○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○ ○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○ Direct Fired Absorption Chillers 100 through 770 tons ○○○○○○○○○○○ ○ ○ ○ ○ ○ ○ ○○○○ Form No. 6066A WCGA FEATURES • Multi-shell design • Advanced proactive microcomputer • On line purging • Hybrid system equipped INTRODUCTION ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ Dunham-Bush has a legacy of innovation that spans most of this century. Since the early 1900’s the company has been providing its customers with innovative solutions for their air conditioning, heating and commercial refrigeration needs. Dunham-Bush now continues this legacy with the introduction of a complete line of absorption cooling products. Space Conditioning, later acquired by Dunham-Bush, was a bit ahead of its time in 1962 when it introduced a double effect absorption chiller. 2 Although this machine never really caught on, it was a pioneer in the market place and continued the Dunham-Bush tradition of innovation. Today, Dunham-Bush brings this technology into the future with a complete line of Absorption Chillers. This fact allows DunhamBush to have a better, more expansive service force for our customers. Dunham-Bush continues to offer complete solutions for our customers, so choose Dunham-Bush Absorption Chillers for your future needs. TABLE OF CONTENTS ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ Page Nomenclature ........................................................................................................................ 3 The Absorption Cycle Basic Principle ...................................................................................... 3 Features, Specifications and Benefits .................................................................................. 4-7 Selection Data & Technical Specifications ............................................................................ 8-9 Application Information.................................................................................................. 10-11 Physical Dimensions ............................................................................................................. 12 Typical Piping Schematic ...................................................................................................... 13 Electrical Wiring Drawing ................................................................................................ 14-16 Engineering Specifications .............................................................................................. 17-20 NOMENCLATURE W C G A - 100 Water Cooled Nominal Capacity (TR) Heat Source G = Gas O = Oil D = Gas or Oil (Dual Fuel) Absorption THE ABSORPTION CYCLE 100 120 150 180 210 240 280 320 360 400 450 500 550 620 690 770 ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ Basic principle The boiling point of water is directly proportional to the pressure. At atmospheric pressure water boils at 212°F (100°C). At lower pressure it boils at a lower temperature. At 0.24” Hg absolute (6mmHg absolute) the boiling point of water is 38.7°F (3.7°C). Further there is a large difference between the vapor pressure of LiBr and water. This means that if we heat the LiBr-water solution, the water will vaporize but the LiBr will stay in the solution and become concentrated. Lithium Bromide (LiBr) is a chemical similar to common salt (NaCl). LiBr is soluble in water. The LiBr water solution has a property to absorb water due to its chemical affinity. As the concentration of LiBr solution increases, its affinity towards water increases. Also as the temperature of LiBr solution decreases, its affinity to water increases. Absorption systems use heat energy to produce a refrigerating effect. In these systems the refrigerant, i.e. water, absorbs heat at a low temperature and pressure during evaporation and releases heat at a high temperature and pressure during condensation. 3 FEATURES, SPECIFICATIONS AND BENEFITS The Dunham-Bush Absorption Chillers have a multishell design, consisting of the upper shell which houses the condenser and low temperature generator, lower shell which houses the evaporator and absorber, high temperature generator with a suitably sized burner, heat exchangers, absorbent and refrigerant pump, purge pump, purge unit, inter- ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ connecting piping and a machine mounted control panel. Each chiller goes through a series of tests for leak tightness at the factory including the stringent helium leak detection test, for achieving highly reliable operation. Also the number of valves and gasketed joints is kept to the minimum to ensure leak tightness. High Temperature Generator The high temperature generator has a direct flue type furnace with a wetback and wetfront to ensure maximum heat exchange. The shell is made of carbon steel SA 516 Gr 70 and the seams are welded by TIG welding. The tubesheet, similarly made of carbon steel SA 516 Gr 70, has drilled holes to accommodate the tube and each hole incorporates a groove so as to enable leakproof locking. • Using round tubes means that the tubes can be evenly expanded and thus need to be welded only on the outside. These tubes can be removed in the eventuality of tube leak. Some manufacturers use elliptical or oblong tubes, which have to be welded both internally and externally and thus cannot be removed easily during leakage problems. The Dunham-Bush Absorption Chiller uses straight