steam system operation. In addition to trap capacity, steam trap
type, differential pressures, and inlet pressure must always be provided on the contract documents. Do not
locate steam drip legs, with associated traps, more than 500 feet apart.
c. Drip Leg Sizing. Drip legs, installed vertically down from the steam pipe, are used to collect
condensate. Design all steam lines to slope at 1 inch in 20 feet minimum toward these drip legs. It is
preferable to slope the steam lines in the direction of steam flow whenever possible. The steam trap line
and bypass line are connected to the drip leg as indicated in figure 8-1. The drip leg will be the same
nominal pipe size as the main line (up to a 12-inch line) and will provide a storage capacity equal to 50% of
the startup condensate load (no safety factor, one-half of an hour duration) for line sizes 4 inches in diameter
and larger and 25% of the startup condensate load (no safety factor, one-half of an hour
duration) for line
sizes less than 4 inches. In no case will the drip leg be less than 18 inches in length or larger than 12
inches in diameter for all steam line sizes. The designer will calculate startup loads for drip leg sizing using
the methods presented in appendix D.
d. Trap Station Layout. All trap stations will be piped as indicated in figure 8-1, as a minimum. Valve
and strainer sizes will match the line sizes on which they are installed. Pipe lines to and from the steam trap
will be sized based on calculated trap capacity but will be no less than 3/4-inch nominal size (line size "A" on
figure 8-1). If reducing fittings are needed at the trap inlet and outlet, eccentric reducers must be used. The
bypass line will be sized to accommodate warm-up condensate loads. For steam systems with an operating
pressure of 150 psig or less and pipe sizes 12 inches or less, provide a ¾-inch bypass line. If the condensate
return main is a low pressure or gravity flow type, the trap discharge line will be routed through an
accumulator, as indicated in figure 8-2. The accumulator will lower the trap discharge temperature and
minimize flashing when the condensate is introduced into sloped condensate lines which are routed to
receiver/pump sets located in valve manholes. The pumps push the condensate back to the central plant in a
separate pressurized condensate line. See figure 8-3 for a duplex condensate pump set connection detail.
8-1
CEMP-E
TI 810-32
10 January 2002
SLOPE VAULT FLOOR
TO FLOOR DRAIN
6" MIN.
RAISED "HAT TYPE"
PIPE SCREEN MOUNTED
TO FLOOR DRAIN
4" DRAIN PIPE DRAIN EXTENDED AT UNIFORM
SLOPE TO SUMP BASIN OR STORM DRAIN AS
INDICATED ON PLANS.
CAST IRON FLOOR DRAIN WITH
METALIC SPHERE OR FLAPPER
TYPE BACKWATER VALVE.
VALVE MANHOLE FLOOR DRAIN
NO SCALE
Figure 3-22. Valve Manhole Floor Drain Detail.
3-29
CEMP-E
TI 810-32
10 January 2002
CONCRETE SPLASHBLOCK TOP ELEVATION
MUST BE 6" BELOW SUMP
BASIN COVER & LOWER THAN
MANHOLE COVER
SEE FIGURE 3-24 FOR
SUMP BASIN COVER
DETAILS
ON-OFF FLOAT AND SWITCH (TYP.)
8"
ELECTRICAL BOX (SEE ELECT. DETAILS)
8"
2'-0"
8"
4" INLET
4" SANITARY TEE
2" GALVANIZED PUMP
DISCHARGE PIPE (TYP.)
6"
2'-6"
SUMP PUMP (TYP.)
SPLASHBLOCK TO BE INSTALLED
3" MIN. BELOW BASIN TOP
SECTION
1
45^ ELL W/
2 X 2 NIPPLE
TO DISCHARGE
ON SPLASHBLOCK
QUICK DISCONNECT
1
>
1
PIPE SLEEVE
ELECTRICAL BOXES-NEMA 4
ALARM FLOAT
36" REINFORCED CONCRETE PIPE
1/4 " FT. SLOPE
4"
4" SANITARY TEE
ON-OFF FLOAT AND SWITCH
4" GRAVITY INLET
6"
1 1/2 " - 2" INCREASER
14"
30 GPM, 25' HEAD PUMP (TYP.)
GROUT
6" 4"
OFF
NOTES:
SEE FIGURES 3-25 AND 3-26 FOR
SUMP BASIN ELECTRICAL DESIGN.
ELEVATION
SUMP BASIN WITH
DISCHARGE TO GRADE
.
SCALE. 1 INCH = 1 FOOT
12"
6"
0
1'
NOTE TO DESIGNER:
DEPTH DEPENDANT ON MAINTAINING 1/8 " / FT. SLOPE
FROM VAULT MANHOLE OUTLET TO THE SUMP BASIN.
DEPTH WILL BE A MINIMUM OF 4' OR A MINIMUM OF 1'
DEEPER THAN DESIGN FROST DEPTH, WHICHEVER
IS GREATER.
Figure 3-23. Remote Sump Basin.
3-30
AS REQUIRED *
2" SCHEDULE 40 GALVANIZED
PIPE W/COAL TAR COATING ON ALL
PIPES & FITTINGS BELOW GRADE
NON-SHRINKING
GROUT W/WATER STOP
CEMP-E
TI 810-32
10 January 2002
CHANNEL STRUT, SIMILAR OR
EQUAL TO "UNISTRUT" WELDED
TO BOTTOM EDGE OF
ANGLE FRAME
1/4 " X 3" X 3" STEEL ANGLE FRAME
CHANNEL STRUT
HANGER STRAP FOR MOUNTING
MISC. EQUIPMENT
CHANNEL STRUT
OPEN POSITION
OF COVER
AUTOMATIC HOLD
OPEN ARM
HANDLE
1/4 " STEEL
DIAMOND PLATE
COVER
1/4 " X 3" X 3"
STEEL ANGLE FRAME
REMOVABLE KEY
WRENCH
3"
STEEL STRAP
ANCHOR
HINGE
24" X 24"
3"
3"
CHANNEL
STRUT
27" X 24"
STANDARD LOCKING COVER
1/4 " STEEL
DIAMOND PLATE
COVER
1/4 " X 3" X 3"
STEEL ANGLE FRAME
HASP AND STAPLE
3"
STEEL STRAP
ANCHOR
HINGE
24" X 24"
3"
3"
CHANNEL
STRUT
27" X 24"
OPTIONAL LOCKING COVER
SUMP BASIN COVER
1
.
SCALE. 1 2 INCH = 1 FOOT
12"
9"
6"
3"
0
1'
Figure 3-24. Sump Basin Cover Details.
3-31
CEMP-E
TI 810-32
10 January 2002
Table 8-1. Pipe sizing guidelines for condensate return systems.
TWO-PIPE SYSTEM SIZING GUIDELINES
_____________________________________________________________________________
?? DETERMINE CONDENSATE LINE PRESSURE (AS OBSERVED FROM ON-SITE
PRESSURE GAGES).
?? DETERMINE CONDENSATE LOAD (lbm/hr) FROM CENTRAL PLANT LOGS AND OTHER
INPUT.
?? ASSUME CONDENSATE AT TRAP DISCHARGE IS A COMBINATION OF CONDENSATE
AND FLASH STEAM.
?? SIZE LINE TO ACCOMMODATE 5,000 ft/min STEAM AND CONDENSATE MIXTURE
VELOCITY AND TO ENSURE MIXTURE PRESSURE IS HIGH ENOUGH TO OVERCOME
LINE LOSSES.
THREE-PIPE SYSTEM SIZING GUIDELINES
____________________________________________________________________________________
GRAVITY LINE
??
SLOPE AT 1 inch/20 feet (MINIMUM) TOWARD RECEIVER.
??
??
TOTAL PRESSURE DROP LESS THAN 0.25 psi.
LINE SIZE WILL BE TWO (2) INCHES.
PUMPED LINE
??
SIZE PUMPS TO MOVE CONDENSATE TO THE CENTRAL PLANT AT THE REQUIRED
HEAD AT 200 deg. F.
8-10
CEMP-E
TI 810-32
10 January 2002
APPENDIX A
REFERENCES
Government Publications
Department of the Army
TM 5-802-1
Economic Studies for Military Construction Design-Applications
TM 5-809-1
Load Assumption for Buildings
Non-government Publications
American National Standards Institute (ANSI)
1430 Broadway, New York, NY 10018
H35.1
(1990) Alloy and Temper Design System for Aluminum
American Society for Testing and Materials (ASTM)
1916 Race Street, Philadelphia, PA 19103
A 36
(1991) Structural Steel
A 53
(1988a) Pipe, Steel, Black and Hot Dipped, Zinc
Coated, Welded and Seamless
A 123
(1989a) Zinc (Hot-Dip Galvanized) Coatings on
Iron and Steel Products
A 615
(1990) Deformed and Plain Billet-Steel Bars for
Concrete Reinforcement
American Society of Heating, Refrigerating, and Air Conditioning Engineers, Inc.,
1791 Tullie Circle, N.E., Atlanta, GA 30329
ASHRAE Handbook
Fundamentals
ASHRAE Handbook
HVAC Systems and Applications
American Society of Mechanical Engineers (ASME),
22 Law Drive, Box 2300, Fairfield, NJ 07007-2300
B31.1
(1989) Power Piping
Canadian Society of Civil Engineers,
Montreal, Quebec, Canada
(1986) Cold Climate Utilities Manual
A-1
CEMP-E
TI 810-32
10 January 2002
APPENDIX B
B-1
CEMP-E
TI 810-32
10 January 2002
APPENDIX C
CONDENSATION LOAD CALCULATIONS (NORMAL)
Step #1 Determine the heat loss per foot of line.
Q = 2? (Tst - Tout)/(ln(ro/ri )/kp + ln(rio /ro) /kin + 1/3r io )
Assumptions. This equation models an insulated pipe surrounded by air. The convective
resistance between the insulation and the outside of the pipe is assumed to be negligible. Also,
the convective heat transfer coefficient outside of the insulation is assumed to be 3 BTU/hr-ft2
deg. F.
Step #2 Determine the flow of condensate from the heat loss calculated in step #1.
m = Q/(hst - hcon)
Step #3 Multiply the flow rate per foot, calculated in step #2, by the total number of feet of steam
line that slopes toward the trap in question. The result is the minimum flow capacity of the trap.
where:
Q
= heat loss per foot of pipe; Btu/hr-ft
Tst
= temperature of steam; deg. F
Tout
= temperature of ambient conditions; deg. F
ro
= outside pipe radius; feet
ri
= inside pipe radius; feet
rio
= outside insulation radius; feet
kp
= thermal conductivity of pipe; Btu/hr-ft- deg. F; (26 Btu/hr-ft-deg. F for steel)
kin
= thermal conductivity of insulation; Btu/hr-ft- deg. F * (see table below)
m
= mass flow rate of condensate; lbm/hr-ft
hst
= enthalpy of saturated steam; Btu/lbm
hcon
= enthalpy of condensate; Btu/lbm
-----------------------\1\ *K-value (Btu/hr-ft-deg. F /1/
Insulation Type
Mineral Fiber
Calcium Silicate
400 deg. F
0.034
0.042
300 deg. F
0.029
0.038
C-1
200 deg. F
0.024
0.035
CEMP-E
TI 810-32
10 January 2002
APPENDIX D
CONDENSATION LOAD CALCULATIONS (STARTUP)
Step #1 Determine the heat loss per foot of line.
The startup load can be calculated by determining the amount of heat that is
required to heat the steam pipe from an ambient temperature to the saturation
temperature of the steam the pipe is to carry. This is done by using the
following equation:
Q
= (vp * c p * ? p (tst - Tout))/t; Btu/ft
where:
vp
= ? (ro2- r2); in ft3/ft
Step #2 Determine the pounds of condensate per foot from the heat loss calculated in step #1.
m
= Q/(hst - hcon); lbm/ft
Step #3 Multiply the condensate per foot, calculated in step #2, by the
total number of feet of steam line that slopes toward the drip leg in
question. Then convert the total pounds of condensate to gallons assuming
200 F condensate:
Total Condensate Volume (gallons)=(m*L)*7.49 gallons/ft3
60.1 lbm/ft3
where:
Q
Tst
Tout
ro
ri
m
hst
hcon
cp
?p
= heat loss per foot of pipe; Btu/hr-ft
= temperature of steam; deg. F
= temperature of ambient conditions; deg. F
= outside pipe radius; feet
= inside pipe radius; feet
= mass flow rate of condensate; lbm/hr-ft
= enthalpy of saturated steam; Btu/lbm
= enthalpy of condensate; Btu/lbm
= specific heat of pipe (steel); (0.10 to 0.11) Btu/lbm/degrees F
= density of pipe (steel); (489) lbm/ft3
t
= length of time for startup; hrs (typically 0.5 hrs.)
L
vp
= total length of pipe draining to drip; ft
= volume of pipe material per foot; ft3/ft
D-1
TI 810-32
10 January 2002
Technical Instructions
HEATING AND COOLING
DISTRIBUTION SYSTEMS
Headquarters
U.S. Army Corps of Engineers
Engineering Division
Directorate of Military Programs
CEMP-E
TI 810-32
10 January 2002
MATCH EXISTING
DRAIN PAN
8"MIN
1"MIN
6"MIN
1"MIN @ ROADS
DETAIL A
NO SCALE
STD TRENCH COVER
3'-0"
1'-6"
1'-6"
SEE TRENCH
COVER REINF.
1"MIN
7"
#[email protected] 6" O.C.
DRAIN PAN REINF.
#[email protected] EVEN SPACES
WIDTH OF TRENCH
COVER
NO SCALE
TRENCH CROSSING WITH DRAIN PAN
NOTE TO THE DESIGNER:
TRENCH CONCRETE THICKNESSES AND REINFORCEMENT SHOWN
MUST BE VERIFIED FOR EACH DESIGN BY THE DESIGNER.
Fig. 4-12. Trench Crossing With Drain Pan.
4-15
CEMP-E
TI 810-32
10 January 2002
SAW CUT
(TYPICAL)
BACKFILL
2"
(TYP.)
TACK COAT
EXISTING
GRADE
NEOPRENE GASKET
MATCH EXISTING
(TYPICAL)
WATERSTOP
COMPACTED
GRANULAR FILL
EXPOSED TOP
PARKING LOT TRANSVERSE SECTION
NO SCALE
Figure 4-13. Parking Lot Crossing; Exposed Top
4-16
CEMP-E
TI 810-32
10 January 2002
EXISTING BITUMINOUS
SURFACING
SAW CUT
(TYPICAL)
3" ASPHALT SURFACING
12"
MIN.
EXCAVATION WIDTH
12"
MIN.
1" MINIMUM
NEOPRENE GASKET
(TYP.)
TACK COAT
STABILIZED
BASE COURSE
WATERSTOP
COMPACTED
GRANULAR FILL
COVERED TOP
PARKING LOT TRANSVERSE SECTION
NO SCALE
Figure 4-14. Parking Lot Crossing; Covered Top
4-17
CEMP-E
TI 810-32
10 January 2002
Table 4-2. Support spacing schedule
\1\ MAXIMUM HORIZONTAL PIPE SUPPORT SPACING FOR STEEL /1/
DISTRIBUTION PIPING
PIPE SIZE
SPACING
(INCHES)
(FEET)
1
7
1-1/4
7
1-1/2
9
2
10
2-1/2
11
3
12
2-1/2
13
4
14
5
16
6
17
8
19
10
22
12
23
14
25
16
27
18
28
20
30
24
32
30
33
NOTES TO THE DESIGNER: These spacings are maximum for horizontal, straight
runs. More closely spaced supports must be provided for bends and risers and at
equipment.
4-24
CEMP-E
TI 810-32
10 January 2002
4-25
CEMP-E
TI 810-32
10 January 2002
Table 4-3. Trench dimension schedule.
TRENCH DIMENSION SCHEDULE
STANDARD
TRENCH
INTEM NO.
[PIPE
SIZES
(INCHES)
A
B1
B2
C*
D1
D2
6”
6”
6”
6”
6”
6”
6”
6”
E*
F
MIN.
Hw
MIN.
NOTES TO THE DESIGNER:
1. CLEARANCES BASED ON THE THICKEST INSULATION, IF LESS INSULATION (LOWER
“k”) IS PROVIDED. DIMENSIONS C, D, E AND F WILL BE DIFFERENT THAN SCHEDULED.
HOWEVER, OVERALL TRENCH DIMENSIONS SHSALL REMAIN THE SAME. C* & E*
DIMENSIONS MUST BE MAINTAINED THROUGHOUT ALL STRAIGHT SECTIONS OF
TRENCH TO ALLOW PROPER CLEARANCES FOR EXPANSION.
2. SCHEDULE DESIGNATIONS ARE ASSOCIATED WITH TRENCH DIMENSION SECTION,
FIGURE 4-5.
Table 4-4. Expansion Loop Schedule*
Loop
Name
Line
Sizes
X
Y
YY
Z
ZZ
W
H
U
REMARKS
*See Expansion Loop Detail for Designations (Figure 4-16).
NOTE TO THE DESIGNER:
If only one support is required along parallel leg of loop, ZZ =0. If only one
support is required along perpendicular legs of loop, YY = 0.
4-26
W
CEMP-E
TI 810-32
10 January 2002
CHAPTER 2
SYSTEM SELECTION
2-1. GENERAL. When designing a heating or cooling distribution system, the designer must
first select two critical items: media type and system type.
2-2. DISTRIBUTED MEDIA SELECTION.
a. Connecting to an existing system. Almost all heating and cooling distribution systems will be
connected to an existing central distribution system. In this case, the designer most often designs for the
media to which it is being connected-HTHW, LTHW, steam/condensate, or chilled water.
b. Installation of new system. When no existing system is present, the designer must select the
system that is most appropriate for the end user. High temperature hot water and steam/condensate
systems are the most common types of distribution systems currently used on military installations.
However, a new system should only use the temperatures and pressures necessary to meet the
requirements of the installation. For example, the use of high pressure steam sterilizers or steam kettles at
several facilities may require the use of a high pressure steam or HTHW system. However, it is usually
much more cost effective (on a first cost and life cycle cost basis) to use a low or medium temperature hot
water distribution systems whenever possible and to incorporate stand alone high pressure/temperature
systems where required. The lower maintenance costs, safer operation, longer life of systems, and simpler
system controls for hot water systems often offset the costs of larger piping required. For further assistance
for selecting the system type, refer to ASHRAE Handbook, "HVAC Systems and Equipment.”
2-3. SYSTEM TYPES. When selecting a distribution system, the designer must determine which system
types apply to a particular medium. The designer must also exclude systems which are not appropriate for
a particular site or for which the customer has no interest. Examples of this are locating aboveground
systems in non-industrial areas where the installation is sensitive to the aesthetic appearance of the area or
routing concrete shallow trench systems through drainage swales or flood plains.
a. Heat Distribution Systems in Concrete Trenches (chapter 4). This system is a buried system with
its removable concrete cover installed at grade and will typically be used for HTHW and steam/condensate
systems. In rare instances, it may also be used for chilled water and LTHW in the event no plastic piping
is installed in the same trench as high temperature (greater than 250 degrees F) piping systems.
Experience has shown that if insulation of a high temperature system is compromised, temperatures can
increase to such a level and cause damage to the plastic piping.
b. Pre-engineered Underground Heat Distribution Systems (chapter 5). This system is designed for
higher pressure and temperature applications. The two types of pre-engineered systems are the drainabledryable-testable (DDT) type which is used for high pressure steam/condensate and HTHW at all sites, and
high temperature hot water at any type of site, and the water spread limiting (WSL) type which is used only
for steam/condensate systems in bad and moderate sites. HTHW supply and return lines may be provided
in a single casing; however, steam and condensate lines must always be provided in separate casings
because condensate lines typically last less than half as long as the steam line and are easier to replace
when in a separate casing.
c. Prefabricated Underground Heating/Cooling Distribution System (chapter 6). This system is
designed for lower temperature and pressure applications. It is typically used for LTHW, chilled water, or
combination LTHW/chilled water systems.
d. Aboveground Heat Distribution System (chapter 7). This system may be used for HTHW,
steam/condensate, and LTHW systems, and for chilled water systems where freezing is not a concern.
2-1
CEMP-E
TI 810-32
10 January 2002
2-4. SYSTEM SELECTION. The system type selected will be based on the type of media that is
distributed.
a. High Temperature Water and Steam/condensate Systems. The order of preference for system
types for high temperature and high pressure systems are:
(1) Aboveground Heat Distribution System. This is the least expensive system and historically
requires the lowest maintenance and operating costs. However, the safety and aesthetics of an
aboveground system are not always desirable and must be accepted by the end user.
(2) Heat Distribution Systems in Concrete Trenches. This is the most dependable of the buried
distribution systems. The piping is totally accessible through removable concrete covers, the piping does
not come in contact with the soil, and ground water is drained away from the piping system to low point
drains. Except in rare instances, this is the system that should be selected if aboveground is not
acceptable with the end user.
(3) Pre-engineered Underground Heat Distribution System. This type of buried distribution
system should be selected as the last option due to very short system lives which are typically caused by
poor drainage, poor corrosion protection, and improper installation. Instances where it would be used would
be when aboveground is not acceptable with the end user or when drainage swales and high ground water
prevent the installation of a concrete trench system.
b. Low Temperature and Chilled Water Systems. The order of preference for system types for hot
water, chilled water or combination hot/chilled water are:
(1) Aboveground Heat Distribution System. This is the least expensive system and historically
requires the lowest maintenance and operating costs. However, the aesthetics of an aboveground system
are not always desirable and must be accepted by the end user. In addition, aboveground systems are
typically not used for chilled water because of potential freezing problems in colder climates and heat gain in
warmer areas.
(2) Prefabricated Underground Heating/Cooling Distribution System. This buried distribution
system is relatively inexpensive and dependable. The non-metallic casing materials provide excellent
protection from corrosion and the lower temperatures and pressures allow the system to operate for
extended periods of time. It is an excellent application for chilled water since the system is installed
underground, limiting the amount of heat gain to the system.
2-2
CEMP-E
TI 810-32
10 January 2002
CHAPTER 3
GENERAL DISTRIBUTION SYSTEM DESIGN
3-1. GENERAL. Some aspects of a heating or cooling distribution system design are similar regardless
of the system type. These aspects are covered in this chapter.
3-2. SITE SOIL SURVEY. After general routing has been proposed and before specific design has
begun, a detailed soil survey will be conducted for all distribution systems.
a. The survey will be made after the general layout of the system has been determined, will cover
the entire length of the proposed system, and will be made by a geotechnical engineer. The geotechnical
engineer will be a registered professional engineer with a minimum of three years of experience in the field
of soil mechanics and foundation design. This engineer must also be familiar with the local soil
conditions.
b. If at all possible, the survey should be conducted during the time of the year when the
ground-water table is at its highest point; if this is not possible, water table measurements will be
corrected, on the basis of professional judgement and local knowledge, to indicate conditions likely to
exist at the time of year when the water table is at its highest point. It may be necessary to dig test pits
at the worst locations to investigate the soil for evidence of high water table.
c. As a minimum, information on ground-water conditions, soil types, terrain, and precipitation
rates and irrigation practices in the area of the system will be collected. This information will be obtained
from available records at the installation. In addition, soil resistivity will be determined for
the cathodic
protection system design for Pre-Engineered Underground Heat Distribution Systems.
d. Information on ground-water conditions and soil types (in most cases not necessary for
Prefabricated Underground Heating and Cooling Distribution Systems and Aboveground Heat Distribution
Systems) will be obtained through borings, test pits, or other suitable exploratory means. Generally, a
boring test pit will be made at least every 100 feet along the line of the proposed system within areas of
prior construction. In open undisturbed natural areas the spacing of borings may be increased. Each
exploratory hole will extend to a level at least five feet below the anticipated elevation of the bottom of
the proposed system. If a significant difference in underground conditions
is found at adjacent
exploratory points, additional explorations will be made between those points in order to determine more
precisely where the change occurs. Upon completion of the survey, each exploration point will be
classified on the basis of the criteria presented in the guide specification for Pre-Engineered Underground
Heat Distribution Systems or in the guide specification for Heat Distribution Systems in Concrete Shallow
Trenches. The classification criteria is different for each system. Note that although classification is not
a requirement for design of Prefabricated Underground Heating and Cooling Distribution Systems or
Aboveground Heat Distribution Systems, the site survey, except for borings or test pits, must be
conducted to ensure that actual site
characteristics have been identified so that accurate plan and
profile drawings can be generated.
3-3. UTILITY INVESTIGATION. All existing, concurrently constructed and new utilities will be identified
if within 25 feet of the proposed distribution system routing. If the proposed routing crosses any utilities,
burial depths will be determined. Utility locations and depths can be verified through base personnel
familiar with utilities, base/post utility maps and by site visits. The designer is responsible for these site
visits to verify locations of utility interferences and to coordinate all other construction items with the user.
In the event utility information is not available, utility location consultants may be procured who specialize
in the location, identification and depth determination of utilities. If interferences exist, details will be
provided in the design to relocate utilities or modify system routing to avoid the interference.
3-1
CEMP-E
TI 810-32
10 January 2002
3-4. SYSTEM LAYOUT PLAN/PROFILE. All distribution systems require a layout plan and profile be
provided by the designer.
a. Layout plans will include, but not be limited to:
(1) system routing (including expansion loops and bends, manhole locations and anchor
locations).
(2) stationing numbering for the system (one dimensional coordinates from the point of origin of
the distribution system).
(3) all utilities within 25 feet of the system.
(4) all roads and buildings clearly labeled.
(5) types of surface conditions (asphalt, concrete, seeding, gravel, etc.).
(6) grade contour lines (new and existing).
(7) all dimensions and clearances to ensure accurate routing.
b. A profile of the system will also be drawn and, as a minimum, show:
(1) all system stationing numbering.
(2) system slope drawn to scale (1-inch to 20 feet minimum for all systems) to all low points.
(3) new and existing grade.
(4) all existing or new utilities shown at their actual burial depths.
3-5. EXPANSION COMPENSATION. All expansion systems, loops, and bends, will be sized in order to
prevent excessive pipe stresses (due mainly from thermal expansion) from exceeding those allowed by the
Power Piping Code, ASME B31.1. Mechanical expansion joints are not recommended for absorbing system
expansion. Mechanical expansion joints greatly increase the maintenance requirements of the distribution
systems. In the unlikely event that expansion joints must be used, they must be placed in an adequately
sized valve manhole. The designer is responsible for expansion calculations for Heat Distribution Systems in
Concrete Trenches, Prefabricated Underground Heating/Cooling Distribution Systems, and Aboveground
Heat Distribution Systems. The designer is also responsible for the expansion and stress determinations in
all the valve manholes, including the location of the equipment/pipe support locations. Even though the
manufacturer is responsible for the expansion calculations for Pre-Engineered Underground Heat Distribution
Systems, the calculations will be thoroughly reviewed by the designer at the shop drawing review. It is
recommended that a three dimensional finite element computer program be used for determining system
stresses. Many finite element software packages are available which operate on desktop computers. The
temperature differential used in the stress analysis will be the maximum temperature of the media less the
minimum temperature the system will encounter during a shutdown. All loops and bends will be sized based
on zero percent cold springing. Cold springing effects lessen over time and are difficult to maintain in the
event the system is ever cut, and shall therefore not be included in the analysis. However, loops may be
installed with cold springing as an added conservative measure.
3-6. VALVE MANHOLES. For all distribution systems, valve manholes will be designed by the
project designer. A valve manhole is required for all buried system lateral connections, all below
3-2
CEMP-E
TI 810-32
10 January 2002
to above ground system transitions, all drain points (low points), all below ground valving, all trap
stations, high points for vents of buried systems, and to minimize depth of buried systems.
Distance between valve manholes varies with different applications. However, spacing shall
never exceed 500 feet with Pre-Engineered Underground Heat Distribution Systems or
Prefabricated Underground Heating/Cooling Distribution Systems to minimize excavation when
searching for failures and to minimize effects of a failure. To enhance maintainability, avoid
valve manholes deeper than 6 feet.
a. Manhole internals. Layout of each manhole will be designed on a case by case basis.
(1) Equipment/valve locations. It is important to first layout, to scale, all manhole piping,
insulation, valving (with stems upright 90 degrees or less from vertical), and equipment and then locate the
manhole walls around these appurtenances to ensure adequate manhole size and room for maintenance
personnel. One line diagrams of piping and equipment are unacceptable. See figure 3-1 for a typical
manhole plan. Note that all valve manhole layouts have certain designer requirements in common. The
designer will:
(a) Provide main line isolation valves in valve manholes to most efficiently minimize outages to
buildings served by the distribution system. When installed, main line isolation valves will be located
downstream of the building's service laterals.
(b) Provide lateral isolation valves within the valve manholes for all laterals runs.
(c) Locate all carrier pipe vents and drains needed within the manhole for proper system
drainage of the main and lateral lines.
(d) Layout all valve manhole internals (valves and valve stems, pipe w/insulation, access
ladders, isolation flanges, and equipment) to scale to ensure adequate clearance has been provided for
operation and maintenance within the manhole.
(e) Ensure no non-metallic piping is routed in the manholes (i.e., as allowed with chilled water
or condensate return systems) which also serves high temperature mediums that could damage the
non-metallic piping. Damage to non-metallic piping is caused when manholes flood and the hot piping boils
the flood water. Boiling water can exceed the temperature allowables of many nonmetallic piping materials.
Because of this, the designer must transition to steel piping at the manholes (see figure 8-4).
(2) Clearances. Design will provide for clearance around piping and equipment in the manhole in
accordance with table 3-1.
(3) Access Ladders. Access ladders will be required on all valve manholes greater than 3 feet in
depth. Ladders will be welded steel and will consist of uprights and nonslip steps or rungs. Uprights will be not
less than 16 inches apart and steps or rungs will be spaced no greater than 12 inches apart. Ladders will
extend not less than 6 inches from the manhole wall and will be firmly anchored to the wall by steel inserts
spaced not more than three 3 feet apart vertically. All parts of the ladders will be hot-dipped galvanized after
fabrication in conformance with ASTM A 123. The top rung of the ladders shall be not more than 6 inches from
the top of the manhole. A typical valve manhole access ladder detail is shown in figure 3-2.
(4) Insulation. Insulation for valves, fittings, field casing closures, and other piping system
accessories in valve manholes will be of the same types and thicknesses as those provided in the distribution
systems' guide specification. All insulation will be premolded, precut, or job fabricated to fit and will be
removable and reusable. Insulation jackets will be provided for all pipe insulation in manholes and will comply
with the requirements of the particular distribution system guide specification.
3-3
CEMP-E
TI 810-32
10 January 2002
(5) Isolation flanges. Isolation flanges will be provided when connecting to an existing cathodically
protected heating or cooling distribution system or to prevent a new system's cathodic protection system
from contacting an existing system. The isolation flanges will be installed in the valve manhole and a typical
flange detail is shown in figure 3-3.
(6) Valve/piping supports. Piping in valve manholes often will need supports within the manhole
especially when larger valves or equipment are attached to the piping. These supports will be located on the
manhole plans as determined by the designer's expansion compensation calculations for each manhole
valving and equipment layout. Typical valve/piping support details are shown in figure 3-4.
b. Valve manhole construction. Valve manholes will be field constructed of reinforced concrete
conforming to the current criteria. Valve manholes will be constructed of 4,000 psi minimum compressive
strength concrete. Reinforcing bars will conform to ASTM A 615, grade 60. Typical reinforcing steel details
and sizing are shown in figure 3-5 and table 3-2 respectively. Concrete floor slabs and walls will be of
sufficient weight to prevent flotation in high water table areas. Floor slabs will be sloped to the drain which will
be installed in the floor slab. Concrete wall sections will be not less than 8 inches thick and must meet
anticipated load and soil conditions. Side walls will be constructed in a monolithic pour. Water stops will be
provided at all construction joints. Do not locate valve manholes in roads or parking areas which create an
inadequate amount of manhole ventilation and poor access.
c. Valve manhole covers. The valve manhole cover types discussed here are: raised solid plate,
supported cover, and concrete.
(1) Raised solid plate covers. Raised solid plate covers are preferred for HTHW and
steam/condensate systems installed in Pre-Engineered Underground Heat Distribution Systems. For shallow
concrete trench systems, the raised solid plate cover’s raised feature will interfere with the trench's walkway
function. When the valve manhole cover must remain flush with the trench top, the supported cover is the
preferred type. For the raised solid plate cover, ventilation openings are provided around the entire perimeter
below the raised top. The height of the valve manhole wall above grade (6 inches, minimum) shall be sufficient
to prevent surface water entry. The solid plate cover assembly is removable. The cover, constructed of
aluminum, also provides sectionalized access for inspection and maintenance. The solid plate cover raised
frame design and section, lifting lug, and handle details are shown in figure 3-6 through 3-12. Figure 3-13
contains notes for raised solid plate cover figures.
(2) Supported covers. Supported covers may be used for any distribution system covered in this
manual. For Pre-engineered Underground or Prefabricated Underground Heat Distribution Systems, design
the cover to be at least 6 inches above the surrounding grade. When used for concrete shallow trench
systems, the finished top will be flush with the concrete trench top. Required grates or other structural
members used for supporting covers to be made of corrosion resistant material such as aluminum or
galvanized steel. Details for the supporting cover are shown in figures 3-14 through 3-18. These details are
designed for loadings up to 150 psf and must be re-evaluated for larger loadings. Other structural solutions for
supporting the checkered plate are acceptable. The checkered plate cover (also referred to as diamond or
embossed plate) as shown in figure 3-18, will be installed over grating or other structural supports in most
locations to minimize the influx of leaves and other debris. The checkered plate is attached to the grating and
is removable.
(3) Concrete covers. The use of concrete covers is discouraged, but, if used, they must be used with
4 x 4 ft. aluminum doors for any distribution system covered in this manual. Concrete covers should only be
used if desired by the user or if specific design conditions exist, such as below to aboveground system
transitions. When used for Pre-engineered Underground or Prefabricated Underground Heat Distribution
Systems, design the top of the concrete cover to be a minimum of 6 inches above the surrounding grade.
When used for concrete shallow trenches, design the cover to be flush with the trench top. Concrete
requirements for this cover are similar to those required for valve manhole construction. Concrete cover will be
designed to support anticipated loadings. Figure 3-19 shows a typical concrete cover plan and figure 3-20
3-4
CEMP-E
TI 810-32
10 January 2002
provides construction details for this cover. The concrete cover detailed is designed for loadings up to 150 psf.
For greater loadings, the design must be re-evaluated. A disadvantage of concrete covers is the difficulty in
providing ventilation. For concrete shallow trench systems, a single 6 inch gooseneck pipe will be used, as
detailed in figure 3-21, to allow steam to exit the valve manhole if a leak or excessive heat loss is present.
Note that for shallow trench systems, the gooseneck will be installed off to one side of the valve manhole
concrete top to minimize pedestrian traffic interference. For Pre-engineered Underground Heat Distribution
Systems, two 6 inch goosenecks will be used. One will extend below the top as detailed in figure 3-21. The
other will be similar but will extend to within 8 inches of the valve manhole floor on the opposite side of the
manhole.
d. Valve manhole drainage. Drainage of water from the valve manhole is mandatory for the successful
operation and longevity of buried heating or cooling distribution systems. There are three types of valve
manhole drainage systems described in this manual: gravity drainage, pumped drainage from a sump basin,
and pumped drainage from the valve manhole.
(1) Gravity drainage. The most cost effective and lowest maintenance system is gravity drainage to
a storm drain when location, depth of existing storm drains, and local regulatory requirements allow this
possibility. Drainage lines will be 6 inches in diameter minimum and will conform to the latest storm drain
criteria and will be sloped at one percent, minimum. Valve manhole outlet will be a floor drain with backflow
preventer to prevent storm water inflow from the storm drain (see figure 3-22). Note that valve manhole drain
outlets shall be covered with a "hat type" cast iron pipe screen to minimize the accumulation of trash over the
drain inlet. Also, the manhole floor will be sloped toward the drain.
(2) Pumped drainage from sump basin. For pumped drainage, a duplex submersible pump system
installed in a remote sump basin may be provided as indicated in figures 3-23 and 3-24. The sump basin will
be located no more than 10 feet from the valve manhole. Drainage from the valve manhole to the sump basin
will be similar to drainage to a storm drain including the valve manhole floor drain (fig 3-22). Discharge from
the pumps can be routed to a splashblock at grade or to an adjacent storm sewer. Design of the surrounding
grade must ensure drainage away from the sump basin, valve manhole and concrete shallow trench (if used)
when discharging to grade. A power pedestal complete with failure warning light will be provided with each
basin as shown in figure 3-25. A typical wiring diagram and sequence of operation are shown in figure 3-26. A
specification for the sump basin system can be included in the applicable manhole or heat distribution section
of the contract specification. The sump basin design has proven to operate well even in the colder climates of
the upper tier states in the continental United States. It is also an excellent method to retrofit existing
manholes that currently do not drain properly. The remote sump basin increases the life of the systems by
removing the sump pump and pump controls from the hot, humid environment of the manhole. Also, pump
maintenance will be done outside of the manhole. The pumps are easily disconnected and lifted to grade.