and plain, round tubes made of boiler quality, with 2" (50.8 mm) diameter and 0.144" (3.66 mm) wall thickness. Each tube is individually expanded and seal welded from the outside to the tubesheet. The advantages of this construction are: • This design can accommodate a higher sulfur content in the fuel as compared to that normally acceptable to other manufacturers. • Heat release rate for the Dunham-Bush Absorption Chiller is 100,000 Btu/hr (29.3 kW) as compared to heat flux of 150,000 Btu/hr (41.0 kW) normally used by other manufacturers. A bigger furnace with lower heatflux reduces the depletion of corrosion inhibitor at high temperatures. • Access is provided to tubes for cleaning. • Flue gas pressure drop is maximum 3.15” H 2O (80 mm kPa) and the stack temperature is limited to around 392°F. • Reliable burner is used. • Large diameter tubes mean less soot deposition, even when heavier fuels are used. • Plain tubes without any spirals/turbulators mean less cleaning frequency even though it increases the size of the high temperature generator. Plain tubes also ensure that soot deposition is limited and thus problems like increased back-pressure, improper combustion, burner backfiring and in some cases even furnace collapse are eliminated. Burner The UL listed burner is supplied along with the chiller/ heater unit, capable of firing on one of the following fuels: a. Natural gas b. No. 2 fuel oil The burner supplied meets all major insurance, military and local codes. The burner is provided with a burner mounted control panel and is provided with necessary controls and stand alone safeties to provide safe and efficient working. 4 With a wide and established network of service centers throughout the country, the Dunham-Bush Absorption Chiller has an added advantage of being the only chiller and burner combination supplied from one manufacturer. The burner control panel is designed to interface directly with the microcomputer based chiller/heater control panel, to provide integrated burner firing control for the chiller/heater operation. FEATURES, SPECIFICATIONS AND BENEFITS (CONT.) ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ Upper Shell Assembly Condenser and low temperature generator The low temperature generator and condenser sections are housed in a common fabricated carbon steel shell, but with separate compartments for each section. The condenser and low temperature generator are separated by a partition plate fitted with stainless steel (SS-430) eliminators. The Dunham-Bush Absorption Chiller uses plain DLP (Deoxidized Low Phosphorous) copper tubes in the condenser section. The condenser has marine type hinged water headers, with side exit nozzles for ease of maintenance. The tubes of the low temperature generator are low finned copper. Lower Shell Assembly Evaporator and absorber (side by side construction) The lower shell houses the evaporator and absorber sections, separated by eliminators of SS-430, to prevent any liquid carryover. The Absorption Chiller uses plain DLP (Deoxidized Low Phosphorous) copper tubes in the evaporator and absorber sections. All the tubes are subjected to hydrostatic pressure and eddy current tests. The advantage of specifically using the more expensive DLP copper, with phosphorous content of less than 0.005 ppm, instead of the DHP grade tubes used in competitive machines is: Phosphorous content of higher than 0.005 ppm in the tubes of absorption machines results in “stress corrosion cracking”. At a microscopic level, stress corrosion cracking takes place at grain boundaries by the attack of a salt (e.g. lithium bromide) on the grain boundary. The absorber has marine type hinged water headers, with side exit nozzles for ease of opening during maintenance. The evaporator has headers with side exit nozzles. The advantage of using these headers is that normally the water piping need not be removed/ cut before the headers can be opened for tube cleaning and other maintenance activities. Heat Exchangers There are two heat exchangers - low temperature and high temperature heat exchanger. Both the heat exchangers are shell and tube type, designed for maximum heat exchange between the two circulating streams of LiBr. The tube material for low temperature heat exchanger is spiral copper and for high temperature heat exchanger is spiral cupro-nickel (90:10). Overflow Pipe (Auto Decrystalization Line) An overflow pipe is provided connecting the shell side of the low temperature generator to the absorber and bypassing the heat exchanger. The blockage of the strong solution line from the low temperature generator to the absorber leads to the accumulation of concentrated LiBr in the low temperature generator. This causes the solution level to rise in the low temperature generator, and the overflow of hot concentrated LiBr from the low temperature generator to the absorber directly begins. The heated weak solution warms up the crystallized solution on the shell side of the heat exchanger and hence melts the crystals. Canned Motor Pumps The Dunham-Bush Absorption Chiller uses only one absorbent and one refrigerant pump, thus minimizing the electrical consumption and reducing the maintenance, as these pumps are the only moving parts in an absorption chiller. These pumps are low net positive section head pumps and are self lubricating type. These canned motor pumps are cooled by the fluids they handle. The canning of the stator eliminates any chances of shorting. Both the pumps have separate motors and hence are independent of each other. The absorbent pump has both the over-current and high temperature protection to prevent motor burnout. 5 FEATURES, SPECIFICATIONS AND BENEFITS (CONT.) These canned motor pumps are provided with an inbuilt bearing monitoring terminal, which enables the condition of the pump bearings (TRG reading) to be evaluated for wear, externally, without stopping the chiller. ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ Further to facilitate the pump maintenance and repair without breaking the chiller vacuum, specially fabricated and leak tight isolation valves are provided at the suction and discharge ends for both pumps. This drastically reduces the downtime. Gravity Feed Trays The refrigerant from the condenser is not directly sprayed over the chilled water tube bundle. The water (refrigerant) from the condenser is first simply allowed to fall into the evaporator section alongside the shell. This water flashes and self cools itself to approximately 39°F (3.9°C), and collects at the bottom of the evaporator from where the refrigerant pump pumps it to the top of the feed trays. The Dunham-Bush Absorption Chillers have gravity feed trays for the spray of refrigerant in the evaporator and LiBr in the absorber section. These feed trays are manufactured with utmost precision and have perforations perfectly aligned with and running along the entire length of the tubes. Refrigerant and the LiBr droplets fall on the center of each tube ensuring maximum area coverage and hence maximum heat transfer in the respective section. Purge Pump, Purge Storage Tank And Purging Mechanism The purging unit consists of a factory mounted and tested electrical motor driven purge pump, storage tank and all the necessary piping and valves. Any non-condensable gas, like hydrogen and oxygen, generated due to the chemical reaction inside the chiller, moves toward the low pressure lower shell. These gases are automatically purged to the purge tank thereby maintaining the vacuum inside the chiller. The purge tank is a double walled cylinder with the outer cylinder connected to the absorber shell. A tapping from the absorbent pump running through the center of the inner cylinder sprays the LiBr through a nozzle. The high velocity generates a low pressure area, which sucks the non-condensables from the absorber section and bubbles through the LiBr solution to get trapped in the annular space between the two cylinders. The purge pump can then be operated to remove these stored gases from the purge tank. Solution Level Control The Dunham-Bush Absorption Chillers use highly reliable floatless level electrodes for controlling the level of the refrigerant in the evaporator and the level of lithium bromide solution in the high temperature generator and also to prevent the pumps from cavitation. These floatless level electrodes ensure that proper signals are transmitted to the refrigerant and absorbent pumps for starting/ stopping. The use of float valves for level control is avoided. Corrosion Inhibitor A corrosion inhibitor is added to the lithium bromide solution to minimize the possibility of any corrosion occurring in the absorption machine. The Absorption Chillers use lithium molybdate as the inhibitor. Lithium molybdate has excellent corrosion inhibition properties. The use of lithium nitrate is avoided as it desiccates at high temperatures, and therefore will not protect the absorption machine. Lithium intrate is also a substance controlled by the EPA. Sight Glasses And Service Valves The Dunham-Bush Absorption Chiller is provided with an optimum number of sight glasses and service valves for easy diagnosis, user-friendly operation and trouble-shooting. The number of sight glasses and service valves is kept to a minimum to reduce the 6 number of potential leakage points. The sight glasses are provided at the evaporator absorber shell and high temperature generator to monitor the refrigerant and solution levels. FEATURES, SPECIFICATIONS AND BENEFITS (CONT.) ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ Other Features • The unit is charged with a positive charge of • The crossover piping from the absorber to the nitrogen gas, to avoid any ingress of air inside the unit during shipping. Shipment of chiller under vacuum is not recommended. condenser is a standard feature of the DunhamBush Absorption Chiller. This feature saves the installing contractor both labor and material. • The Dunham-Bush Absorption Chiller is provided with a factory-mounted, wired and tested microcomputer-based control panel. Optional Features • On-line standby canned motor pumps • Three piece shipment On-line standby absorbent and refrigerant pumps can be offered for extremely critical operations where continuous operation is required. The Dunham-Bush Absorption Chiller can be shipped in three sections, comprising of lower shell assembly, upper shell assembly and high temperature generator, for convenience of rigging the chiller inside the existing building structure. • On-line bearing monitoring for canned motor pumps As a special option Dunham-Bush can provide a TRG meter for on-line bearing monitoring of the pumps. By continuously measuring the bearing clearance, through eddy currents, the TRG reading proactively lets the user know the condition of the bearings at any given instant. • Special tube material for evaporator/ absorber/condenser The selection of tube material is done purely on the