The sump pumps used in the sump basin must incorporate the design characteristics listed in table 3-3.
(3) Pumped drainage from valve manhole. Another means to pump water from the manhole is to
locate the duplex sump pumps in the valve manhole. Typically, a 2'0" by 2'0" by 1'0" (deep) sump will be
provided in a corner of the valve manhole. The duplex sump pumps will be installed to pump
out of this sump. Valve manhole sump pump electrical arrangement should be installed as shown in figure
3-27. The control panel with high level warning light will be mounted adjacent to the valve manhole at grade.
This keeps the electrical panel out of the hot, humid environment of the manhole. The sequence of operation
and wiring diagrams will meet the requirements of figure 3-26. Pump discharge can be routed to a
splashblock at grade (similar to the sump basin discharge piping arrangement on figure 3-23) or to an adjacent
storm drain. Electric sump pumps used in the valve manholes must incorporate the design characteristics
listed in table 3-3. Note that life of the pumps are typically shortened when installed in the hot and humid
valve manhole environment.
e. General.
(1) Valve manhole wall penetrations. A design must be provided for the distribution system wall
3-5
CEMP-E
TI 810-32
10 January 2002
penetrations. For a shallow trench system, the wall penetrations will typically be the same size as the inside
dimension of the shallow trench connecting to the valve manhole. For shallow trench dimensions, refer to
chapter 4 of this manual. Structural reinforcement must be designed around this opening. Drainage from the
trench will then flow into the manhole. For Pre-engineered or Prefabricated Underground Heat Distribution
Systems, sleeved openings will typically be provided with an expandable seal between the casing and the pipe
sleeve as indicated on figure 3-28. Structural reinforcement must be designed to avoid contact with the pipe
sleeve and water stop to prevent grounding of the system's cathodic protection.
(2) Waterproofing. Waterproof membranes will be placed in or below the concrete bottom slab
and continued up the outer sides to the top of the sidewalls in accordance with the valve manhole guide
specification.
(3) Pipe anchoring adjacent to valve manholes. Regardless of the buried distribution system, pipe
anchors should be provided between 2 to 5 feet of a manhole wall to minimize movement through the
manhole. For piping which passes through valve manholes, anchoring on one side only is typically adequate.
Anchoring piping on more than one side may restrict piping movement and overstress the piping in the valve
manhole. Anchors will typically be provided as part of the distribution system and will not be embedded in
the manhole wall. However, if the manhole is used to support an anchor, the manhole must be designed to
withstand the forces exerted by the system. Expansion compensation stress calculation will always be
conducted to ensure proper anchor locations throughout the distribution system. These calculations must
also account for the expansion in the valve manholes.
(4) Piping materials in valve manholes. Nonmetallic piping must not be used in the same valve
manholes as piping carrying higher temperature media that could cause the temperature around the
non-metallic piping to exceed the allowables and potentially cause permanent damage to the non-metallic
piping. In addition, chilled water systems with PVC carrier piping must never be installed in the same valve
manhole with any heating system.
3-6
8-9
COOLING TANK: 18 INCHES LONG, 8"
DIA. SCHEDULE 80 PIPE WITH 8"
DIA. WELD CAPS
DIFFUSER: 10 INCHES OF 1/2 "
PIPE WITH MINIMUM OF 18 - 1/8 "
DIA. HOLES, CAPPED AT END
3/4 "
FROM STEAM
MAIN TRAP
VAULT WALL
6"
INSULATED NONMETALLIC PIPE (TYP)
18" MIN.
18" MIN. FROM FLR.
0 - 150 PSIG
GAGE WITH COCK
1" MIN. DIA.
UNION (TYP.)
GATE VALVE
(TYP.)
3/4 " DISCHARGE
ABOVE GRADE
NON-METALLIC TO
STEEL COUPLING
OR FLANGE
ADJUSTABLE ANGLE THERMOMETER WITH 30^F TO
300^ F RANGE AND A 3/4 " NPT BRASS WELL
1/2 " DRAIN
3/4 " TEMPERATURE
RELIEF VALVE SET TO
OPEN AT 250^
PUMPED INSULATED RETURN CONDENSATE
MAIN (SCH. 80 STEEL)
SYSTEM PRESSURE
MAXIMUM TRAP
(PSIG)
CAPACITY (LBS./HR.)
50
250
380
100
150
500
625
200
790
300
960
400
STEAM TRAP CAPACITY LIMITATIONS
CEMP-E
TI 810-32
10 January 2002
CONDENSATE COOLING SYSTEM
NO SCALE
Fig. 8-4
.
Condensate Cooling System for Non-metallic Pipe Detail.
CEMP-E
TI 810-32
10 January 2002
TYP.
1/4
1/2 " DIA. EXPANSION
ANCHOR BOLTS
7"
(TYP.)
16"
6"
12"
8"
2" X 3/8 " STEEL
BAR (TYP.)
3'-0" MAX.
NEW OR
EXISTING
WALL
3/4 " DIA. RUNG
(TYP.)
9" X 4" X 2"
WIDE X 1/2 "
THICK STEEL
BRACKET
(TYP.)
BOTTOM OF
VALVE
VAULT
3"
VALVE MANHOLE DEPTH VARIES
2"
TOP OF PIT
ACCESS LADDER
.
SCALE. 1 INCH = 1 FOOT
12"
6"
0
1'
Figure 3-2. Access Ladder Detail.
3-9
CEMP-E
TI 810-32
10 January 2002
INSULATING BOLT SLEEVE
1/16" MIN. WALL THICKNESS
STEEL WASHER
1/8 " THK. INSULATING GASKET
SET SIMILAR
FLANGE BOLT
NUT
PIPE
STEEL WASHER
FLANGES
ISOLATION FLANGE
NOTE:
NO SCALE
CONTRACTOR SHALL COMPLY WITH THE ISOLATION FLANGE MANUFACTURER'S
RECOMMENDATIONS FOR BOLT TORQUES AND BOLTING PATTERN. CONTRACTOR
SHALL ALSO RECHECK BOLT TORQUES 72 HOURS AFTER SYSTEM STARTUP.
Figure 3-3. Typical Isolation Flange Detail.
3-10
CEMP-E
TI 810-32
10 January 2002
DRILL THRU 13/16 " DIA. 4 PLACES,
FOR 3/4 " DIA. CONCRETE EXPANSION
ANCHORS, 8 1/2 " LONG WITH 2"
THREAD LENGTH
6 1/8 "
4 1/4 "
ANGLE
4" X 3" X 3/8 " X 4 1/2 "
3
1/4
3
PLATE 12" X 3/4 " X 1'-3 1/4 "
6 1/8 "
W6 X 20
1/4
1/4
SECTION
TYP.
1
NOTES:
1
5/8J"
W6 X 20
4'-0"
18" x 18" x 6"
CONCRETE PAD (TYP.)
6"
VARIES
1. PIPING SHALL REST ON THIS PIPE SUPPORT BY
MEANS OF A FREE PIPE SHOE (SUPPORT) AS
DETAILED IN FIG. 4-1. PIPE SHOES SHALL BE
CENTERED ON THE TOP BEAM OF THIS SUPPORT
IN THE COLD CONDITION.
3/4 " DIA. X 10" LONG
EXPANSION ANCHORS
(TYP.)
SLAB REINFORCEMENT
NOT SHOWN FOR
CLARITY
VALVE AND PIPE SUPPORT
SCALE.. 1 INCH= 1 FOOT
1'
12"
6"
0
Figure 3-4. Typical Valve/Piping Support Detail.
3-11
1
CEMP-E
TI 810-32
10 January 2002
L2
VERT. BARS
W2
W1
2'-4"
HORIZ. BARS
8" (typ.)
L1
PLAN IN SECTION
NO SCALE
L2
2" COVER
(TYP)
H1
(GRATE COVER SHOWN, FOR CONCRETE COVER SEE DETAIL A ON C-24)
VERT. BARS
HORIZ. BARS
4" CLEAR
(TYP)
TOP SECONDARY
REINFORCEMENT
TOP PRINCIPAL
REINFORCEMENT
#[email protected] VERTICAL BAR,
EMBED 24"(MIN.)
IN WALL
2" COVER
6"(TYP)
W.S.(TYP)
1'
W.S.
(TYP)
6"(TYP)
3" COVER(TYP)
BOTTOM PRINCIPAL REINFORCEMENT
BOTTOM SECONDARY REINFORCEMENT
*
VALVE MANHOLE SECTION*
NO SCALE
Figure 3-5. Valve Manhole Elevation and Section.
3-12
NOTE
SEE TABLE 3-2
FOR REINFORCEMENT
BAR SIZES.
CEMP-E
TI 810-32
10 January 2002
OUTSIDE PIT DIM. (LENGTH + 1")-(SEE
NOTE 1) FIG. 3-13
C 12X25
3"X2"X 5/16 "
A
Fig 3-7
3/8 " ALUMINUM PLATE
CONFORMING TO
ANSI H35.1
SLOPE
SLOPE
3"X2"X 5/16 "
(SEE NOTE 6
ON FIG. 3-16)
FLAT BAR 5/16 "LP X1"XLG
OF C12X25 (SEE NOTE 5
ON FIGURE 3-13
SUPPORT LP (TYP.)
5/16 " THICK ALUM.
HINGED CHECKER
TOP (TYP.)
2'-6"
OUT SIDE PIT DIM. (WIDTH + 1")-(SEE
NOTE 1) FIG. 3-13
HINGE (TYP.)
SLOPE
CORNERLP (TYP.)
B
Fig 3-8
HANDLE (TYP.)
SUPPORT LP (TYP.)
LADDER
C
Fig 3-9
RAISED COVER PLATE
NO SCALE
NOTE TO DESIGNER:
PLATE COVER SHOWN IS DESIGNED FOR LOADINGS UP TO 40 psf WHEN SPACING
BETWEEN SIDWALL AND CENTER SUPPORTS IS LESS THAN 3'6". LOADINGS OR
SPACINGS GREATER THAN THESE MUST BE DESIGNED FOR ON A CASE BY CASE BASIS.
Figure 3-6. Raised Cover Plate Design.
3-13
CEMP-E
TI 810-32
10 January 2002
6"
DETAIL - 1
(FIG. 3-10)
GRADE
CONC. PIT WALL
(TYP.)
SECTION A-A
NO SCALE
Figure 3-7. Section A-A of Raised Cover Plate.
3-14
CEMP-E
TI 810-32
10 January 2002
LIFTING LUG DETAIL (TYP.)
(SEE FIGURE 3-11)
1'-4"X6"X 5/16 " CORNER PLATE
(8 REQ'D PER ASSEMBLY)
1'-4"X6"X 5/16 " SUPPORT
PLATE (SEE NOTE 2 ON
FIGURE 3-13)
TYP.
ANGLE FRAME
5/16
TYP.4 PLACES
PER PLATE
1/4
TYP.
2
1/4
2
OUTSIDE CONCRETE VALVE
MANHOLE WALL (TYP.)
SECTION B-B
NO SCALE
Figure 3-8. Section B-B of Raised Cover Plate.
3-15
CEMP-E
TI 810-32
10 January 2002
SUPPORT LP
(SEE NOTE 2)
TYP.
HANDLE
ALUM. TOP
1/4
C12X25XLG. TO SUIT
(SEE NOTE 3)
I
` 3"X2"X 5/16 "
FRAME (TYP.)
1/2 " CLEARANCE
(SEE NOTE 1)
CONCRETE WALL
NOTE:
NOTES ARE LOCATED ON FIG. 3-13.
SECTION C-C
NO SCALE
Figure 3-9. Section C-C of Raised Cover Plate.
3-16
CEMP-E
TI 810-32
10 January 2002
3" S.S. HINGE, WELD TO CORNER
P
L 8, BOLT TO ALUM. TOP WITH
S.S. BOLTS, HEX NUTS AND
WASHERS TO SUIT.
TYP.
1/4
TYP.
1/4
CORNERLP
1/4
6
TYP.
NO. 2 MESH HARDWARE
CLOTH, TACK WELD TO
3"X2"X 5/16 " ANGLE FRAME
DETAIL - 1
NO SCALE
Figure 3-10. Detail of Raised Cover Plate.
3-17
CEMP-E
TI 810-32
10 January 2002
4"
2"
1
3/
4"
0 3/4 "R
6"
1 1/2 "
3/8 " THK. P
L
NOTE:
4 LUGS REQ'D PER ASSEMBLY
LIFTING LUG
NO SCALE
Figure 3-11. Lifting Lug Detail.
3-18
CEMP-E
TI 810-32
10 January 2002
4"
2 1/2 "
1 1/2 "
3/16 "
ALUMINUM L
P
9/16 " O DRILL HOLE FOR
1/2 "X1 1/2 " SQ. HD. BOLT,
HEX NUT 8 LOCK WASHER
(STAINLESS STEEL)-(TYP.)
NOTE: 2 HANDLES REQ'D, PER HINGED TOP,
MIN. 6 PER PIT COVER ASSEMBLY.
HANDLE
NO SCALE
Figure 3-12. Handle Detail.
3-19
1 1/2 "
CEMP-E
TI 810-32
10 January 2002
GENERAL NOTES: (FOR RAISED COVER PLATE)
1. FIELD VERIFY OUTSIDE DIMENSIONS OF NEW MANHOLE BEFORE CONSTRUCTING
MANHOLE COVER ASSEMBLY. ADD 1" TO OUTSIDE MANHOLE DIMENSIONS
(TO ALLOW FOR CLEARANCE) TO DETERMINE INSIDE ASSEMBLY DIMENSIONS.
2. EACH SUPPORT PLATE SHALL BE LOCATED HALFWAY BETWEEN CORNER
PLATES AT 3 SIDES OF MANHOLE. 2 SUPPORT PLATES SHALL BE LOCATED
BETWEEN 2 SPLIT ALUM. CHECKER TOP AT ONE SIDE OF MANHOLE.
3. SUPPORT CHANNELS SHALL BE C12X25XLG, TO EQUAL WIDTH OR LENGTH
DIM. PLUS 1" TO SUIT INSIDE ASSEMBLY DIM. THE CHANNEL SHALL REST
ON THE CONCRETE MANHOLE TOP AND THE ALUM. TOP SHALL REST ON THE
FLAT BAR PLATE.
4. CHANNEL SUPPORT, CORNER PLATES, SUPPORT PLATES, ANGLE FRAME
HARDWARE CLOTH, AND LIFTING LUGS SHALL BE HOT-DIPPED GALVANIZED
BEFORE INSTALLATION ON VALVE MANHOLES.
5. FLAT BAR 5/16 " THK. WELDED TO TOP OF C12X25 TO MAKE ALUM.
CHECKER TOP SLIGHTLY SLOPED AS INDICATED. LOCATE FLAT BAR
TO MATCH CHANNEL BEFORE WELDING.
6. ANGLE 3"X2"X 5/16 " WELDED TO C12X25 8 3"X 2"X5/16" AT EACH END
LENGTH SHALL EQUAL HALF OF LENGTH OR WIDTH OF VALVE MANHOLE.
Figure 3-13. Notes for Raised Cover Plates.
3-20
CEMP-E
TI 810-32
10 January 2002
SEE DETAIL
FIGURE 3-16
C
L VALVE MANHOLE
THIS SECTION OF
GRATING TO BE
INSTALLED OVER
MANHOLE ACCESS
LADDER
TO SUIT MANHOLE
1/8 "
GRATING
GRATING
MIN.
2'-6"
1/8 "
1/8 "
1/4 " SPACE
1/8 "
1/8 "
1/2 LENGTH OF PIT
SEE DETAIL
FIGURE 3-15
TYPICAL SUPPORTED COVER PLAN
(GRATE SUPPORT)
NO SCALE
NOTE TO DESIGNER:
GRATES IN FIGURES 3-14 THRU 3-16 ARE FOR LOADINGS UP TO 150 psf.
LOADINGS GREATER THAN THESE MUST BE DESIGNED FOR ON A CASE BY CASE BASIS.
Figure 3-14. Typical Supported Cover Plan (Grate Support).
3-21
CEMP-E
TI 810-32
10 January 2002
GRATING SHALL BE GALVANIZED AND CONFORM TO FEDERAL
SPECIFICATION RR-G-661. GRATING OVER MANHOLE,
EXCEPT LADDER ACCESS PORTION, TO BE W-19-4 (1x 3/16)
GRATING, CAPABLE OF A UNIFORM LOADING OF 145 psf
5/8 "X 5/16 " BAR ALL
AROUND WELD TO
ANGLE
EXIST. FIN.
GRADE
1/8 "
6"
MIN.
`1 3/4 x 1 3/4 x 1/4
1/2 " x 4" LOADED ANCHOR
STUD @ 2'-6" O.C.
ANGLE SUPPORT FOR GRATING
NO SCALE
Figure 3-15. Detail of Angle Support for Grating.
3-22
CEMP-E
TI 810-32
10 January 2002
GRATING, SEE DETAIL
FIGURE 3-17
EXIST. FIN.
GRADE
1/8 "
8"
1/2 WIDTH OF
PIT WALL
W 10X26 BEAM LOCATED
AT CL OF VALVE PIT,
SEE FIGURE 3-19 FOR
LOCATION REQUIREMENTS
1/2 " ANCHOR BOLTS
W/LOCK WASHER &
NUT (2 REQ'D)
STRUCTURAL SUPPORT FOR GRATING
NO SCALE
Figure 3-16. Detail of Structural Support for Grating.
3-23
CEMP-E
TI 810-32
10 January 2002
GRATING SUPPORT STEEL
L-LENGTH
(FT.)
W-WIDTH
(FT.)
VALVE
M.H.PLAN
REMARKS
A
4 OR LESS
AS REQ'D
NO MEMBER
REQ'D
B
GREATER
THAN 4 NOT
TO EXCEED 12
AS REQ'D NOT
TO EXCEED
12
ONE MEMBER
REQ'D
C
GREATER
THAN 12 NOT
TO EXCEED 16
GREATER
THAN 12 NOT
TO EXCEED 16
THREE
MEMBERS
REQ'D
NOTE: 1. FOR VALVE MANHOLE WITH DIMENSIONS L & W
GREATER THAN 16 FEET REQUIRES STEEL MEMBERS
AND GRATING TO BE DESIGNED FOR UNIFORM
LOADING OF 145 psf.
2. INTERSECTION OF STEEL MEMBERS MUST BE
DESIGNED FOR LOADING AND DIMENSIONS
INDICATED.
W
L
SEE NOTE 2
PLAN A
L
1/2 W
W10x26 TYP.