basis of the water quality available. Dunham-Bush can offer the following special tube material depending on the available water quality: Cupro-nickel (90:10) Cupro-nickel (70:30) SS-316 L Titanium • Cooling water flow switch As an optional feature, paddle type flow switch is available for the absorber- condenser water circuit. The chilled water flow switch is a standard supply. • Inverter drive for absorbent pump A microprocessor-based inverter drive can be offered on the Dunham-Bush Absorption Chiller. The inverter drive suitably varies the flow of the dilute solution from the absorber to the high temperature generator, thus limiting the input steam to the generator. This assists the chiller to obtain superior part load performance. Double Effect Direct Fired 7 SELECTION DATA & TECHNICAL SPECIFICATIONS ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ Selection Data: Double Effect Gas Fired Absorption Chiller All double effect gas/oil fired chillers are rated for the following standard parameters: Chilled water temperature in / out Cooling water temperature in / out Chilled water / cooling water fouling factors Minimum gas pressure at the inlet of the gas train Maximum working pressure in the water system Calorific value of natural gas : : : : : : 54 / 44°F 85 / 95.4°F 0.00025 ft2-hr-°F/Btu .66 ft H2O 113.8 psi 1084.4 Btu/ft3 (12.2 / 6.7°C) (29.4 / 35.2°C) (0.000044 m2- /kW) (2.0 kPa) (784.5 kPa) (9650 Kcal/Nm3) Burner is supplied with the chiller. For conditions other than mentioned here, please contact the nearest Dunham-Bush Office / Sales Representative Technical Specification Sheet Gas Fired Absorption Chiller Model: WCGA 100 120 150 180 210 240 280 320 93 112 140 167 195 223 260 298 kW 327.4 394.2 492.8 587.8 686.4 785.0 915.2 1049.0 gpm 224.8 271 338.8 403.9 471.7 539.4 629.2 720.7 L/S 14.2 17.1 21.4 25.5 29.8 34.0 39.7 45.5 Ft H 2O 16.1 18 17.1 16.4 18.4 18.7 24.3 24 kPa 48.0 53.9 51.0 49.0 54.9 55.9 72.5 71.5 4 4 4 4 5 5 5 6 102 102 102 102 127 127 127 152 6 6 4 4 4 4 4 4 gpm 409.2 492.8 616 739.2 862.4 985.6 1148.4 L/S 25.8 31.1 38.9 46.6 54.4 62.2 72.4 82.7 Ft H 2O 12.5 13.1 17.7 20.3 16.7 18.7 26.2 24 kPa 37.2 39.2 52.9 60.8 50 55.9 78.4 71.5 5 5 5 5 6 6 6 8 127 127 127 127 152 152 152 203 No. of passes (Absorber) 3 3 2 2 2 2 2 2 No. of passes (Condenser) 1 1 1 1 1 1 1 1 1977.4 2330.5 2813 3072 56 66 74 87 Chilled water circuit Capacity Flow rate Pressure drop Connection diameter Tons in mm No. of passes (Evaporator) Cooling water circuit Flow rate Pressure drop Connection diameter in mm 1311.2 Fuel circuit Gas Consumption 8 ft3/hr 1095 m 3/hr 31 1341.7 1624.3 38 46 3460.4 98 SELECTION DATA & TECHNICAL SPECIFICATIONS (CONT.) Model: WCGA ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ 360 400 450 500 550 620 690 770 335 372 419 465 512 577 642 716 1636.8 1802.2 2031.0 2259.8 2520.3 1395.7 1553.2 1734.5 Chilled water circuit Capacity Tons kW Flow rate Pressure drop Connection diameter 1179.2 1309.4 1474.9 gpm 810.5 899.8 1013.8 1124.2 1238.6 L/S 51.1 56.8 64.0 70.9 78.1 88.1 98.0 109.4 Ft H2O 23.3 24.9 24 23.3 27.9 28.9 21.3 23.3 kPa 69.6 74.5 71.5 69.2 83.3 86.2 63.7 69.6 6 6 8 8 10 10 10 10 152 152 203 203 254 254 254 254 4 4 4 4 4 4 3 3 2046 2186.8 2464 2741.2 3058 in mm No. of passes (Evaporator) Cooling water circuit Flow rate gpm 1474.0 1636.8 1843.6 L/S 93.0 103.3 116.3 129.1 138 155.4 172.9 192.9 Ft H2O 21.3 23 20.3 20.3 24 25.3 34.8 36.4 kPa 63.7 68.6 60.8 60.8 71.5 75.5 103.9 108.8 8 8 10 10 12 12 12 12 203 203 254 254 305 305 305 305 No. of passes (Absorber) 2 2 2 2 2 2 2 2 No. of passes (Condenser) 1 1 1 1 1 1 1 1 5437.1 5826.2 6744.2 7521 155 165 191 213 Pressure drop Connection diameter in mm Fuel circuit Gas Consumption ft3/hr 3707.6 m 3/hr 105 4237.2 4943.4 120 140 8227.2 233 9 APPLICATION INFORMATION ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ Location And Space Requirements The Dunham-Bush Absorption Chillers have negligible noise and vibration and may generally be located at any level in a building. The chiller plant room should be sufficiently ventilated to provide enough circulation of air and also to ensure that the burner gets the required quantity of air for efficient combustion. The unit should be placed on a level foundation. Sufficient space at either end of the unit should be provided for tube cleaning/removal. Also sufficient clearances should be provided on the remaining sides of the unit for the necessary access and maintenance. Refer to the physical dimensional table for space and clearance requirements. Since water is the refrigerant, the unit must be located where the ambient temperature does not fall below the freezing point. Water Circuits Water Piping: All chilled water and cooling water piping should be designed and installed in accordance with the accepted piping practice. The piping should be adequately supported to avoid any strain on the chiller components. All water piping should be thoroughly flushed clean before connecting to the unit. A suitably sized expansion tank should be provided in the chilled water line. Pressure gages should be installed at the inlet and outlet water lines of the unit. Air vents should be located at all high points in the water piping system. All drain points should be located at low points to facilitate complete system drainage. Both the chilled and cooling water pumps should be located to discharge a positive pressure and required flow through the unit. Shut-off valves should be provided to allow unit isolation during maintenance. The chilled water piping should be insulated to minimize heat gain, and to prevent condensation of moisture. Water Quality: Proper quality of water should be monitored and maintained to ensure long life, and trouble free and efficient operation of the entire cooling system. Impurities in water can cause scale formation, thereby causing a reduction in heat transfer and affecting the performance of the unit. The impurities can also be a potential for mechanical damage to the unit and the system. The use of properly sized water strainers and water treatment may be necessary to maintain the required water quality. It is desirable to set the appropriate water quality control values under the guidance of a water processing specialist who will periodically control it. Suggested Guide Of Cooling And Chilled Water For The Dunham-bush Absorption Chiller Items pH at 77°F (25°C) Electrical conductivity at 77°F(25°C) M alkalinity Total hardness Chloride ion Sulfuric acid ion Total iron Sulfur ion Ammonium ion Silica ion (SiO2) Free carbonic acid Unit Micro S/cm ppm ppm (CaCO3) ppm (Cl) ppm (SO4) ppm (Fe) ppm (S) ppm (NH4) ppm SiO2 ppm (HCO3) Cooling Water One-pass or Make-up Water circulating 6.5~8.0 6.5~8.0 Chilled Water 800 or less 100 or less 200 or less 200 or less 200 or less 1.0 or less Not detected 1.0 or less 50 or less - 500 or less 100 or less 100 or less 100 or less 100 or less 1.0 or less Not detected 0.5 or less 50 or less 0 200 or less 50 or less 50 or less 50 or less 50 or less 0.3 Not detected 0.2 or less 30 or less - Circulating 6.5~8.0 If such water conditions exist which cannot be corrected by proper water treatment, it may be necessary to provide a larger fouling/scaling allowance and/or choose special tube material suitable for the water quality. 10 APPLICATION INFORMATION (CONT.) ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ Fuel And Exhaust Piping The Dunham-Bush Absorption Chiller utilizes natural gas or oil no. 2 as the fuel source. Depending on the requirement, the chiller is equipped with a suitable burner, capable of firing either one, or both fuels. The dual-fuel firing capability gives the user more flexibility. The fuel and the exhaust piping should be designed and installed in accordance with the standard engineering practice and conforming to the local codes. The site erected exhaust gas duct should have a removable section above the unit, to facilitate the duct and the machine maintenance. For multiple units, it is important to provide separate ducts from the unit to the main chimney (stack) and also each duct should be provided with a suitable damper. This damper should be shut-off for the unit, while the unit is not in operation. Cooling And Heating Modes The Dunham-Bush Direct Fired Absorption Chiller can be utilized to meet both heating and cooling requirements of a building. For hot water temperatures below 140°F (60°C), a two-pipe system is utilized. Thus the same set of piping, pumps, etc. can be used for either cooling or heating purposes. If the required temperature of hot water is higher than 140°F (60°C), then a four-pipe system can be utilized, by the addition of an optional heat exchanger on the unit. This feature assists the owner to eliminate any additional heating equipment, and also saves the plant room space and reduces the maintenance. An optional heat exchanger is also added onto the unit if the requirement is for simultaneous heating and cooling. 11 PHYSICAL DIMENSIONS ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ Direct Oil/Gas Fired Absorption Chiller Model: WCGA Length: Width: Height: Clearance for tube cleaning: 100 120 150 180 210 240 280 320 in 148.2 144.3 157.1 149.0 162.0 169.5 172.4 175.2 mm 3765 3665 3990 3785 4115 4305 4380 4450 in 100.8 103.1 106.3 109.3 110.0 110.0 113.0 119.5 mm 2560 2620 2700 2775 2795 2795 2870 3035 in 93.1 94.7 94.7 95.5 104.8 99.3 109.1 109.1 mm 2365 2405 2405 2425 2661 2521 2772 2772 in 94.5 94.5 133.9 133.9 133.9 133.9 161.4 161.4 mm 2400 2400 3400 3400 3400 3400 4100 4100 Max shipping weight: lb 15212 16314 19401 24692 26676 29983 36376 kg 6900 7400 8800 9300 11200 12100 13600 16500 Total shipping weight: lb 15212 16314 19401 20503 24692 26676 29983 36376 A Shipping method ONE SECTION 20503 kg 6900 7400 8800 9300 11200 12100 13600 16500 lb 16094 17196 20503 21605 26235 28439 31967 38581 kg 7300 7800 9300 9800 11900 12900 14500 17500 360 400 450 500 550 620 690 770 in 175.2 181.3 175.2 187.2 228.7 228.7 277.2 277.2 mm 4450 4605 4450 4755 5810 5810 7040 7040 in 121.5 121.5 129.3 129.3 132.7 133.9 133.9 133.9 mm 3085 3085 3285 3285 3370 3400 3400 3400 in 113.0 113.0 116.4 120.7 120.7 123.9 128.2 130.4 mm 2870 2870 2956 3067 3067 3147 3257 3312 in 161.4 161.4 161.4 161.4 209.4 209.4 258.3 258.3 mm 4100 4100 4100 4100 5320 5320 6560 6560 Max shipping weight: lb 38360 47085 46738 48501 60627 65036 74736 78704 kg 17400 18500 21200 22000 27500 29500 33900 35700 Total shipping weight: lb 38360 47085 46738 48501 60627 65036 74736 78704 kg 17400 18500 21200 22000 27500 29500 33900 35700 Operating weight: lb 40785 43431 49824 51808 64154 68784 78925 83334 kg 18500 19700 22600 23500 29100 31200 35800 37800 Operating weight: Model: WCGA Length: Width: Height: Clearance for tube cleaning: A ONE SECTION HEIGHT Shipping Method CLE AR AN CE FOR TU B E R EMO VA L A A 12 LE NG TH WID TH TYPICAL PIPING SCHEMATIC ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ 13 ELECTRICAL WIRING DRAWINGS ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ WCGACTAA.DWG 14 ELECTRICAL WIRING DRAWINGS (CONT.) 8 49 ~ REFRIGERANT LEVEL 50 ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ~ (1DI/OB) 2 2LS 51 9 3 1 10 52 5 53 6 7 54 56 RE1 RE2 57 13H 13DI 13N 85 84 83 55 32 4 RE3 4SN 58 59 4C 4CP 9C 9CP 4NO 33 2CR 9NO ALARM OUTPUT 2LT R 60 SEE NOTE 11 61 100 62 3CR 5SN 101 5CP 6C 5NO 34 6CP 6NO 35 7C 7CP 7NO 8C 8CP 10C 10CP 102 64 2CR 104 66 4CR SEE LINE 48 105 COOLING WATER CONTROL 19 CONTROL POWER 36 68 69 40 70 71 HIGH TEMP GENERATOR PRESSURE SWITCH 42 RIBBON CABLE 72 1PS TO DIGITAL I/O BOARD 73 J3 75 MICROCOMPUTER (MCB) J2 76 J5 DISPLAY J6 77 RS485 J7 79 82 PRESS HELP KEY FOR BASIC OPERATION INSTRUCTIONS. 