W
1/2 W
W
L
PLAN B
1/2 L
PLAN C
GRATING SUPPORT STEEL LOCATIONS
NO SCALE
Figure 3-17. Grating Support Steel Locations.
3-24
CEMP-E
NOTE:
TI 810-32
10 January 2002
PROVIDE A MINIMUM OF 4
CONNECTIONS PER PANEL.
CONNECTIONS SHALL BE 4 1/2 "
FROM EDGES OF PANELS AND
10" FROM ENDS OF PANELS.
3/8 " NUT-TACK WELD TO PLATE
1/8 " CHECKERED PLATE
2" SQ.X4" GALV. WASHER
GALV. STEEL GRATING
3/8 "0X1 1/2 " GALV. BOLT
CONNECTION FOR ATTACHING
CHECKERED PLATE TO GRATING
VARIES
VARIES
5/16 " ALUMINUM CHECKERED
PLATE IN CONFORMANCE
WITH ANSI H35.1.
PLATE WILL BE SAME
DIMENSION AS GRATING
SECTION IT COVERS
EXTEND ALUMINUM
CHECKERED PLATE
TO COVER BEAM
BLOCKOUTS
CHECKERED PLATES SHALL BE
PROVIDED WITH 12"X12"
VENTILATION OPENINGS AT
CORNERS (TYP.)
NOTE: SPACING BETWEEN PANELS AND BETWEEN
PANELS AND ANGLES SHALL BE 1/4 "
OPEN GRATE COVER W/CHECKER PLATE
CHECKER PLATE COVER DETAILS
NO SCALE
DESIGNER NOTE: CHECKERED PLATE TO BE USED TO COVER GRATING IN COLD CLIMATES
AND AREAS WHERE TRASH ACCUMULATION IS A CONCERN.
Figure 3-18. Detail of Checker Plate Cover.
3-25
CEMP-E
TI 810-32
10 January 2002
#[email protected] 9"O.C. EACH
WAY,TYP.
6" GOOSENECK
1'-2 1/2 "
IF CONCRETE TRENCH USED, THIS
PORTION OF CONCRETE MANHOLE LID'S
LIP TO BE DELETED TO ALLOW
TRENCH WALLS TO BUTT DIRECTLY
UP TO MANHOLE WALLS. TYPICAL OF
ALL MANHOLE TO TRENCH TRANSITIONS
C
(M
A
N
H
OL
E
C
O
VE
R)
F
4'(
A
C
C.
D
O
O
R)
1
A
(M
A
N
H IN
OLSI
E D
WE
ALFA
LSC
- E)
*
CONCRETE SHALLOW
TRENCH,(IF USED)
HINGES
(TYP.)
TWO
ADDITIONAL #5
EACH SIDE OF
OPENING
4'-0"X4'-0" ALUMINUM ACCESS
DOOR,"BILCO" MODEL JD-2AL
OR EQUAL W/SLIP RESISTANT
FINISH
LADDER
E
SECOND 6" GOOSENECK FOR
DIRECT BUIRIED SYSTEMS ONLY
B (MANHOLE WALLSINSIDE FACE)
1'-2 1/2 "
1'-2 1/2 "
4'(ACC. DOOR)
G
H
D (MANHOLE COVER)
(11'-0" max.)
CONCRETE COVER PLAN
NO SCALE
NOTE TO DESIGNER:
CONCRETE COVER DETAILED IS DESIGNED FOR LOADINGS UP TO 150 psf.
LOADINGS GREATER THAN THESE MUST BE DESIGNED FOR ON A CASE BY CASE BASIS.
Figure 3-19. Typical Concrete Cover Plan.
3-26
* SEE FIGURE 3-20
FOR SECTION
1
CEMP-E
TI 810-32
10 January 2002
DETAIL
A
FINISH GRADE
ELEVATION
PRECAST CONCRETE
MANHOLE COVER
6"
1 1/2 "
#[email protected] 9"
O.C.E.W.
MANHOLE WALL
DETAILS ON
SHEET C-21
SECTION 1
NO SCALE
NEOPRENE PAD
6"
10"
2"
2"
#5 BAR
CONTINUOUS
2"
1/2 "
6"
DETAIL
A
NO SCALE
CONCRETE COVER DETAILS
Figure 3-20. Concrete Cover Details.
3-27
CEMP-E
TI 810-32
10 January 2002
18"
WELD 6" PIPE
SECTIONS
45^
45^(TYP.)
24"
PAINTED 6"
SCHEDULE 40
STEEL PIPE
12"
VALVE
MANHOLE TOP
TYPICAL GOOSENECK DETAIL
.
SCALE. 1 INCH = 1 FOOT
12"
6"
0
1'
Figure 3-21. Gooseneck Detail.
3-28
CEMP-E
TI 810-32
10 January 2002
SLOPE VAULT FLOOR
TO FLOOR DRAIN
6" MIN.
RAISED "HAT TYPE"
PIPE SCREEN MOUNTED
TO FLOOR DRAIN
4" DRAIN PIPE DRAIN EXTENDED AT UNIFORM
SLOPE TO SUMP BASIN OR STORM DRAIN AS
INDICATED ON PLANS.
CAST IRON FLOOR DRAIN WITH
METALIC SPHERE OR FLAPPER
TYPE BACKWATER VALVE.
VALVE MANHOLE FLOOR DRAIN
NO SCALE
Figure 3-22. Valve Manhole Floor Drain Detail.
3-29
CEMP-E
TI 810-32
10 January 2002
CONCRETE SPLASHBLOCK TOP ELEVATION
MUST BE 6" BELOW SUMP
BASIN COVER & LOWER THAN
MANHOLE COVER
SEE FIGURE 3-24 FOR
SUMP BASIN COVER
DETAILS
ON-OFF FLOAT AND SWITCH (TYP.)
8"
ELECTRICAL BOX (SEE ELECT. DETAILS)
8"
2'-0"
8"
4" INLET
4" SANITARY TEE
2" GALVANIZED PUMP
DISCHARGE PIPE (TYP.)
6"
2'-6"
SUMP PUMP (TYP.)
SPLASHBLOCK TO BE INSTALLED
3" MIN. BELOW BASIN TOP
SECTION
1
45^ ELL W/
2 X 2 NIPPLE
TO DISCHARGE
ON SPLASHBLOCK
QUICK DISCONNECT
1
>
1
PIPE SLEEVE
ELECTRICAL BOXES-NEMA 4
ALARM FLOAT
36" REINFORCED CONCRETE PIPE
1/4 " FT. SLOPE
4"
4" SANITARY TEE
ON-OFF FLOAT AND SWITCH
4" GRAVITY INLET
6"
1 1/2 " - 2" INCREASER
14"
30 GPM, 25' HEAD PUMP (TYP.)
GROUT
6" 4"
OFF
NOTES:
SEE FIGURES 3-25 AND 3-26 FOR
SUMP BASIN ELECTRICAL DESIGN.
ELEVATION
SUMP BASIN WITH
DISCHARGE TO GRADE
.
SCALE. 1 INCH = 1 FOOT
12"
6"
0
1'
NOTE TO DESIGNER:
DEPTH DEPENDANT ON MAINTAINING 1/8 " / FT. SLOPE
FROM VAULT MANHOLE OUTLET TO THE SUMP BASIN.
DEPTH WILL BE A MINIMUM OF 4' OR A MINIMUM OF 1'
DEEPER THAN DESIGN FROST DEPTH, WHICHEVER
IS GREATER.
Figure 3-23. Remote Sump Basin.
3-30
AS REQUIRED *
2" SCHEDULE 40 GALVANIZED
PIPE W/COAL TAR COATING ON ALL
PIPES & FITTINGS BELOW GRADE
NON-SHRINKING
GROUT W/WATER STOP
CEMP-E
TI 810-32
10 January 2002
CHANNEL STRUT, SIMILAR OR
EQUAL TO "UNISTRUT" WELDED
TO BOTTOM EDGE OF
ANGLE FRAME
1/4 " X 3" X 3" STEEL ANGLE FRAME
CHANNEL STRUT
HANGER STRAP FOR MOUNTING
MISC. EQUIPMENT
CHANNEL STRUT
OPEN POSITION
OF COVER
AUTOMATIC HOLD
OPEN ARM
HANDLE
1/4 " STEEL
DIAMOND PLATE
COVER
1/4 " X 3" X 3"
STEEL ANGLE FRAME
REMOVABLE KEY
WRENCH
3"
STEEL STRAP
ANCHOR
HINGE
24" X 24"
3"
3"
CHANNEL
STRUT
27" X 24"
STANDARD LOCKING COVER
1/4 " STEEL
DIAMOND PLATE
COVER
1/4 " X 3" X 3"
STEEL ANGLE FRAME
HASP AND STAPLE
3"
STEEL STRAP
ANCHOR
HINGE
24" X 24"
3"
3"
CHANNEL
STRUT
27" X 24"
OPTIONAL LOCKING COVER
SUMP BASIN COVER
1
.
SCALE. 1 2 INCH = 1 FOOT
12"
9"
6"
3"
0
1'
Figure 3-24. Sump Basin Cover Details.
3-31
CEMP-E
TI 810-32
10 January 2002
NEMA 4 LOCKABLE
ENCLOSURE
M
M
ELECTRICAL SERVICE
(SEE NOTE 2)
CONCRETE PAD
2'-0"
PLAN
NO SCALE
SEE NOTE 1
RED LENS
SEE NOTE 4
ALTERNATOR
A
MOTOR STARTER MINIMUM
SIZE: NEMA 00
NEMA 4 LOCKABLE
ENCLOSURE
20 AMP 3
POLE CB
4' MIN.; 7' MAX.
6" THICK CONCRETE
PAD (SEE NOTE 3)
ELECTRICAL SERVICE
(SEE NOTE 2)
GRADE
LEVEL SWITCH (ALARM)
LEVEL SWITCH (ON)
LEVEL SWITCH (OFF)
M1
SCHEMATIC
NO SCALE
NOTES:
1.
2.
3.
4.
HIGH WATER LEVEL ALARM LIGHT. 120 VOLTS, 75 WATT SEALED BEAM LAMP, 60 FLASHES PER MINUTE.
FEDERAL SIGNAL MODEL 27-S OR APPROVED EQUAL. THE LENS SHALL BE RED.
ABOVE GROUND CONDUIT FEEDING ENCLOSURE AND ALL PENETRATIONS
OF CONCRETE PAD AND SUMP BASIN WALL WILL BE MADE OF RIGID STEEL.
CONCRETE PAD SHALL EXTEND BEYOND THE ENCLOSURE AT LEAST 6" ON ALL SIDES.
PROVIDE SIGN WITH 2" HIGH, 1/8 " STROKE, YELLOW LETTERS, STATING THE FOLLOWING; "THE CIRCUIT
BREAKER MUST BE LEFT IN THE ON POSITION. THIS CIRCUIT PROVIDES POWER TO THE SUMP PUMPS ON THE
UNDERGROUND HEAT DISTRIBUTION SYSTEM. FAILURE TO KEEP THIS CIRCUIT ON WILL CAUSE EXTENSIVE
AND COSTLY DAMAGE TO THE UNDERGROUND HEAT (STEAM) DISTRIBUTION SYSTEM."
Figure 3-25. Sump Basin Electrical Details.
3-32
M2
SUMP BASIN
CEMP-E
TI 810-32
10 January 2002
"POWER ON" LIGHT MOUNTED
ON SIDE OF ENCLOSURE
480 VOLT TO
120 VOLT *
LEVEL SW.
(ALARM)
R
R
SIZE AS
REQUIRED
TO ALTERNATOR
LEVEL SW.
(OFF)
LEVEL SW.
(ON)
P1
OL
OL
OL
OL
OL
OL
A
P2
P1
P2
P1
P2
OL
OL
M1
OL
3/4 HP
OL
M2
3/4 HP
SEQUENCE OF OPERATION:
THE ALTERNATOR SHALL OPERATE A PUMP UPON WATER LEVEL REACHING LEVEL SWITCH ON AND
DEENERGIZE IT WHEN THE WATER LEVEL FALLS BELOW LEVEL SWITCH OFF. IT SHALL ALTERNATE
PUMPS ON EACH SUCCESSIVE CLOSING OF LEVEL SWITCH ON. IF THE WATER CONTINUES TO RISE
PAST THE ALARM LEVEL, THE RED LIGHT SHALL BE ENERGIZED AND THE LAG (SECOND) PUMP
SHALL BE ENERGIZED.
SUMP PUMP CONTROL-3 LINE DIAGRAM
NO SCALE
NOTE TO THE DESIGNER:
ACTUAL SYSTEM VOLTAGE AND HORSE POWER REQUIREMENTS
MUST BE VERIFIED AND DETAILED FOR EACH DESIGN
Figure 3-26. Sump Pump Wiring Diagram.
3-33
CEMP-E
TI 810-32
10 January 2002
NEMA 4 LOCKABLE
ENCLOSURE
M-1
M-2
SUMP PIT
(2'x2'x1' (deep)
MINIMUM)
ELECTRICAL SERVICE
(SEE NOTE 2)
CONCRETE PAD
2'-0"
PLAN
VALVE
MANHOLE
NO SCALE
SEE NOTE 1
RED LENS
SEE NOTE 4
ALTERNATOR
A
MOTOR STARTER MINIMUM
SIZE: NEMA 00
20 AMP 3
POLE CB
NEMA 4 LOCKABLE
ENCLOSURE
4' MIN.; 7' MAX.
6" THICK CONCRETE
PAD (SEE NOTE 3)
ELECTRICAL SERVICE
(SEE NOTE 2)
GRADE
ROUTE 2" DISCHARGE PIPE AS
DETAILED FOR SUMP BASIN
SYSTEM (FIGURE 3-23)
LEVEL SWITCH (ALARM)
LEVEL SWITCH (ON)
VALVE
MANHOLE
LEVEL SWITCH (OFF)
M1
M2
SCHEMATIC
NO SCALE
NOTES:
1.
HIGH WATER LEVEL ALARM LIGHT. 120 VOLTS, 75 WATT SEALED BEAM LAMP, 60 FLASHES PER MINUTE.
FEDERAL SIGNAL MODEL 27-S OR APPROVED EQUAL. THE LENS SHALL BE RED.
2.
ABOVE GROUND CONDUIT FEEDING ENCLOSURE AND ALL PENETRATIONS
OF CONCRETE PAD AND VALVE MANHOLE WALL WILL BE MADE OF RIGID STEEL.
3.
CONCRETE PAD SHALL EXTEND BEYOND THE ENCLOSURE AT LEAST 6" ON ALL SIDES.
4.
PROVIDE SIGN WITH 2" HIGH, 1/8 " STROKE, YELLOW LETTERS, STATING THE FOLLOWING; "THE CIRCUIT
BREAKER MUST BE LEFT IN THE ON POSITION. THIS CIRCUIT PROVIDES POWER TO THE SUMP PUMPS ON THE
UNDERGROUND HEAT DISTRIBUTION SYSTEM. FAILURE TO KEEP THIS CIRCUIT ON WILL CAUSE EXTENSIVE
AND COSTLY DAMAGE TO THE UNDERGROUND HEAT (STEAM) DISTRIBUTION SYSTEM."
VALVE MANHOLE SUMP ELECTRICAL DETAILS
Figure 3-27. Valve Manhole Sump Pump Electrical Details.
3-34
CEMP-E
TI 810-32
10 January 2002
EXTEND 1" PIPE 12" ABOVE
TOP OF MANHOLE (OR NEAR
TOP OF SUPPORTED COVER OR
RAISED SOLID PLATE COVER
MANHOLES)
1/4"
CONDUIT SEAL
(SIMILAR OR EQUAL TO
LINK-SEAL MODEL - LS)
3"
WATER STOP
WELDED TO
SLEEVE
PIPE SLEEVE
SEE NOTE 1
6"
CASING OF EXISTING
DDT PRE-ENGINEERED
UNDERGROUND HEAT
DISTRIBUTION SYSTEM
INSULATION ON
CARRIER PIPE
1" THREADED BRASS CAP
OR PLUG
SEE NOTE 2
INSIDE WALL OF MANHOLE
NOTES:
1. END SEAL OR GLAND SEAL SHALL BE PROVIDED
ON ALL DDT PRE-ENGINEERED BURY SYSTEMS
INSIDE MANHOLE WALLS. CASING AIR SPACE
SHALL BE PROVIDED WITH DRAIN PLUG AND VENT.
VENT SHALL HAVE 1 " PIPE ROUTED AS INDICATED.
2. INSIDE DIAMETER (ID) OF SLEEVE SHALL BE DETERMINED
AFTER CASING OUTSIDE DIAMETER (OD) HAS BEEN
VERIFIED. GENERALLY, SLEEVE (ID) SHALL BE 5" MORE
THAN CASING OD. VERIFY WITH SEAL MANUFACTURER.
CASING WALL PENETRATION
NO SCALE
Figure 3-28. Casing Wall Penetration Detail.
3-35
CEMP-E
TI 810-32
10 January 2002
Table 3-1. Valve Manhole Clearances.
RECOMMENDED INTERNAL CLEARANCES
MINIMUM
DISTANCE
(INCHES)
FROM
TO
O.D. OF
PIPE
INSULATION
OR
CONDUIT
END OF
VALVE
STEM OR
BODY
BOTTOM
ELEC. LADDER OF TRAP
STATION
EQUIP.
OR DRAIN
WALL
18"
18"
-
6"
18"
FLOOR
24"
24"
36"
12"
12"
TOP OF
MANHOLE
18"
12"
6"
6"
36"
NOTES:
1. IN ADDITION TO THE CLEARANCES FOR THE LADDER
INDICATED PROVIDE 24" AROUND THE LADDER
FOR MAINTENANCE ACCESS.
2. PROVIDE 24" AROUND SIDES OF MANHOLE DRAIN TO
ALLOW FOR CLEANING OF DEBRIS.
VALVE MANHOLE CLEARANCES
3-37
CEMP-E
TI 810-32
10 January 2002
Table 3-2. Reinforcing Steel Sizes.