83 TO DISPLAY CONTROL VALUE 87 89 89 NAME TLW °F PWR LOSS CWR MAX FREEZE SET POINTS A OPEN 39 °F 730 mmHG 2TAS 1PS 3TS COOLING WATER OUTLET TEMP RED 59 CLOSE 760 mmHG AI BOARD #1 (1AIB) BLK 52 WHT 51 RED 59 BLK 53 WHT 51 RED 59 BLK 54 WHT 51 92 GND NAME SET POINTS A TLW °C TLW PWR LOSS CWR MAX FREEZE OPEN 39.0 °F (3.9 °C) 730mmHG 1 4AI 4RES 250 55 (4TB) 2 BLK 1 81 5 AI 8RES 250 2 BLK 0.0 0.0 4.0°C CLOSE (+) 1ZD 0-5VDC (-) GND CHILLED WATER RESET OPTIONAL GND 93 SEE NOTE 8 94 RIBBON CABLE 1SC 98 99 100 101 8 11 ANALOG OUTPUT BOARD (AOB) AO1 12VAC AO3 GND 12 102 760mmHG STACK TEMP 3 63 97 B 5TS GND 6AI 51 1 61 2 62 GND (3TB) HIGH TEMP GENERATOR TEMP 3 5TSI (3TB) 50 WHT GND +5 4TS SH GND 2AI 3AI 1 2 +5 96 FURNISHED NOT FURNISHED 4TSI (3TB) 50 WHT 1AI 95 METRIC DISPLAY OPTION 16N 7CPR +5 91 0.0 0.0 39.2 °F 14N 15N 6CPR GND 90 B TLW 16DI TO BURNER CONTROL 2 2TS COOLING WATER INLET TEMP FOR MORE INFORMATION SEE OWNERS MANUAL. 88 15DI 41 RIBBON CABLE 1TS LEAVING CHILLER TEMP 1) PRESS MENU KEY TO DISPLAY MENU ITEM. 2) USE UP OR DOWN ARROW TO MOVE TO DESIRED MENU ITEM. 3) PRESS ENTER KEY TO SELECT DESIRED MENU ITEM. 4) USE UP OR DOWN ARROW TO DISPLAY DESIRED CONTROL VALUE. 86 16H 10NO MACHINE ON/OFF 12VAC INSTRUCTIONS 85 44 12 KEYBOARD 84 15H RS232 80 81 43 8N0 37 5CPR BURNER FAULT 11 78 14DI 14H BURNER ON 8 74 1PS 4CR 19 COOLING WATER CONTROL 67 2TAS CHILLED WATER INTERLOCK 6SN 103 ALARM CONTACTS 65 1 2 3 4 3CR CHILLED WATER PUMP CONTACTS 63 1 2 3 4 5C JUMPER ON ADDRESS #4 103 67 (+) 0-10VDC 68 (+) REMOTE TLW SIGNAL 69 (-) 1 4 7 2 115VAC 9 (+) 4-20mA 6 10 (-) TO BURNER CONTROL GROUND SH 104 105 106 107 108 NOTES 1- FUSES SHALL BE TIME DELAY TYPE. 2- ALL FIELD WIRING SHALL COMPLY WITH LOCAL, STATE AND NATIONAL CODES. 3- USE COPPER CONDUCTORS ONLY. CONTROL WIRING 14AWG WITH MAX. 15A OVERCURRENT PROTECTION. USE TERMINAL 2 FOR NEUTRAL CONNECTIONS. 4- DISCONNECT MEANS AND BRANCH CIRCUIT PROTECTION SHALL BE PROVIDED BY INSTALLER IF NOT SUPPLIED. 109 110 111 112 113 7- CUSTOMER CONTROL CONTACTS MAY BE WIRED BETWEEN TERMINALS 16&17. 8- IF 0-5 VDC CWR IS USED, SET SETPOINT 3B TO RESET DESIRED AT +5VDC INPUT. CAUTION: DO NOT SUPPLY OVER 5.0VDC TO ANALOG INPUT. 10- SHIELDED CABLE IS RECOMMENDED FOR CUSTOMER SUPPLIED CONTACT WIRING. GROUND ON SUBPANEL. 11- CONTACT RATING IS 10A AT 125 VAC AND 5A AT 250 VAC (1/2 HP). WCGACTBA.DWG 15 ABSORBENT PUMP #2 OVERLOAD 6L2 6L3 2L1 2L2 2L3 6CR 90 21 91 SEE AFD OPTION 118 120 11CP 4H 11NO 2 20DI 4N 7SN 93 92 SEE AFD OPTION ABSORBENT PUMP #2 CONTACTOR (13) 4M 1M-2 6LT W (#4 ON 2DIOB) REFRIGERANT PUMP #2 OVERLOAD 5MOL 26 5MOL 121 ~ ~ 119 5M 4M 1M 11C 3N 94 ~ ~ 6L1 117 ~ ~ 116 HMT 1TAS-2 19DI (#3 ON 2DIOB) ~ ~ FURNISHED NOT FURNISHED 3H ~ ~ DUAL ABSORBENT AND REFRIGERANT PUMP OPTION ~ ~ 115 ~ 114 ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ~ ELECTRICAL WIRING DRAWINGS (CONT.) 12CP 12C 12NO 8SN 96 95 122 REFRIGERANT PUMP #2 CONTACTOR (14) 5M 2M-2 4-MTR ABSORBENT PUMP #2 5-MTR REFRIGERANT PUMP #2 7LT W ~ 124 ~ 1-MTR ABSORBENT PUMP #1 123 125 TEMPERATURE SENSOR OPTION 126 FURNISHED NOT FURNISHED 127 128 129 8TSI NOT FURNISHED 6TS RS232 ENTERING CHILLER WATER TEMP J6 131 132 MODEM 134 GND LINE 136 BLK 60 WHT 51 GND 8TS LOW TEMP HEAT EXCHANGER TEMP 3 SH (4TB) GND 2 BLK 9TSI (3TB) 50 WHT 1 1 9TS 2 3 2 BLK SH POWER OUTLET 137 57 2 LOW TEMP GENERATOR TEMP WHT 1 2 11AI (#3) 6RES 250 9AI (#1) WHT 50 (3TB) 1 1 +5 7TSI 1 7TS 2 BLK 59 TELEPHONE 133 7 RED (3TB) 50 WHT AI BOARD #2 (2AIB) FURNISHED 130 135 RIBBON CABLE TO MCB MODEM OPTION 10AI (#2) 2RES 250 56 (4TB) 12AI (#4) 7RES 250 2 BLK CONDENSED REFRIGERANT TEMP 3 SH (4TB) GND GND 138 58 139 ADJUSTABLE FREQUENCY DRIVE (AFD) OPTION 141 FURNISHED 142 NOT FURNISHED 24 143 1L1 144 REMOVE 1M & 1MOL 145 146 R 1L2 1AFD S 1L3 T 2 5CR REMOVE 1M UNLESS DUAL PUMP OPTION IS SUPPLIED U V W 1L1 6L1 ABSORBENT PUMP 6L2 REMOVE 1M & 1MOL 6L3 1AFD R 1L2 1L3 T 71 149 TB2-6 TB2-7 8 TB2-8 150 72 151 152 TB2-11 5CR ANALOG OUTPUT BOARD ~ 155 AO2 156 GND ~ 154 TB2-10 73 0-10VDC 74 157 TB2-2 1H 13 SEE LINE 13 TB2-9 8 66 NOTE: TO RESET FAULT, REMOVE POWER FROM DRIVE (OPEN 1CB) 22 TB2-3 6CR 70 TB2-6 71 TB2-7 TB2-8 FAULT OUTPUT 6CR 2 TB2-12 153 18AWG 5CR 23 72 TB2-11 8 TB2-9 FAULT OUTPUT 6CR 2 TB2-12 ~ 70 6L3 W ANALOG OUTPUT BOARD AO2 GND 66 TB2-10 ~ 5CR ABSORBENT PUMP 6L2 V GND ~ 18AWG 148 6L1 U S GND 147 ~ 140 73 NOTE: TO RESET FAULT, REMOVE POWER FROM DRIVE (OPEN 1CB) TB2-2 0-10VDC TB2-3 74 SEE LINE 28 158 159 LEGEND 160 AE AFD 161 DOOR LATCH SOLENOID OPTION 165 AI C CB CO CP CPR CR CTR CWDP 166 CWFS 162 FURNISHED NOT FURNISHED 163 164 167 1 1SOL 2 CWP CWR DI FU GND I/O LS LT M MTR NC NO OL ABSORBENT ELECTRODE ADJUSTABLE FREQUENCY DRIVE ANALOG INPUT SHORTING CONTACTOR CIRCUIT BREAKER CONVENIENCE OUTLET CONTROL POINT CAPACITOR CONTROL RELAY CONTACTOR CHILLED WATER DIFF. PRESSURE