VALVE MANHOLE REINFORCEMENT SCHEDULE
MAXIMUM DIMENSION*
WALL REINFORCEMENT
OUTSIDE
L1XW1
INSIDE
L2XW2
HORIZONTAL
9'4"X9'4"
8'0"X8'0"
#[email protected]"
15'4"X15'4"
14'0"X14'0"
#[email protected]"
SLAB REINFORCEMENT
TOP
BOTTOM
SECONDARY SECONDARY
BOTTOM
PRINCIPAL
TOP**
PRINCIPAL
#[email protected]"
#[email protected]"
#[email protected]"
#[email protected]"
#[email protected]"
#[email protected]"
#[email protected]"
#[email protected]"
#[email protected]"
#[email protected]"
VERTICAL
NOTES TO THE DESIGNER:
* L1,L2,W1, AND W2 DIMENSIONS FROM FIGURE 3-5. MAXIMUM DEPTH (H1) FOR THIS TABLE IS 8'0"
** PRINCIPAL REINFORCEMENT WILL SPAN THE SHORTER DIMENSION
REINFORCED CONCRETE DESIGN IS BASED ON THE FOLLOWING:
1. LOADS : 200 psf SURCHARGE ADJACENT TO VAULT.
2. SOIL PROPERTIES = MOIST = 120 pcf WATER TABLE 2' BELOW SURFACE
SATURATED = 125 pcf BEARING CAP. = 1500 psf. MIN.
Ko = .80
VALVE MANHOLE REIN. STEEL SIZES
3-38
CEMP-E
TI 810-32
10 January 2002
Table 3-3. Sump Pump Checklist.
SUMP PUMP CHECKLIST
ITEM
PUMPS' DESCRIPTION
1.
ELECTRICALLY DRIVEN.
2.
DUPLEX SYSTEM WITH ALTERNATOR.
3.
DEDICATED ELECTRICAL SERVICE.
4.
SUBMERGED OPERATION IN 200^F WATER.
5.
ENTIRE PUMPING SYSTEM CAPABLE OF
200,000 CYCLES OF OPERATION IN
200^F, 100% RELATIVE HUMIDITY ENVIR.
6.
PERMANANTLY LUBRICATED BEARINGS.
7.
BRONZE IMPELLER.
8.
MONEL SHAFT.
9.
CAPABLE OF PASSING 3/8 INCH SPHERES.
10.
SCREENED INLET.
11.
BRONZE HOUSING.
3-39
CEMP-E
TI 810-32
10 January 2002
CHAPTER 4
HEAT DISTRIBUTION SYSTEMS IN CONCRETE TRENCHES
4-1. GENERAL. The concrete shallow trench (CST) is a system, which allows insulated carrier pipes to
be routed underground but yet not have the piping in contact with the soil. The system also provides
comparatively easy access for maintenance and repair by means of removable concrete tops. These
exposed tops can be used as sidewalks since the system is installed at grade.
4-2. SYSTEM DESIGN. The designer is responsible for conducting a site investigation, designing the
distribution system plan and profiles, and designing the valve manholes, as described in chapter 3 of this
manual. In addition, the designer will use details and descriptions presented here to design a concrete
shallow trench system at a particular site.
a. Trench Systems - General.
(1) Piping and fittings. All carrier piping and pipe fittings will be carbon steel and will be designed
to satisfy the temperature and pressure requirements of the system. Materials will conform
to the
requirements in the guide specification.
(2) Pipe supports. Pipe supports will typically consist of three types: free, guided, and anchor.
These supports are detailed in figure 4-1, figure 4-2, and figure 4-3. All of these pipe supports will be
mounted on channel supports mounted to the trench walls as detailed in figure 4-4. Supports may be
mounted by other means, such as on concrete pedestals, provided that paths for water flow are
maintained. Table 4-1 provides guidance for the sizing of the channel supports. Note that the channels
for anchor supports in the table are designed for more substantial loads than required for free and guided
supports. The anchor support channel in this table is adequate for approximately 1,000 pounds force
axially. The designer will determine axial force requirements at all anchor points and design the channels
to accommodate these forces. \1\ Maximum distance between support channels shall be as listed in
table 4-2. /1/ These spacings are applicable to long, straight runs of piping only and must be reduced at
elbows, vertical risers, valving, and equipment. The actual spacings, in these instances, will be
determined by analyzing the pipe stresses with the pipe stress analysis, as described in chapter 3 of this
manual. The designer should note that there are other types of supports (such as roller type) that may
also be used. However, all supports must be capable of withstanding the thermal stresses and forces
exerted on them.
(3) Clearances. Clearances in the trench will be adequate to provide room for expansion,
movement, and a sufficient amount of access for cleaning and maintenance. There must also be
minimum of 4 inches clearance under the support channels to ensure ground water drainage along
trench floor. Figure 4-5 provides a trench cross-section, which corresponds to the table 4-3 trench
dimension schedule, which must be filled in by the designer.
air
a
the
(4) Insulation and jacketing. Insulation will be selected in accordance with insulation thickness
tables in the guide specification. These insulation thicknesses were developed using a life cycle cost
analysis. All insulations used have passed the Federal Agency Committee's boiling test
and are listed
in the guide specifications. All insulation in the trench will be covered with jacketing material in
conformance to the guide specification.
b. Trench System - Structural. The concrete trench will be field constructed of reinforced concrete
conforming to the current criteria. Trench walls and floors will be poured in place-they will not be precast.
Trench tops will be poured in place or precast. Walls, floors, and tops will be constructed with 4,000 psi
minimum compressive strength concrete. Reinforcing bars will conform to ASTM A 615, grade 60. Wall,
4-1
CEMP-E
TI 810-32
10 January 2002
floor, and top thicknesses shall be 6 inches, minimum. However, thicker sections may be required to
accommodate site specific loadings or to prevent flotation. Concrete trench floors shall be sloped at a 1
inch in 20 feet slope toward all low points to ensure proper drainage. Doweled or keyed joints and water
stops shall be provided at all construction joints and shall be detailed as shown in figure 4-6. Trench
reinforcing details will be provided and will be similar to the section shown in figure 4-7. Note that actual
concrete thicknesses and reinforcing bar sizes will be verified by the designer for each project. Trench
corners will be constructed as detailed in figure 4-8. Trench tops will be no longer than eight feet to allow
easy removal and placement.
c. Trench Top Removal Devices. The most common type of removal devices for the trench tops
will be the sling type as detailed in figure 4-9. Four lifting devices are required to lift a trench top. One set
of lifting devices will accommodate all trench tops for each contract. In some instances, sling type lifting
devices will not be convenient to use (eg. when the trench top butts up against a parallel sidewalk or when
the trench is routed through a parking area). In these instances, the designer shall require coil inserts to
be cast into the trench cover in four locations that will accommodate threaded lifting eye bolts. When not
being used, threaded plugs are inserted into the coil inserts. The lifting devices are also detailed in figure
4-9.
d. Road and Parking Lot Crossings. Road crossing requirements will be designed on a case by
case basis and must take into account pavement materials, soils, and frost characteristics of the design
site. A typical road crossing is shown in figure 4-10. Figure 4-11 details a concrete trench to curb and
gutter system transition and figure 4-12 details a concrete trench to drain pan system transition. In all
instances, the crown of the road crossing will be matched and the thickness of the trench top will be
designed to accommodate worst case loadings. Parking lot crossings typically will have the trench top
exposed at grade as shown in figure 4-13. Exposed tops allow for easier trench top removal over
extended lengths of paved areas. If appearance of the crossing is critical, black pigments may be added
to the concrete tops at the road crossing to match the surrounding pavement. In rare instances, the
trench tops may be covered with asphalt surfacing, as detailed in figure 4-14.
e. Sidewalk Intersections. In the event the trench system intersects an existing sidewalk, the
trench system will match the sidewalk as detailed in figure 4-15.
f. Expansion Compensation. Expansion loop and bend design is the responsibility of the designer,
and is covered in chapter 3 of this manual. The expansion loop design is critical. Sufficient space needs
to be provided in the expansion loop area to ensure that no pipe or insulation interference will occur due to
pipe movement as shown in figure 4-16. This detail indicates location of supports and also shows how the
piping system will be offset to allow for expansion movement in the trench. Table 4-4 is a typical loop
schedule, which corresponds to figure 4-16. The locations of the supports in the expansion loops will be
determined from the designer's piping stress analysis and then entered in Table 4-4. All piping stresses
will be less than ASME B31.1 allowables for each application. The designer will require inspection ports
be provided in the trench tops at each bend in the trench system routing for the purpose of observing pipe
movement at the bends during system startup. The inspection port is similar to the access cover detailed
in figure 4-18, except the nominal diameter of the lid will be 12 inches.
g. Sealants. The trench will be sealed to minimize the influx of ground water. A 1/4 inch thick
neoprene pad will be used between trench tops and tops of trench walls. The pad will have a minimum width
of 2 inches. All trench joints must be sealed with elastomeric sealants, which are available as a one or two
component system. Asphaltic sealants have not performed as reliably for this application. The elastomeric
sealant should be able to resist 50 percent total joint movement. The nonsagging type must be used for
vertical joints. The self-leveling type must be used for trench top butt joints as shown in figure 4-17. Other
horizontal joints may be sealed with either type of elastomeric sealant, but the sealant used in trench
bottoms must finish flush with the floor.
4-2
CEMP-E
TI 810-32
10 January 2002
h. Vents and drains. Piping vents and drains will be located at all high and low points, respectively
\1\ (see figure 4-19) /1/. Piping drains will be provided in valve manholes only where access can be achieved
and where system drainage is provided. Piping vents may be located anywhere in the trench piping system
with an access cover provided in the trench top, as detailed in figure 4-18 or with an aluminum access door
shown in figure 3-19.
4-3. GENERAL CONSIDERATIONS. The designer will address these key areas to ensure a satisfactory
shallow trench design.
a. The grading design will ensure ground water will not pond or sit over the trench. The trench will
not be routed through existing flood plains, swales, or in areas where seasonal water accumulates. Another
distribution system, preferably an Aboveground Heat Distribution System (chap 7), should be used in these
areas. In areas where seasonal ground water will cause a trench flotation problem, the design will include a
subdrainage system along the trench if thickening of system walls and floor slabs to offset the buoyancy
effect is not practical.
b. The trench floors will slope a minimum of 1 inch in 20 feet toward valve manholes and the piping
will parallel the trench floor. This will allow the trench to drain off all water that may enter. Drainage will
then be provided from the valve manholes as described in chapter 3 of this manual.
c. Valve manholes should be spaced to minimize the depth of the trench system. Additional
manholes may be less expensive than excessive trench depths to accommodate the slope while still
keeping the trench tops at grade.
4-3
CEMP-E
TI 810-32
10 January 2002
PIPE
PIPE
INSULATION
INSULATION
SEE NOTE 2
SEE NOTE 2
TYP.
1/4
SEE NOTE 3
*
*
1 1/2 "
1 1/2 "
*
SEE NOTE 1
S-1
PIPE 2" THRU 10"
8"
S-2
PIPE 12" THRU 24"
HEAT INSULATED PIPING
(100^F - 750^F)
SHOES FOR CARBON STEEL PIPE
MATERIAL
TYPE
STEEL ASTM
SIZE
S-1
S-2
CARBON A-36
CARBON A-36
ST 6 X 15.9 X 16" LONG
1 PLATE
8" X 16" X 1/4 " THK. (HORIZ.)
2 PLATES
6" X 16" X 1/4 " THK. (VERT.)
NOTES:
1. WELD THICKNESS SHALL BE SAME AS PIPE SHOE OR PIPE WALL
THICKNESS, WHICHEVER IS THINNEST.
2. WHERE INSULATION IS GREATER THAN SHOE HEIGHT, CUT AWAY
INSULATION PARTIALLY WHERE IT INTERFERES WITH PIPE
SHOES AND SUPPORTS.
3. SEE TABLE 4-1 FOR CHANNEL SUPPORT SCHEDULE.
FREE PIPE SUPPORT
NO SCALE
Figure 4-1. Free Pipe Support Detail.
4-4
FS
CEMP-E
TI 810-32
10 January 2002
PIPE
PIPE
INSULATION
INSULATION
S-2
S-1
TYP.
SEE NOTE 1
G-4
SEE NOTE 1
3/161 1/2 "-3
TYP.
G-5
SUPPORT CHANNEL
IN TRENCH (TYP.)
(SEE NOTE 2)
GUIDE ANGLE
(TYP.)
3/161 1/2 "-3
1/4 " CLR.
(TYP.)
GUIDE ANGLE
(TYP.)
1/4 " CLR.
(TYP.)
PIPE 2"THRU 10"
PIPE 12"THRU 24"
HEAT INSULATED PIPING
GUIDES FOR PIPE SHOE
MATERIAL
TYPE
STEEL ASTM
SIZE
G-4
CARBON A-36
1" X 1" X 3/16 "
ANGLE 16" LONG
G-5
CARBON A-36
1" X 1" X 3/16 "
ANGLE 16" LONG
NOTE:
1. FOR PIPE SHOES S-1 AND S-2,
SEE DETAILS FOR ,(Fig. 4-1)
2. SEE TABLE 4-1 FOR CHANNEL SUPPORT SCHEDULE.
GUIDED PIPE SUPPORT
NO SCALE
Fig. 4-2. Guided Pipe Support Detail.
4-4
CEMP-E
TI 810-32
10 January 2002
PIPE
INSULATION
PIPE
S-1
SEE NOTE 1
TYP.
TYP.
1/4
INSULATION
1/4
S-2
SEE NOTE 1
SUPPORT CHANNEL
IN TRENCH (TYP.)
(SEE NOTE 2)
PIPE 12" THRU 24"
PIPE 2" THRU 10"
NOTE:
1. FOR PIPE SHOES S-1 AND S-2
SEE DETAILS ON FIGURE 4-1.
2. SEE TABLE 4-1 FOR CHANNEL SUPPORT SCHEDULE.
ANCHOR PIPE SUPPORT
NO SCALE
AS
Figure 4-3. Pipe Anchor Detail.
4-6
CEMP-E
TI 810-332
10 January 2002
1/2 OF INSIDE
TRENCH WIDTH
SUPPORT CHANNEL
>
SYMMETRICAL ABOUT >
6"
1
2
VARIES
NOTE:
SEE FIGURE 4-5 FOR SECTION
1
COMPOSITE PLAN - TRENCH
NO SCALE
SEE DETAIL
1/2" P L
EMBEDDED IN
TRENCH WALL
C
CHANNEL
6"
BACKFILL
MATERIAL
VARIES
SECTION
2
NO SCALE
3/16
NOTE: THE CHANNEL SUPPORT MAY LAY ON TOP
OF THE ANGLE RATHER THAN BEING SUSPENDED
BELOW THE ANGLE AND HELD ON BY BOLTS AS
SHOWN. PLACING THE CHANNEL ON TOP WOULD
ALLOW THE ANGLE TO SUPPORT THE CHANNEL
AND THE BOLTS WOULD HOLD THE CHANNEL IN
POSITION
ANGLE
CHANNEL
SUPPORT
TWO A307
BOLTS
PLATE W/WELDED ANCHOR
STUDS (SEE TABLE 4-1 FOR
NUMBERS AND SIZES)
DETAIL
C
NO SCALE
PIPE SUPPORT CHANNEL
Figure 4-4. Pipe Support Channel.
4-7
TI 810-332
30 August 1999
5 1/4 "**
CEMP-E
6"
PIPE SUPPORT
(TYP.)
* 4" CLEARANCE PROVIDED FOR
PROPER DRAINAGE OF TRENCH
SYSTEM.
** CONCRETE TOP THICKNESS MAY
BE INCREASED, AS NECESSARY,
TO ACCOMMODATE ANTICIPATED
LLOADINGS.
4"
*
8"
MIN.
SEE FIG. 4-4,
DETAIL C
MIN.
D1/2 + 8"
D1/2 F
3/4 "
HW + 12" *
1 1/2 " (TYP.)
RETURN
SUPPLY
C
E
D1
B1
A
6"
SUPPORT
CHANNEL
C
D2
B2
W
6"
NOTES:
1. DIMENSION "HW" SHALL BE INCREASED AS
NECESSARY TO ACCOMADATE THE MINIMUM
TRENCH BOTTOM SLOPE OF 1" PER 20 FEET.
2. SEE TABLE 4-3 FOR TRENCH DIMENSION SCHEDULE.
TYPICAL TRENCH & COVER DIMENSIONS
SECTION 1 FROM FIGURE 4-4
NO SCALE
Figure 4-5. Trench Dimension Section.
4-8
CEMP-E
TI 810-32
10 January 2002
FORMED OR SAWCUT
SEALANT RESERVOIR
SLAB STEEL STOP
2" FROM JOINT
(TYP.)
SHEET STEEL FORM
AS PER SPECS.
T/2
T
SMOOTH DOWELS- 3/4/ "o X 16"
LONG @ 12" O.C. PAINTED
& OILED PER SPECS.
(RETAINED IN PLACE
SHEET STEEL FORM)
KEYED
DOWELED
CONSTRUCTION JOINT
NO SCALE
Figure. 4-6. Construction Joint Detail
4-9
CEMP-E
TI 810-32
10 January 2002
BROOM FINISH
W.W.F. 6X6-W1.4XW1.4
STD. SIDEWALK
EDGE
1" CLEAR
#4 [email protected]
8" O.C.
#4 [email protected]
16" O.C.
1" CLEAR
#4 [email protected]
12" O.C.
1/4 " NEOOPRENE
PAD (TYP.)
6" TYP. MIN.
#5 [email protected]
12" O.C.
2 1/2 " CLEAR
2 1/2 " CLEAR
*
SEE TABLE 4-3 FOR TRENCH
DIMENSION SCHEDULE.
TRENCH & COVER REINFORCING
NO SCALE
NOTE TO THE DESIGNER:
TRENCH REINFORCEMENT AND CONCRETE THICKNESS SHALL
DE DETERMINED BY A STRUCTURAL ENGINEER BASED ON SITE
SPECIFIC LOADS AND SOIL PROPERTIES. REINFORCEMENT
SHOWN IS THE MINIMUM REQUIRED.
Figure 4-7. Typical Trench Section.
4-10
CEMP-E
TI 810-32
10 January 2002
#[email protected]" O.C.
HORIZ. WALL
REINFORCEMENT
#4 CORNER BAR
@ 12" O.C.
24"
24"
TYPICAL TRENCH WALL
CORNER REINFORCING
NO SCALE
Figure 4-8. Trench Corner Detail.
4-11
CEMP-E
TI 810-32
10 January 2002
STEEL LIFTING DEVICE W/ SLING BY
CONTRACTOR. DELIVER 1 SET OF 4 TO
GOVERNMENT AT END OF CONTRACT.
JOINT SEALANT
TRENCH COVER
(TYP.)
TOP SLAB JOINT
8"
8"
h*
TRENCH COVER
(TYP.)
TRENCH WALL
1'-0"
1'-0"
LIFTING SLOT 4" DEEP
TYPICAL AT 4 CORNERS
* DESIGN HEIGHT "h" OF SLOT TO
ACCOMMODATE SUBMITTED LIFTING DEVICE.
LIFTING SLOT (TYP.)