CHILLED WATER FLOW SWITCH CHILLED WATER PUMP CHILLED WATER RESET DIGITAL INPUT FUSE GROUND INPUT/OUTPUT LEVEL SENSOR LIGHT CONTACTOR MOTOR NORMALLY CLOSED NORMALLY OPEN OVERLOAD PWR RE RES RLY S SC SCR SH SN SOL T TAS TB TLW TR TS TSI UVR VM ZD * [] POWER SUPPLY REFRIGERANT ELECTRODE RESISTOR RELAY SWITCH SIGNAL CONDITIONER SPEED CONTROL SHIELD SNUBBER SOLENOID TRANSFORMER THERMOSTAT TERMINAL BLOCK TEMP LEAVING WATER TIMER TEMP. SENSOR TEMP SENSOR INTERFACE UNDERVOLTAGE RELAY VOLTMETER ZENER DIODE MANUAL RESET FACTORY TERMINAL FIELD WIRING FIELD SUPPLIED STANDARD COMPONENT 8 2 ABSORBENT LOW LEVEL 3LS 3 10 11 5 DIGITAL I/O BOARD #2 (2 D I/O B) 9 45 1H 17DI (#1) 1N 4 GND 82 86 AE5 AE3 ABSORBENT LOW-LOW LEVEL 4LS 3 9 1 10 5 46 2H 18DI (#2) 2N 4 12VAC 88 82 AE4 JUMPER ON ADDRESS #3 AE5 RIBBON CABLE TO MICROCOMPUTER J2 WCGACTCA.DWG 16 11 12 ENGINEERING SPECIFICATIONS ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ ○ Provide ................no.(s) factory assembled, leak tested Natural Gas/Fuel oil no.2 Fired Double Effect DunhamBush Absorption Chiller. Each chiller shall have a capacity of ................. TR, cooling ................. gpm of chilled water from .................ºF to .................. ºF, when supplied with condenser water at a temperature of ............ºF. The unit selection shall be based upon a fouling factor of ................ for the evaporator and ................ for the condenser/absorber circuit. Natural gas/fuel oil no. 2 at a pressure of ................. psi shall be provided before the inlet of burner. The supply power characteristics shall be ................Volts, .............Phase, ..............Hz. The chiller shall be of multi-shell design consisting of lower shell assembly, upper shell assembly, high temperature generator mounted with a suitably sized burner, heat exchangers, absorbent pump, refrigerant pump, purge pump, purge unit and inter-connecting piping & accessories. The unit shall operate on Water-Lithium Bromide cycle. All tubes in the condenser shall be individually replaceable from either end of the chiller. The condenser shall have marine type hinged water headers with side nozzles for easy opening and access to the tube bundle. All the tubes shall be fitted in the respective tube sheets expanded into grooved holes. 4. High temperature generator The high temperature generator shall have straight and plain, circular carbon steel boiler quality tubes, adequately sized and 0.144" wall thickness. All the tubes shall be fitted in the respective tube sheets duly expanded for a tight fit and welded. Inside welding of the tubes shall be avoided to facilitate the removal of tubes at the site, if required. A suitably sized burner for firing natural gas/fuel oil no. 2 shall be mounted on the high temperature generator. Burner: The chiller unit shall be supplied with a UL listed burner, capable of firing on one or both of the following fuels: 1. Mechanical description All the heat exchangers shall be of shell and tube type welded construction. The material of shell, tube sheets and water boxes shall be as per SA 515/516 Gr 70/60 or IS 2002 Gr 2 or IS 2062. a. Natural gas b. No. 2 fuel oil The burner shall be provided with a burner mounted control panel, necessary controls and stand alone safeties to provide safe and efficient working. 2. Lower shell assembly 5. Heat exchangers The evaporator and absorber sections shall be housed in a common fabricated carbon steel shell, but with separate compartments for each section. The evaporator and absorber shall be separated by rows of stainless steel (SS-430) eliminators. Material for evaporator and absorber tubes shall be plain DLP (Deoxidized Low Phosphorous) grade copper. All the tubes shall be fitted in the respective tube sheets duly expanded for a tight fit. All the tubes shall be individually replaceable from either end of the chiller. The absorber shall have marine type hinged water headers with side nozzles for easy opening and access to the tube bundle. The evaporator water headers shall have side nozzles for easy opening and access to tube bundle. 3. Upper shell assembly The low temperature generator and condenser sections shall be housed in a common fabricated carbon steel shell, but with separate compartments for each section. The condenser and low temperature generator shall be separated by a partition plate fitted with stainless steel (SS-430) eliminators. Material for condenser tubes shall be plain DLP (Deoxidized Low Phosphorous) grade copper. The tubes of the low temperature generator shall be low finned copper. The heat exchangers shall be of shell and tube type welded construction. There shall be three heat exchangers - low temperature, high temperature and drain heat exchanger. The tube material for low temperature heat exchanger shall be spiral copper, for high temperature heat exchanger shall be spiral cupronickel (90:10) and for drain heat exchanger (heat reclaimer) shall be stainless steel (SS-430) titanium stabilized, for maximum heat transfer between the circulating fluids. 