SECTION
SIDE VIEW
NOTES:
1. DESIGN OF LIFTING DEVICE SHALL SATISFY ACI
REQUIREMENTS ALONG LIFTING SLOTS.
SHEAR
2. CONTRACTOR SHALL DISTRIBUTE LOAD EQUALLY BETWEEN THE FOUR
LIFTING DEVICES BY USING A STRONGBACK OR APPROVED EQUAL.
SLING LIFTING DEVICE
NO SCALE
HEAVILY GREASED SETTING PLUG
(MANUFACTURED BY DAYTON-SUPERIOR
TYPE T-7 OR APPROVED EQUAL)
SETTING PLUG SHALL REMAIN INSERTED
UNTIL REMOVED BY THE OWNER. IF THE
USE OF THE COIL INSERTS IS REQ'D FOR
COVER INSTALLATION, THE CONTRACTOR
SHALL RE-GREASE SETTING PLUG AND
INSERT INTO COIL INSERT AFTER COVER
INSTALLATION IS COMPLETE. INSTALL
4 INSERTS PER COVER EACH 12" FROM
THE TRENCH TOP SIDE AND 12" FROM
TRENCH TOP END.
3 5/16 " MIN
3/4 "o X 6" LENGTH COIL INSERT FOR
8" COVERS OR 3/4 "o X 4" LENGTH
COIL INSERT FOR 6" COVERS AS
MANUFACTURED BY DAYTON-SUPERIOR
TYPE B-17 OR APPROVED EQUAL. MIN.
TENSILE CAPACITY SHALL BE 4500 lbs.
SECTION
NO SCALE
NOTE:
PROVIDE 1 SET OF 4 OF EACH
EYE BOLT TYPE TO GOVERNMENT
AT END OF CONTRACT.
3"
"
3/4
NOTE:
DETAIL APPLIES FOR TRENCH COVERS AT ALL ROAD
CROSSINGS, AND AT ALL PARKING LOT CROSSINGS.
DETAIL ALSO APPLIES TO ALL TRENCH COVERS
THAT BUTT UP TO BACK OF CURBS, AND ANY
OTHER AREAS THAT WOULD RESTRICT THE USE
OF THE STANDARD LIFTING DEVICES. LIFTING SLOTS
SHALL BE PROVIDED IN ALL TRENCH COVERS
REGARDLESS OF WHETHER COIL INSERTS ARE USED
OR NOT.
MINIMUM EYE BOLT REQUIREMENTS
NO SCALE
EYE BOLT LIFTING DEVICE
NO SCALE
FIGURE 4-9. TYPICAL LIFTING DEVICES.
4-12
CEMP-E
TI 810-32
10 January 2001
CENTERLINE
OF ROAD
>
3
A
SEE DETAIL
SEE DETAIL
>
FIGURE 4-12
B
FIGURE 4-11
3" MIN.
SECTION
3
NO SCALE
TRENCH ROAD CROSSING
NO SCALE
Fig. 4-10. Typical Trench Road Crossing.
CENTERLINE
OF ROAD
C
L
3
A
SEE DETAIL
SEE DETAIL
C
L
FIGURE 4-11
FIGURE 4-12
3" MIN.
SECTION
3
NO SCALE
TRENCH ROAD CROSSING
NO SCALE
Fig. 4-10. Typical Trench Road Crossing.
4-13
B
CEMP-E
TI 810-32
10 January 2002
SEALENT WITH BACKING ROD
MATCH CURB
1/2 "
1 1/2 "
8" MIN.
6" MIN.
6" MIN.
1" MIN.
@ ROADS
VARY FROM 90^ IF JOINT
OPENING WILL EXCEED 1/2 "
4
DETAIL
B
NO SCALE
STD TRENCH COVER
2'
SYMMETRICAL
ABOUT
>
TRENCH COVER
6"
CURB&GUTTER
UNIT BEYOND
1/2 "
1/2 " R
8" MIN.
BITUMINOUS
PAVEMENT
1"
3/4 " R
1"
8"
1'
1/2 " SEAL
EXPANSION
JOINT
5 11/16 "
PROVIDE EXPANSION
MATERIAL BETWEEN
TRENCH CURB AND
EXISTING CURB
SEE TRENCH COVER
REINFORCEMENT
#[email protected] EVEN SPACES, WIDTH
OF TRENCH COVER
#[email protected] 6" O.C.
SECTION
TYPICAL CURB & GUTTER
REINFORCING DETAIL
4
NO SCALE
NO SCALE
TRENCH CROSSING WITH CURB AND GUTTER
NO SCALE
NOTE TO THE DESIGNER:
TRENCH CONCRETE THICKNESSES AND REINFORCEMENT SHOWN MUST BE VERIFIED FOR
EACH DESIGN BY THE DESIGNER.
Fig. 4-11. Trench Crossing with Curb and Gutter.
4-14
CEMP-E
TI 810-32
10 January 2002
MATCH EXISTING
DRAIN PAN
8"MIN
1"MIN
6"MIN
1"MIN @ ROADS
DETAIL A
NO SCALE
STD TRENCH COVER
3'-0"
1'-6"
1'-6"
SEE TRENCH
COVER REINF.
1"MIN
7"
#[email protected] 6" O.C.
DRAIN PAN REINF.
#[email protected] EVEN SPACES
WIDTH OF TRENCH
COVER
NO SCALE
TRENCH CROSSING WITH DRAIN PAN
NOTE TO THE DESIGNER:
TRENCH CONCRETE THICKNESSES AND REINFORCEMENT SHOWN
MUST BE VERIFIED FOR EACH DESIGN BY THE DESIGNER.
Fig. 4-12. Trench Crossing With Drain Pan.
4-15
CEMP-E
TI 810-32
10 January 2002
SAW CUT
(TYPICAL)
BACKFILL
2"
(TYP.)
TACK COAT
EXISTING
GRADE
NEOPRENE GASKET
MATCH EXISTING
(TYPICAL)
WATERSTOP
COMPACTED
GRANULAR FILL
EXPOSED TOP
PARKING LOT TRANSVERSE SECTION
NO SCALE
Figure 4-13. Parking Lot Crossing; Exposed Top
4-16
CEMP-E
TI 810-32
10 January 2002
EXISTING BITUMINOUS
SURFACING
SAW CUT
(TYPICAL)
3" ASPHALT SURFACING
12"
MIN.
EXCAVATION WIDTH
12"
MIN.
1" MINIMUM
NEOPRENE GASKET
(TYP.)
TACK COAT
STABILIZED
BASE COURSE
WATERSTOP
COMPACTED
GRANULAR FILL
COVERED TOP
PARKING LOT TRANSVERSE SECTION
NO SCALE
Figure 4-14. Parking Lot Crossing; Covered Top
4-17
CEMP-E
TI 810-32
10 January 2002
EXISTING CONSTRUCTION
JOINT LOCATION
EXISTING
SIDEWALK
1/2 "
EXISTING
SIDEWALK
EXPANSION JOINT
MATERIAL, TYPICAL
NEOPRENE GASKET
MATCH EXISTING
SIDEWALK
(TYPICAL)
WATERSTOP
COMPACTED
BACKFILL
SIDEWALK TRANSVERSE SECTION
NO SCALE
Figure 4-15. Sidewalk Transverse Section Detail.
4-18
CEMP-E
TI 810-32
10 January 2001
"Z"
"ZZ"
"Z"
SYMMETRICAL
ABOUT >
FS
B1+2
FS
B1
A
B2
FS
"YY"
FS
"X"
"W"
FS
FS
FS
B1-4
A
B2+4
SEE PLAN FOR
SUPPORT TYPES
AND LOCATIONS
B2+4
A
B1-4
COVERED TRENCH
NEW 4"
CONCRETE
SIDEWALK
FILLER,
INSTALL
AT LOOP
"U"
ANCHOR TO ANCHOR DISTANCE VARIES -
SEE PLANS FOR STATIONING
NOTES:
1. DIMENSIONS A, B, AND B2 ARE FROM THE "TRENCH
DIMENSION SCHEDULE", TABLE 4 3.
2. DIMENSIONS Z,ZZ,Y,YY,W,H,X, AND U ARE FROM THE
"EXPANSION LOOP SCHEDULE", TABLE 4-4.
EXPANSION LOOP
NO SCALE
NOTE TO THE DESIGNER:
BETWEEN THE FIRST FS
AT THE LOOP
AND THE ANCHOR, ALTERNATEFS
AND
GS
(FIGURES 4-2 AND 4-3)
TO KEEP PIPING SYSTEM CENTERED
IN TRENCH.
Fig. 4-16. Expansion Loop Detail.
4-19
"Y"
SEE PLAN FOR
SUPPORT TYPES
AND LOCATIONS "X"
"H"
SEE FIG. 4 1
B2-2
FREE SUPPORT
(TYP.),
"Y"
A
TYPICAL
BOTH SIDES
CEMP-E
TI 810-32
10 January 2002
TRENCH TOP SEALANT
1/2 "
BACKING ROD
1/2 "-+ 1/8 "
DISCONTINUE REINF.2"
FROM JOINT (TYP.)
TRENCH COVER JOINT-ELEVATION
NO SCALE
Figure 4-17. Trench Cover Joint Detail.
4-20
CEMP-E
TI 810-32
10 January 2002
HEAVY DUTY MANHOLE FRAME &
TYPE "C" COVER NEENAH
OR EQUAL
6"MIN
CAST FRAME INTO
TOP SLAB
"A"*
EDGE OF SLAB
TRENCH TOP SLAB
MACHINED BEARING SURFACE
DIMENSION "A"
24 INCHES FOR VENT ACCESS
12 INCHES FOR INSPECTION PORT
* CENTER MANHOLE ON TRENCH TOP
ACCESS COVER
NO SCALE
Figure 4-18. Access Cover Detail.
4-21
CEMP-E
TI 810-32
10 January 2002
LOW POINT
PITCH DOWN
TO DRAIN
1" SCHED 80 PIPE
1" GLOBE VALVE
THREADED PIPE CAP,
DO NOT SEAL WELD
WELD
SOCKET WELD
NOTE:
LOW POINTS IN ALL PIPING TO
BE DRAINED.
DRAIN
NO SCALE
THREADED PIPE 1/2 "O
SCHED. 80
SOCKET WELD
CAP(DO NOT WELD)
1/2 " SOCKOLET
1/2 " GLOBE VALVE
HIGH POINT
VENT
NO SCALE
VENT AND DRAIN DETAILS
Figure 4-19. Vent and Drain Details.
4-22
CEMP-E
TI 810-32
10 January 2002
Table 4-1. Channel Support Schedule
LOCATION
PLATE
ANCHOR
STUDS
ANGLE
*
CHANNEL
BOLTS
Free and
Guided
Supports
1/2" x 10" x
10"
4-1/2" x 4"
2" x 2" x 1/4"
x 6" long
MC 6" x 15.3"
1/2"
Anchor
Supports
3/4" x 10" x
10"
6-5/8" x 4"
2" x 2" x 1/4"
x 6" long
MC 8" x 22.4"
3/4"
* Schedule for channel detailed in Figure 4-4.
NOTE TO THE DESIGNER:
Channels exceeding loadings indicated in manual shall be designed for vertical and axial loadings
encountered.
4-23
CEMP-E
TI 810-32
10 January 2002
Table 4-2. Support spacing schedule
\1\ MAXIMUM HORIZONTAL PIPE SUPPORT SPACING FOR STEEL /1/
DISTRIBUTION PIPING
PIPE SIZE
SPACING
(INCHES)
(FEET)
1
7
1-1/4
7
1-1/2
9
2
10
2-1/2
11
3
12
2-1/2
13
4
14
5
16
6
17
8
19
10
22
12
23
14
25
16
27
18
28
20
30
24
32
30
33
NOTES TO THE DESIGNER: These spacings are maximum for horizontal, straight
runs. More closely spaced supports must be provided for bends and risers and at
equipment.
4-24
CEMP-E
TI 810-32
10 January 2002
4-25
CEMP-E
TI 810-32
10 January 2002
Table 4-3. Trench dimension schedule.
TRENCH DIMENSION SCHEDULE
STANDARD
TRENCH
INTEM NO.
[PIPE
SIZES
(INCHES)
A
B1
B2
C*
D1
D2
6”
6”
6”
6”
6”
6”
6”
6”
E*
F
MIN.
Hw
MIN.
NOTES TO THE DESIGNER:
1. CLEARANCES BASED ON THE THICKEST INSULATION, IF LESS INSULATION (LOWER
“k”) IS PROVIDED. DIMENSIONS C, D, E AND F WILL BE DIFFERENT THAN SCHEDULED.
HOWEVER, OVERALL TRENCH DIMENSIONS SHSALL REMAIN THE SAME. C* & E*
DIMENSIONS MUST BE MAINTAINED THROUGHOUT ALL STRAIGHT SECTIONS OF
TRENCH TO ALLOW PROPER CLEARANCES FOR EXPANSION.
2. SCHEDULE DESIGNATIONS ARE ASSOCIATED WITH TRENCH DIMENSION SECTION,
FIGURE 4-5.
Table 4-4. Expansion Loop Schedule*
Loop
Name
Line
Sizes
X
Y
YY
Z
ZZ
W
H
U
REMARKS
*See Expansion Loop Detail for Designations (Figure 4-16).
NOTE TO THE DESIGNER:
If only one support is required along parallel leg of loop, ZZ =0. If only one
support is required along perpendicular legs of loop, YY = 0.
4-26
W
CEMP-E
TI 810-32
10 January 2002
CHAPTER 5
PRE-ENGINEERED UNDERGROUND HEAT DISTRIBUTION SYSTEM
5-1. GENERAL. Unlike Heat Distribution Systems in Concrete Trenches, which are totally designed by
the designer, Pre-engineered Underground Heat Distribution Systems are designed by the system
manufacturer. These pre-engineered systems are factory fabricated in lengths, which are transported
to the site for field assembly. Other types of systems and materials are continuously being evaluated
and will be included in guide specifications and this manual when deemed acceptable. There are two
types of these systems. The DDT type is allowed for severe, bad and moderate site conditions. In
severe sites allow only drainable-dryable-testable type systems. In bad and moderate sites allow DDT
and water spread limiting systems. These \1\ site /1/ conditions (or classifications) are described in
detail in the guide specifications. Although the manufacturer is responsible for the pre-engineered
system design, the project designer also has design responsibilities which include establishing the site,
soil, and groundwater conditions, pipe sizes, proposed routing (including construction limits) estimated
length, elevations, profiles of the system along with existing and finished earth surfaces and
obstructions \1\ within /1/ 8m (25 feet) of the system centerline including adjacent or crossing utilities.
The project designer also provides information on location and design of manholes and entrances to
buildings and manholes.
5-2. MANUFACTURER'S RESPONSIBILITY.
a. Pre-engineered Underground Heat Distribution System design. The manufacturer is responsible
for the Pre-engineered Underground Heat Distribution System. This responsibility includes any or all of
the following: insulation types, guided and anchor supports, end seals, casing and piping joint closure,
casing type and thickness, and carrier pipe depending on
the type of Pre-engineered Underground
Heat Distribution System provided. There are two types of Pre-Engineered Underground Heat Distribution
Systems. The drainable-dryable-testable system is a factory fabricated system, which includes a watertight outer protective casing of steel, an air space, and an insulated carrier steel pipe. Casing drains and
vents
are provided in end plates, which are installed in valve manholes. DDT systems can be used for
any heating medium including HTHW, high and low pressure steam, and condensate return and in any
site condition (severe, bad or moderate). The water spread limiting
systems is also a factory fabricated
system, which includes an outer protective casing and
an insulated carrier pipe. The system is
fabricated in sections, which are independent from each other. Ground water or condensate, which leaks
from or into one section, cannot travel into the next section. Field-assembly of the sections requires no
welding; the sections are pushed together and are sealed with a system of couplings and seals. WSL
systems can
be used only in bad and moderate site conditions. The designer must determine the
site conditions before a system type is selected. The site conditions will be considered severe, bad or
moderate based on the site investigation results. For DDT and WSL systems, steam and condensate
lines must always be installed in separate casings, as shown for a DDT system in figure 5-1, due to the
corrosion problems associated with condensate return systems. Water systems may use just one
casing for both supply and return pipes as detailed for a DDT system in figure 5-2, although installing the
pipes in separate casings is preferred by most users because it is less difficult to isolate leaks. The tops
of the casings will typically be buried between 2 and 6 feet below grade. However, note that excessive
burial depths increase the installation and repair costs and should be avoided where possible.
b. Expansion compensation. The manufacturer is responsible for the system expansion
compensation. A detailed stress analysis will be submitted for review as part of the contract requirements.
The manufacturer will normally make use of expansion loops and bends to absorb system expansion in DDT
systems. For WSL systems, field joints may be used to accommodate expansion. Except in rare
instances, expansion joints will not be permitted.
5-1
CEMP-E
TI 810-32
10 January 2002
c. Pre-engineered system's representative. The manufacturer is required to ensure that a qualified
direct employee of the system manufacturer is present to guarantee proper installation when the following
types of work are performed:
(1) inspection, unloading and storage of materials.
(2) inspection of trench prior to laying of casing.
(3) inspection of concrete thrust blocks.
(4) hydrostatic test of all service lines.
(5) field joint closure work.
(6) air test of casing.
(7) coating patch work.
(8) holiday test of casing coating.
(9) initial backfill up to 10 inches above the top of the casing.
(10) radiographic weld examination.
(11) startup and operation tests.
5-3. PROJECT DESIGNER’S RESPONSIBILITY.
a. Site information. As with all buried distribution systems, the site investigation is the responsibility of
the designer. As described in chapter 3 of this manual, the designer will obtain soil borings, be responsible for
designing the grading in the area, investigate all utilities for possible conflicts, and design for utility relocation as
necessary. The designer must then determine the site conditions (severe, bad, or moderate) before a system
type (DDT or WSL) is selected. The designer will then provide plans and profiles of the Pre-engineered system
routing. The designer will show approximate slope of the system (1 inch in 20 feet is required to ensure
drainage). This slope must be maintained in the entire system including through each leg of each expansion
loop to ensure proper system drainage.
b. Valve manholes. The designer will design all valve manholes for the system as described in chapter 3
of this manual. The manholes will be no further apart than 500 feet to minimize excavation if a leak in the
system must be found. The manholes will also be provided at all high (vent) points and low (drain) points in the
system. The valve manholes will include ground water drainage capabilities as explained in chapter 3. Casing
vents and drains will be included for maintenance of the casing air space in DDT systems as shown in figure
5-3.
c. Insulation. The insulation types used on the Pre-engineered Underground system will only be those
that are listed in the guide specification. The insulation thickness tables in the guide specification will be used
in determining required insulation thickness. These insulation thicknesses were developed using life cycle cost
analyses.
d. Cathodic protection. The designer will be responsible for the cathodic protection design for all
systems with coated steel casings. The designer shall also require that dielectric flanges be provided to isolate
the system’s cathodic protection system from non protected systems. These dielectric flanges shall always
be installed inside valve manholes.
e. Review. The designer will provide a detailed review of the manufacturer's shop drawings to ensure the
5-2
CEMP-E
TI 810-32
10 January 2002
system meets the requirements of the contract. As a minimum, the following items are required in this review
process:
(1) carrier pipe size and thickness.
(2) insulation thickness, type and K-value.
(3) casing material and thickness.
(4) casing coating material and thickness.
(5) verification of constant system slope to all low points (proposed elevations at all casing joints
on submitted shop drawing layouts).
(6) cathodic protection design.
(7) manufacturer’s system stress analysis.
5-3
CEMP-E
TI 810-32
10 January 2002
CARRIER PIPE (TYPICAL)
AIR SPACE (TYPICAL)
GROUND SURFACE
2' (MIN.)
2' (MIN.)
CASING (TYPICAL)
INSULATION (TYPICAL)
TWO CASING SYSTEM
NO SCALE
Figure 5-1. Two Casing System Detail.
5-4
CEMP-E
TI 810-32
10 January 2002
GROUND SURFACE
2'(MIN)
>
INSULATION (TYPICAL)
CARRIER PIPE NO. 2
CASING
CARRIER PIPE NO. 1
NOTE: A STEAM LINE AND A CONDENSATE LINE ARE NOT
TO BE INSTALLED IN THE SAME CASING.
SINGLE CASING SYSTEM (DDT)
NO SCALE
Figure 5-2. Single Casing System Detail.
5-5
CEMP-E
TI 810-32
10 January 2002
90^ RETURN BEND
(TYP.)
12"
MANHOLE COVER
EXISTING FINISH GRADE
VALVE MANHOLE WALL
STRAP & ANCHOR
TO WALL (TYP.)
CASING VENT
BRASS FITTING
(TYP.)
1" CASING VENT
RISER (TYP.)
PIPE SLEEVE
CARRIER PIPES
1" CASING DRAIN
BRASS PLUG
6"
PIPE CASING
CASING, VENT, AND DRAIN (DDT)
NO SCALE
Figure 5-3. Casing, Vent, And Drain Detail.
5-6
CEMP-E
TI 810-32
10 January 2002
CHAPTER 6
PREFABRICATED UNDERGROUND HEATING/COOLING DISTRIBUTION SYSTEM
6-1. GENERAL. This system is similar to Pre-engineered Underground Heat Distribution System (chapter
5) because it is factory fabricated in lengths, which are transported to the site for field assembly. However,
the system is not allowed for any high temperature water (greater than 200 deg. F) or steam/condensate
systems. The project designer is also responsible for more of the overall design.
6-2. SYSTEM DESIGN.
a. Site information. As with all heat distribution systems, the site investigation is the responsibility
of the designer. The designer will obtain soil borings, be responsible for designing all grading in the area,
and investigate all utilities for possible conflicts with the system. The designer will provide detailed design
plans and profiles of the distribution system routings. The design will ensure a minimum slope of 1 inch in
20 feet is maintained between valve manholes. The site information requirements are covered in detail in
chapter 3 of this manual.
b. Valve manholes. The designer will design all valve manholes for the system as covered in chapter
3 of this manual. As with valve manholes for the Pre-engineered Underground Heat Distribution System,
manhole spacing will not exceed 500 feet and all manholes will have drainage capabilities. Also, all valves,
flanges, unions, and couplings shall be located within the manholes.
c. System Material Selections. Although this system is manufactured in sections in a factory, the
designer will specify all materials.
(1) Piping. The piping materials allowed are steel, copper tubing, reinforced thermosetting resin
plastic (RTRP), or polyvinyl chloride (PVC). RTRP piping can not be routed through valve manholes with
heating systems that could damage the RTRP. PVC piping can not be routed in any valve manhole with any
other heating system piping due to its comparatively low temperature tolerance.
(2) Casing. Allowed casing materials are PVC, polyethylene (PE), or RTRP. Because these
casing materials are susceptible to damage from high temperatures, they must be installed a minimum of
15 feet from buried HTHW or steam systems to avoid plastic deformation and failures of the casing
materials.
(3) Insulation. Insulation type for these systems is typically polyurethane foam. Open cell type
insulations, such as fiberglass, mineral wool or calcium silicate, are unacceptable for use with chilled water
systems due to the tendency of condensation forming in these insulations. Insulation thickness will be
specified in the guide specification.
d. Expansion compensation. The designer will perform expansion compensation calculations as
covered in chapter 3 of this manual. When required, based on these calculations, sizes and locations of all
expansion loops and bends, and any other expansion-compensating device, will be clearly shown on the
contract drawings. The designer shall provide expansion loop details.
6-1
CEMP-E
TI 810-32
10 January 2002
CHAPTER 7
ABOVEGROUND HEAT DISTRIBUTION SYSTEMS
7-1. GENERAL. Aboveground distribution systems have the lowest first cost and lowest maintenance
costs of any distribution system described in this manual and are completely designed by the project
designer. This system is a good application for industrial areas and where water tables are high. Many
installations, however, do not desire to have distribution piping above ground for aesthetic reasons.
7-2. SYSTEM DESIGN.
a. Site information. The designer will determine information on the site. The designer will design
all grading for the area and investigate all utilities for conflicts. The designer will provide detailed plans and
profiles of the above ground distribution system routing. Although this system is aboveground, profiles
will indicate system drain and vent points and also potential interferences between the concrete support
piers and any buried utilities.
b. Piping and fittings. All carrier piping and pipe fittings will be carbon steel and will be designed to
satisfy the temperature and pressure requirements of the system. Materials will conform to the
requirements of the guide specification.
c. Pipe supports. The two most common types of aboveground distribution systems are low profile
and high profile.
(1) Low profile system. A typical low profile support is shown in figure 7-1. In this system, the
distribution piping is mounted to concrete piers by means of pipe supports. Typically, the bottoms of the
pipes are mounted no more than 4 feet above grade except at road crossings, which usually incorporate
high profile supports. Typical anchor, free, and guided pipe supports mounted to the concrete piers are
detailed in figure 7-2, figure 7-3, and figure 7-4. Spacing of supports in straight runs of piping will conform
to the support spacing schedule in table 4-2. Provide extra supports, as necessary, at pipe bends and
risers. Requirements for concrete piers and pipe supports are included in the guide specification.
(2) High profile systems. High profile systems are routed high enough to cross roads and avoid
obstructions. Typically the piping will be installed 14 to 16 feet above grade. The system presented in
this manual uses 6-inch concrete-filled pipes embedded in concrete footings as detailed in figure 7-5. The
pipe guides are mounted on channels at the top of the support pipe as detailed in figure 7-6. The pipe
anchors are also mounted to channels and then stabilized with guy cables as shown in figure 7-7.
Structural design for the structural members on these high profile supports in figure 7-6 and 7-7 are for
water filled, schedule 40 steel pipes up to 10-inch nominal size. Conditions outside these constraints
must be designed on a case-by-case basis. The designer for each anchor application will also size the
guy cables. Spacing of supports in straight runs of piping will conform to the support spacing schedule in
table 4-2. Extra supports will be added, as necessary, at pipe bends and risers. Concrete footings and
high profile supports will conform to the requirements of the guide specification.
c. Insulation and jacketing. All piping on aboveground systems shall be insulated and jacketed.
Insulation thicknesses will be determined by insulation tables provided in the guide specification. These
insulation thicknesses were developed using life cycle cost analyses. All insulation will be covered with a
jacketing material in conformance with the guide specification.
e. Expansion Compensation. Expansion loops and bends will be designed as described in chapter 3 of
this manual. Expansion loops will be located to minimize impacts to ground level interferences such as trees
and sidewalks. For horizontal expansion loops, pipe supports will be spaced less than the maximums listed in
7-1
CEMP-E
TI 810-32
10 January 2002
table 4-2 because of the extra bends and associated movement in the loops. In low profile systems, vertical
expansion loops may be used as road crossings. Details will be provided indicating support types and
locations throughout the loops and bends.
f. Vents and Drains. Provide venting of all piping high points and draining of all low points to allow
total drainage of the system. Vent and drain locations will be indicated on the profile drawings. Vents and
drains are similar to those used for the concrete shallow trench system, figure 4-15.
g. Transition to Buried Systems. When a buried system transitions to an aboveground system a valve
manhole will be provided at that point. A manhole top penetration will be provided to allow expansion of the
distribution piping in the man-hole top yet keep rain and ground water out of the manhole. Figure 7-8 shows
such a transition in a valve manhole with a concrete cover. The valve manhole used for this transition must be
large enough to be accessible and will be designed in accordance with chapter 3 of this manual.
7-2
CEMP-E
TI 810-32
10 January 2002
A
12"
A
10" X (A 2) X 3/8 "
STEEL BASE
PLATE
VARIES
DIRECTION OF PIPE
EXPANSION
6"
3"
B
B
A
A
3/4 " ANCHOR BOLT
12" MIN. LENGTH
WT 8 X 13, 15"
LONG, WELD
TO PIPE
WT 8 X 13,
15" LONG FOR FREE AND
GUIDED SUPPORTS, 10"
LONG FOR ANCHOR SUPPORT
LOCATED AS INDICATED IN
"COLD CONDITION" TO
ACCOMODATE EXPANSION.
1" GROUT
ANCHOR BOLT
FIN. GRADE
B
B
WELD
BASE PLATE
3"
A
A
A
A
A
A
A
A
A
A
A
A
"A"
A
1' 0" BELOW DESIGN FROST
DEPTH OR 3' 0" WHICHEVER
IS GREATER
A
A
A
REINFORCED
CONCRETE
SUPPORT
BASE
A
FRONT VIEW
#[email protected]" O.C.
BOTH WAYS,
EACH FACE
12"
A
TYPICAL
SECTION
LOW PROFILE PIPE SUPPORT
NO SCALE
Figure 7-1. Typical Low Profile Support Detail.
7-3
CEMP-E
TI 810-32
10 January 2002
INSULATION
PIPE
3/16 10
10" WT 8X13
3/16 10
ANCHOR SUPPORT AS
NO SCALE
Figure 7-2. Typical Anchor Pipe Support.
7-4
CEMP-E
TI 810-32
10 January 2002
INSULATION
PIPE
15" WT 8X13
3/16 10
FREE SUPPORT
NO SCALE
Figure 7-3. Typical Free Pipe Support.
7-5
FS
CEMP-E
TI 810-32
10 January 2002
INSULATION
PIPE
1/4
10
15" WT 8X13
3/16
10
10" LONG 1/4 "
BENT P
L
7/8 "
1/4 "
GUIDED SUPPORT GS
NO SCALE
Fig. 7-4. Typical Guided Pipe Support.
7-6
CEMP-E
TI 810-32
10 January 2002
6" STD. STEEL PIPE
FILLED WITH CONCRETE
1"
GRADE
6"
#[email protected] 12 TIES
"A"
*
4-#5
1'-6"SQ
5-#4 E.W.
1'
4'-0" SQ
HIGH PROFILE BASE
NO SCALE
NOTES TO THE DESIGNER:
* "A" IS THE DESIGN FROST DEPTH,
SEE TM 5-809-1 FOR FROST DEPTH
1. SITE SPECIFIC DESIGN REQ'D BASED ON
LOADS AND SOIL CONDITIONS.
Figure 7-5. Typical High Profile Base Detail.
7-7
CEMP-E
TI 810-32
10 January 2002
3/4 " DIA. BOLTS
CHANNEL
MC 6 X 15.1
NUT & JAM NUT
TOP ROLLER
SUPPORTS AT
RISERS
A
DISTRIBUTION PIPE
3/4 " DIA. BOLT
1/2 " PLATES
15" MIN.
35" MAX.
1/4
A
PIPE
INSULATION SADDLE
ROLLER TYPE SUPPORT
10"
MAX
RETURN
DISTRIBUTION
PIPE
6" DIA. PIPE COLUMN
CONCRETE FILLED
SIDE VIEW
FRONT VIEW
PIPE GUIDE
NO SCALE
NOTE TO THE DESIGNER:
PIPE SUPPORT SHALL BE REDESIGNED
IF PIPE LARGER THAN 10" IS USED.
Figure 7-6.
Typical Pipe Guide Detail.
7-8
CEMP-E
TI 810-32
30 August 1999
12 '-0"
ANCHOR
ANCHOR
DEADMAN
12'-0"
GUY CABLE
60^
PIPE COLUMN
PLAN - PIPE ANCHOR
NO SCALE
RETURN
DISTRIBUTION
PIPE
DISTRIBUTION
PIPE
3/8 " PLATE
INSULATION
4'-0"
CONTINUOUS
WELD
2'-0"
8"
FILL WITH
CONCRETE
5/8 " DIA. BOLTS
3/8 " PLATE
W 12 X 40
(12" X 8")
CABLE
CLAMP
(TYP.)
1/2 " PLATES
10"
3/4 " DIA. BOLT
1/4
1/4 " FILLER
6" DIA. PIPE
COLUMN
SIDE VIEW
FRONT VIEW
HIGH PROFILE PIPE ANCHOR
NO SCALE
Figure 7-7. Typical Pipe Anchor Detail.
7-19
CEMP-E
TI 810-32
10 January 2002
STAINLESS STEEL BAND (TYPE 201
STAINLESS STEEL, 1/2 " WIDE, 0.030"
THICK) WITH CORROSION RESISTANT
BUCKLES
TRANSITION BOOT CLAMPED TO
INSULATION JACKET ABOVE &
SLEEVE BELOW (SEE NOTES)
SLEEVE GROUTED INTO MANHOLE
TOP (BEVEL EXPOSED END OF
SLEEVE)
18"min
CONCRETE VAULT TOP
6"
2"
2"
INSUL. & JACKETING
STEAM OR CONDENSATE LINES
A
B
C
A=OUTSIDE PIPE DIA.
B=OUTSIDE INSUL.&JACKET DIA.*
C=MIN. SLEEVE INSIDE DIA.=B+4
* SEE SPEC. FOR INSULATION THICKNESS
NOTES:
1. TRANSITION BOOT (LINER) SHALL BE:
- 25 MIL THICKNESS (MIN)
- E.P.D.M. TYPE MEMBRANE
- COMPATIBLE AT HIGH (220^ F) AND LOW
(-40^ F) TEMPERATURES
- RESISTANT TO ULTRAVIOLET LIGHT
DEGRADATION
2. LINER SEAM SHALL PROVIDE 2" MINIMUM OF OVERLAP.
USE SOLVENT CEMENT AS APPROVED BY LINER MANUFACTURER.
VALVE MANHOLE TOP PENETRATION
NO SCALE
Figure 7-8. Valve Manhole Top Penetration Detail.
7-10
CEMP-E
TI 810-32
10 January 2002
CHAPTER 8
SPECIAL CONSIDERATIONS
8-1. GENERAL. Although it is impractical to cover all special considerations, which arise in heating and
cooling distribution designs, this chapter presents typical design problems and solutions associated with
steam, high temperature hot water, low temperature hot water and chilled water systems.
8-2. STEAM SYSTEMS.
a. Trap Selection. Steam traps are used to separate the condensate and non-condensable gases
from the steam. Many types of traps are used on drip legs for steam distribution systems. Those trap
types include float and thermostatic (F&T), inverted bucket, thermostatic and thermodynamic (disc).
However, for buried heat distribution drip leg applications, inverted bucket or thermostatic (bimetallic type)
should be the trap types selected. For drip leg applications where freezing is a consideration,
thermodynamic type (installed vertically) or bimetallic thermostatic type should be selected.
b. Trap Sizing and Location. Trap sizing is important for obtaining an efficient steam distribution
system. Condensation in the steam line is caused by heat loss from the steam line. Trap life will be
shortened, function affected and excessive energy will be wasted if traps are oversized to handle the higher
initial startup condensate flows. Therefore, the traps should be sized for the condensate load seen during
the distribution system normal operation. Because the traps are not sized for startup loadings, the bypass
must be opened at startup to allow condensate to pass until the steam line has reached normal operating
temperatures (see figure 8-1). The designer will calculate heat loss and condensate flow for that particular
design using the methods presented in appendix D for determining condensate loads during normal
operation. It is critical that the designer calculate trap capacity using the Appendix D method for each trap
station in the design to ensure proper steam system operation. In addition to trap capacity, steam trap
type, differential pressures, and inlet pressure must always be provided on the contract documents. Do not
locate steam drip legs, with associated traps, more than 500 feet apart.
c. Drip Leg Sizing. Drip legs, installed vertically down from the steam pipe, are used to collect
condensate. Design all steam lines to slope at 1 inch in 20 feet minimum toward these drip legs. It is
preferable to slope the steam lines in the direction of steam flow whenever possible. The steam trap line
and bypass line are connected to the drip leg as indicated in figure 8-1. The drip leg will be the same
nominal pipe size as the main line (up to a 12-inch line) and will provide a storage capacity equal to 50% of
the startup condensate load (no safety factor, one-half of an hour duration) for line sizes 4 inches in diameter
and larger and 25% of the startup condensate load (no safety factor, one-half of an hour
duration) for line
sizes less than 4 inches. In no case will the drip leg be less than 18 inches in length or larger than 12
inches in diameter for all steam line sizes. The designer will calculate startup loads for drip leg sizing using
the methods presented in appendix D.
d. Trap Station Layout. All trap stations will be piped as indicated in figure 8-1, as a minimum. Valve
and strainer sizes will match the line sizes on which they are installed. Pipe lines to and from the steam trap
will be sized based on calculated trap capacity but will be no less than 3/4-inch nominal size (line size "A" on
figure 8-1). If reducing fittings are needed at the trap inlet and outlet, eccentric reducers must be used. The
bypass line will be sized to accommodate warm-up condensate loads. For steam systems with an operating
pressure of 150 psig or less and pipe sizes 12 inches or less, provide a ¾-inch bypass line. If the condensate
return main is a low pressure or gravity flow type, the trap discharge line will be routed through an
accumulator, as indicated in figure 8-2. The accumulator will lower the trap discharge temperature and
minimize flashing when the condensate is introduced into sloped condensate lines which are routed to
receiver/pump sets located in valve manholes. The pumps push the condensate back to the central plant in a
separate pressurized condensate line. See figure 8-3 for a duplex condensate pump set connection detail.
8-1
CEMP-E
TI 810-32
10 January 2002
This type of condensate return system is referred to as a "three pipe" or a "pumped return" system. If the
steam pressure is sufficiently high, it may be used to force the condensate through the condensate return
system to the central plant as shown in figure 8-1. No accumulator is required for this type system, which is
referred to as a "two pipe" system. Sizing of the lines for both of these systems is presented later in this
chapter.
e. Condensate Cooling System. Fiberglass reinforced plastic (FRP) piping is usually allowed for most
condensate return systems. Since internal corrosion is a frequent problem in steel condensate lines, FRP
eliminates this problem. However, the FRP materials cannot withstand as high of pressures or temperatures as
steel and often fail when exposed to these conditions. A common temperature in an FRP distribution piping
system where damage will occur is 250 deg. F. Condensate temperatures may exceed 250 deg. F. at the outlet
of steam drip leg traps on steam systems that have pressures greater than 15 psig. In order to use FRP
condensate lines in this case, a condensate cooling system will be employed, as detailed in figure 8-4. In this
system, the high temperature condensate is discharged into a cooling tank where it blends with the system
condensate. The blended condensate is then routed to the condensate main. Note that the detail shows the
FRP (or non-metallic) pipe transitioning to steel inside the valve manhole to avoid burying the transition point.
Also, note that nonmetallic piping will not be allowed in a manhole with high temperature hot water or high
pressure steam systems due to the potential for this pipe being exposed to damaging temperatures within the
manhole if the manhole floods or the carrier pipe on the heating system leaks.
f. Non-metallic Pipe Anchors in Valve Manholes. If anchoring of a non-metallic piping system is
required at the valve manhole wall to comply with the distribution system stress analysis, a typical method is
as detailed in figure 8-5. If the system is to be anchored at both of the valve manhole wall penetrations,
provide adequate piping bends in the manhole to accommodate the expansion between the two anchors.
Steel straps and bolts will be sized to accommodate the axial force of that particular piping layout. These
sizes will be entered on the detail. Also, valve manhole sizes must be large enough to accommodate the
anchors and still allow for maintenance access.
g. Pipe Sizing. Pipe sizing is critical to proper operation of both the steam and the condensate return
systems.
(1) Steam. There are several methods to size steam lines. One of the quickest and most popular
methods is using pressure drop versus flow rate charts, which provide steam velocities based on the required
flow and pressure drops. The American Society of Heating, Refrigeration, and Air Conditioning Engineers
(ASHRAE) Fundamentals Handbook, Chapter "Pipe Sizing", is a good source for these steam sizing tables.
Recommended velocities for various system pressure ranges are:
0 - 10 psig, saturated - 1,000 to 4,000 fpm
10 - 50 psig, saturated - 4,000 to 8,000 fpm
50 - 150 psig, saturated - 8,000 to 12,000 fpm
In addition, ensure the total pressure drop in the system will not be excessive. Steam pressure must be high
enough at the end users to meet all special process requirements.
(2) Condensate. As described previously in this chapter, there are basically two types of condensate
return systems used on central heating systems: the two pipe system (which uses steam pressure to force
condensate back to the plant) and the three pipe, or pumped return, system. When sizing lines for these
condensate return systems, table 8-1 will be used for guidance.
h. Steam System Material Selection.
(1) Valves. For high-pressure steam systems (125 psig or greater), valves will be 300-pound class and
8-2
CEMP-E
TI 810-32
10 January 2002
will have welded ends. Steam and condensate valves at lower pressures will be 150-pound class with welded
ends. Valves on trap stations, including the bypass valve, will be 150-pound class with threaded ends. Shutoff
valves will be gate type.
(2) Fittings. All fittings in the steam distribution system, except as discussed for valves, will be
welded except at equipment, traps, strainers, and items which require frequent removal. These items will be
threaded or flanged.
(3) Piping. Steam and condensate piping will usually be carbon steel conforming to ASTM A 53,
Grade B, Type E or S. Steam piping will be schedule 40. Condensate lines will be schedule 80 as will all
welded piping less than 1-1/2 inches. Condensate lines in a pre-engineered underground heat distribution
system may be FRP as discussed in chapter 5.
i. Field Joints. Radiographic examination of all carrier pipe field joints is required.
8-3. HTHW SYSTEMS.
a. Pipe Sizing. Sizing lines for HTHW systems is similar to any water system, except at high
temperatures water becomes less dense and less viscous, and, therefore, the mass flow rate of the system
must be calculated considering the lower density (usually temperatures are around 400 deg. F for HTHW).
m = q x 60 min/hr x 0.1335 ft 3 /gal x ?
where
q = system flow in gal/min
m = mass flow rate in lbm/hr
? = density of water at maximum system temperature in lbM/ft 3
Pressure drop versus flow charts may be used to determine line size, such as the chart included in appendix
B. This chart takes into account the characteristics of higher temperature water systems. Recommended
velocities for various HTHW flows are as follows:
Up to 10,000 lbm/hr
10,000 to 30,000 lbm/hr
30,000 to 200,000 lbm/hr
200,000 lbm/hr on up
-
1 to 2 feet/sec
2 to 3 feet/sec
3 to 5 feet/sec
(use velocity to accommodate 0.50 psi/100 ft., maximum)
b. HTHW System Material Selection
(1) Valves. All valves on HTHW systems will be 300-pound class with welded ends. Shutoff
(isolation) valves will be gate type. Valve packings must be capable of handling the pressures and
temperatures associated with HTHW systems.
(2) Fittings. All fittings on HTHW systems will be welded. The only exceptions will be specialty
equipment such as dielectric flanges used to isolate the piping system from a cathodically protected system.
(3) Piping. HTHW piping will be carbon steel conforming to ASTM A53, Grade B, Type E or S. All
piping will be schedule 40 except for welded pipe less than 1-1/2 inches, which will be schedule 80.
8-3
CEMP-E
TI 810-32
10 January 2002
8-4. LTHW and CW systems.
a. Pipe Sizing. The most efficient method of determining pipe size for LTHW and CW systems is to use
head loss vs. flow rate charts such as those found in ASHRAE Fundamentals, Chapter "Pipe Sizing". These tables
are based on 60 deg. F water so for chilled water pipe sizing there is little error introduced using these charts. For
LTHW systems, the use of the charts does introduce some error. However, the error is on the conservative side
(the charts overstate the pressure drop of LTHW).
b. LTHW and CW Material Selection.
(1) Valves. Typically, valves on either LTHW or CW systems will be 150-pound class and will be
located in the valve manholes. Ball valves provide a good means for line isolation. Although nonmetallic valves
are sometimes allowed for these systems, metallic valves should be used for durability.
(2) Piping. The most common piping materials used for LTHW and CW systems are steel, copper
tubing, reinforced thermosetting resin pipe (fiber- glass) and, for CW only, polyvinyl chloride and polyethylene.
However, do not include nonmetallic piping in the same valve manholes with HTHW and steam systems. Chilled
water lines using PVC piping must be installed in separate valve manholes since PVC can be thermally
damaged at relatively low temperatures. Outside the valve manholes, a separation of 15 feet (minimum) must be
maintained between pre-engineered underground HTHW and steam systems and PVC encased, prefabricated
underground heating/cooling distribution systems to avoid thermal degradation of the PVC.
8-4
CEMP-E
TI 810-32
10 January 2002
STEAM MAIN
HIGH OR MEDIUM
PRESSURE CONDENSATE
RETURN LINE
1" DRAIN
GATE VALVE
* SEE NOTE TO
THE DESIGNER
1"
BYPASS
BALL VALVE
DRIP LEG
ISOLATION GATE
VALVE (TYPICAL)
3/4 "
1" DRAIN
GATE VALVE
CHECK
VALVE
THREADED
CAP
STRAINER WITH
BLOWOFF VALVE
"A"
STEAM
TRAP
3/8 " THREAD-O-LET
TEST CONDITION
REDUCER ,IF NEEDED
(TYPICAL)
TRAP STATION LAYOUT ISOMETRIC
NO SCALE
NOTE TO THE DESIGNER:
* HIGH PRESSURE CONDENSATE DISCHARGE
FROM THE TRAP WILL NOT BE DIRECTLY
ROUTED TO A GRAVITY OR LOW PRESSURE
CONDENSATE SYSTEM. IN THIS INSTANCE,
A 3/4 " LINE WILL BE ROUTED TO AN
ACCUMULATOR BEFORE BEING ROUTED TO A
CONDENSATE PUMP (SEE FIGURE 8-2).
Figure 8-1. Trap Station Layout Schematic.
8-6
CEMP-E
TI 810-32
10 January 2002
INSTALL 1/2 " ANCHOR
BOLTS, 2 REQUIRED
4"
BRACKET
1
.
SCALE. 1 2 INCH = 1 FOOT
12"
9"
0
3"
6"
1'
3/4 " GATE VALVE
SEE
BRACKET
DETAIL
8" WELDING CAP
8" SCH. 40 PIPE
FROM TRAP
3'0"
REINFORCING PLATE
TO CONDENSATE
RETURN LINE
10
"
1'6"
4"
2"
MANHOLE
WALL
3/4 " GATE VALVE
ACCUMULATOR
.
SCALE. 1 INCH = 1 FOOT
12"
6"
0
1'
Fig. 8-2. Accumulator Detail.
8-7
CEMP-E
TI 810-32
10 January 2002
VENT THRU VALVE
MANHOLE TOP
CONDENSATE
PUMP DISCHARGE
CHECK VALVE
CD
CD
CONDENSATE IN
BALL DRAIN
VALVE
PUMP
(TYP. OF 2)
6" CONC. PAD
CHECK VALVE
DUPLEX CONDENSATE PUMP
SET CONNECTION DETAIL
NO SCALE
Fig. 8-3. Duplex Condensate Pump Set Connection Detail.
8-8
8-9
COOLING TANK: 18 INCHES LONG, 8"
DIA. SCHEDULE 80 PIPE WITH 8"
DIA. WELD CAPS
DIFFUSER: 10 INCHES OF 1/2 "
PIPE WITH MINIMUM OF 18 - 1/8 "
DIA. HOLES, CAPPED AT END
3/4 "
FROM STEAM
MAIN TRAP
VAULT WALL
6"
INSULATED NONMETALLIC PIPE (TYP)
18" MIN.
18" MIN. FROM FLR.
0 - 150 PSIG
GAGE WITH COCK
1" MIN. DIA.
UNION (TYP.)
GATE VALVE
(TYP.)
3/4 " DISCHARGE
ABOVE GRADE
NON-METALLIC TO
STEEL COUPLING
OR FLANGE
ADJUSTABLE ANGLE THERMOMETER WITH 30^F TO
300^ F RANGE AND A 3/4 " NPT BRASS WELL
1/2 " DRAIN
3/4 " TEMPERATURE
RELIEF VALVE SET TO
OPEN AT 250^
PUMPED INSULATED RETURN CONDENSATE
MAIN (SCH. 80 STEEL)
SYSTEM PRESSURE
MAXIMUM TRAP
(PSIG)
CAPACITY (LBS./HR.)
50
250
380
100
150
500
625
200
790
300
960
400
STEAM TRAP CAPACITY LIMITATIONS
CEMP-E
TI 810-32
10 January 2002
CONDENSATE COOLING SYSTEM
NO SCALE
Fig. 8-4
.
Condensate Cooling System for Non-metallic Pipe Detail.
CEMP-E
TI 810-32
10 January 2002
STEEL STRAPS (TYP.-4)
WEDGE ANCHOR BOLTS (TYP.-4)
SECTION
A
STEEL STRAP
(TYP.-4)
STEEL FLANGE
NON-METALLIC
PIPE
WELD RISER CLAMP TO
STEEL PIPE (TYP.-2)
INTERIOR STEEL PIPE
ROUTED TO ACCOMODATE
EXPANSION
PRE-INSULATED CONDUIT
SLEEVE & SEAL
AS SPECIFIED
WELD STRAP TO RISER CLAMP
(TYP.-4)
A
PLASTIC FLANGE
WEDGE ANCHOR BOLTS
(TYP.-4)
WALL ANCHOR FOR NON-METALLIC PIPING SYSTEMS
NO SCALE
Fig. 8-5. Non-metallic Piping System Anchor Detail.
8-10
CEMP-E
TI 810-32
10 January 2002
Table 8-1. Pipe sizing guidelines for condensate return systems.
TWO-PIPE SYSTEM SIZING GUIDELINES
_____________________________________________________________________________
?? DETERMINE CONDENSATE LINE PRESSURE (AS OBSERVED FROM ON-SITE
PRESSURE GAGES).
?? DETERMINE CONDENSATE LOAD (lbm/hr) FROM CENTRAL PLANT LOGS AND OTHER
INPUT.
?? ASSUME CONDENSATE AT TRAP DISCHARGE IS A COMBINATION OF CONDENSATE
AND FLASH STEAM.
?? SIZE LINE TO ACCOMMODATE 5,000 ft/min STEAM AND CONDENSATE MIXTURE
VELOCITY AND TO ENSURE MIXTURE PRESSURE IS HIGH ENOUGH TO OVERCOME
LINE LOSSES.
THREE-PIPE SYSTEM SIZING GUIDELINES
____________________________________________________________________________________
GRAVITY LINE
??
SLOPE AT 1 inch/20 feet (MINIMUM) TOWARD RECEIVER.
??
??
TOTAL PRESSURE DROP LESS THAN 0.25 psi.
LINE SIZE WILL BE TWO (2) INCHES.
PUMPED LINE
??
SIZE PUMPS TO MOVE CONDENSATE TO THE CENTRAL PLANT AT THE REQUIRED
HEAD AT 200 deg. F.
8-10
CEMP-E
TI 810-32
10 January 2002
APPENDIX A
REFERENCES
Government Publications
Department of the Army
TM 5-802-1
Economic Studies for Military Construction Design-Applications
TM 5-809-1
Load Assumption for Buildings
Non-government Publications
American National Standards Institute (ANSI)
1430 Broadway, New York, NY 10018
H35.1
(1990) Alloy and Temper Design System for Aluminum
American Society for Testing and Materials (ASTM)
1916 Race Street, Philadelphia, PA 19103
A 36
(1991) Structural Steel
A 53
(1988a) Pipe, Steel, Black and Hot Dipped, Zinc
Coated, Welded and Seamless
A 123
(1989a) Zinc (Hot-Dip Galvanized) Coatings on
Iron and Steel Products
A 615
(1990) Deformed and Plain Billet-Steel Bars for
Concrete Reinforcement
American Society of Heating, Refrigerating, and Air Conditioning Engineers, Inc.,
1791 Tullie Circle, N.E., Atlanta, GA 30329
ASHRAE Handbook
Fundamentals
ASHRAE Handbook
HVAC Systems and Applications
American Society of Mechanical Engineers (ASME),
22 Law Drive, Box 2300, Fairfield, NJ 07007-2300
B31.1
(1989) Power Piping
Canadian Society of Civil Engineers,
Montreal, Quebec, Canada
(1986) Cold Climate Utilities Manual
A-1
CEMP-E
TI 810-32
10 January 2002
APPENDIX B
B-1
CEMP-E
TI 810-32
10 January 2002
APPENDIX C
CONDENSATION LOAD CALCULATIONS (NORMAL)
Step #1 Determine the heat loss per foot of line.
Q = 2? (Tst - Tout)/(ln(ro/ri )/kp + ln(rio /ro) /kin + 1/3r io )
Assumptions. This equation models an insulated pipe surrounded by air. The convective
resistance between the insulation and the outside of the pipe is assumed to be negligible. Also,
the convective heat transfer coefficient outside of the insulation is assumed to be 3 BTU/hr-ft2
deg. F.
Step #2 Determine the flow of condensate from the heat loss calculated in step #1.
m = Q/(hst - hcon)
Step #3 Multiply the flow rate per foot, calculated in step #2, by the total number of feet of steam
line that slopes toward the trap in question. The result is the minimum flow capacity of the trap.
where:
Q
= heat loss per foot of pipe; Btu/hr-ft
Tst
= temperature of steam; deg. F
Tout
= temperature of ambient conditions; deg. F
ro
= outside pipe radius; feet
ri
= inside pipe radius; feet
rio
= outside insulation radius; feet
kp
= thermal conductivity of pipe; Btu/hr-ft- deg. F; (26 Btu/hr-ft-deg. F for steel)
kin
= thermal conductivity of insulation; Btu/hr-ft- deg. F * (see table below)
m
= mass flow rate of condensate; lbm/hr-ft
hst
= enthalpy of saturated steam; Btu/lbm
hcon
= enthalpy of condensate; Btu/lbm
-----------------------\1\ *K-value (Btu/hr-ft-deg. F /1/
Insulation Type
Mineral Fiber
Calcium Silicate
400 deg. F
0.034
0.042
300 deg. F
0.029
0.038
C-1
200 deg. F
0.024
0.035
CEMP-E
TI 810-32
10 January 2002
APPENDIX D
CONDENSATION LOAD CALCULATIONS (STARTUP)
Step #1 Determine the heat loss per foot of line.
The startup load can be calculated by determining the amount of heat that is
required to heat the steam pipe from an ambient temperature to the saturation
temperature of the steam the pipe is to carry. This is done by using the
following equation:
Q
= (vp * c p * ? p (tst - Tout))/t; Btu/ft
where:
vp
= ? (ro2- r2); in ft3/ft
Step #2 Determine the pounds of condensate per foot from the heat loss calculated in step #1.
m
= Q/(hst - hcon); lbm/ft
Step #3 Multiply the condensate per foot, calculated in step #2, by the
total number of feet of steam line that slopes toward the drip leg in
question. Then convert the total pounds of condensate to gallons assuming
200 F condensate:
Total Condensate Volume (gallons)=(m*L)*7.49 gallons/ft3
60.1 lbm/ft3
where:
Q
Tst
Tout
ro
ri
m
hst
hcon
cp
?p
= heat loss per foot of pipe; Btu/hr-ft
= temperature of steam; deg. F
= temperature of ambient conditions; deg. F
= outside pipe radius; feet
= inside pipe radius; feet
= mass flow rate of condensate; lbm/hr-ft
= enthalpy of saturated steam; Btu/lbm
= enthalpy of condensate; Btu/lbm
= specific heat of pipe (steel); (0.10 to 0.11) Btu/lbm/degrees F
= density of pipe (steel); (489) lbm/ft3
t
= length of time for startup; hrs (typically 0.5 hrs.)
L
vp
= total length of pipe draining to drip; ft
= volume of pipe material per foot; ft3/ft
D-1
Was this manual useful for you? yes no
Thank you for your participation!

* Your assessment is very important for improving the work of artificial intelligence, which forms the content of this project

Download PDF

advertisement