6. Refrigerant and absorbent pump The unit shall be provided with two motor-pump assemblies - a refrigerant pump for even distribution of refrigerant on the evaporator tube bundle through gravity feed arrangement and one absorbent pump to deliver the dilute solution to the generator. Both the pumps shall be canned motor, self lubricating type and shall be cooled by the fluid being pumped. The absorbent pump shall be provided with both overcurrent and high temperature protection safeties to prevent the motor from burnout. Both the pumps shall be provided with isolating valves at both the suction and discharge ends for ease of removal of the pumps for maintenance, without breaking the vacuum inside 17 the chiller. Both the pumps shall have a external bearing monitoring system to enable the user to check the condition of the bearing, without dismantling the pumps. 7. Purge recovery unit The purge unit shall be sized to automatically and continuously remove the non-condensable gases from the shell to the storage tank, when the chiller is in operation. The purge unit shall be provided with a factory mounted and tested electrical motor driven purge pump to remove these gases from the storage tank. The unit shall be provided with a solenoid valve or a non-return valve to avoid air from entering the absorption chiller, in case the power fails while the purge pump is in operation. 8. Gravity feed trays The chiller shall be provided with stainless steel (SS430) gravity-feed trays for even distribution of refrigerant and absorbent over the respective tube bundles. The gravity feed trays shall be located just above the top of the respective tube bundle and shall have perforations perfectly aligned with and running along the entire length of the tube bundle. The gravity feed arrangement enhances the machine life by eliminating the chances of erosion of spraying nozzles and disruption of flow due to clogging of nozzles with impurities. 12. Liquids The absorption chiller shall operate on water-lithium bromide cycle. A suitable charge of both the refrigerant and a suitably inhibited lithium bromide shall be supplied by the manufacturer. The inhibitor used shall be environment friendly and shall not be chromate or nitrate based. Also a suitable quantity of heat transfer additive shall be charged in the unit. 13. Controls and safeties Each unit shall be equipped with a factory mounted and pre-wired control system. The chiller shall be equipped with two panels - a combined power and control center, and a burner control panel. The burner control panel shall be designed to interface directly with the microcomputer-based chiller control panel, to provide integrated burner firing control for the chiller operation. The control system shall provide for modulation of the burner based on the desired chilled water leaving temperature, control and monitoring of absorbent, refrigerant and purge pumps and control interlocks for chilled water and cooling water pumps. The control equipment shall be enclosed in a NEMA 1 type sheet metal enclosure mounted on the chiller. The safety and control circuit shall consist of the following: • 9. Sight glasses and service valves The unit shall be provided with a minimum yet sufficient number of sight glasses and service valves for easy diagnosis, user-friendly operation and troubleshooting. The number of sight glasses and service valves shall be kept to a minimum to reduce the number of potential leakage points. The use of threaded type sight glasses shall be avoided. The sight glasses shall be provided at the following locations to monitor the refrigerant and solution levels: • • • • • • Evaporator shell, absorber shell and high temperature generator shell. • 10. Piping • The various sections of the chiller shall be interconnected by suitably sized seamless steel piping. All piping shall be of welded construction complete with necessary valves and fittings. The absorber to the condenser crossover piping shall be suitably welded by the supplier. • • • 11. Auto-decrystalization line The unit shall be provided with an overflow pipe connecting the low temperature generator to the absorber and bypassing the heat exchanger, to enable the hot solution to flow directly from the low temperature generator to the absorber and hence decrystalize the unit. 18 • • • Terminal blocks for control and power connections Microcomputer based control system Individual circuit breakers for each pump and the burner Ambient compensated overloads for all pumps Control transformer Level controller and electrodes for evaporator refrigerant level control and first stage generator (high temperature) solution level control. The use of a float valve for level controls shall be avoided. High motor temperature cutout for absorbent pump Interlock terminals for chilled and cooling water pumps On/off/remote selector switch for unit control Purge pump control switch Indicator lights for control power, absorbent pump, refrigerant pump, purge pump and alarm Temperature sensors and digital display for the following: Chilled water leaving temperature, cooling water entering and leaving temperature and first stage (high temperature) generator temperature Freeze protection thermostat Factory mounted flow switch & differential pressure switch for chilled water Burner control and monitoring Information display The computer shall have a simple keyboard accessed input system and shall be complete with a two line 80 character alphanumeric display. The input shall be accomplished through simple menu driven display screens, with on-line help available by pressing a help button at any time during operation. The information shall be in the English language with numeric data provided in English units. The following information shall be provided on the computer: • • • • • • • • Leaving chilled water temperature Entering and leaving cooling water temperatures First stage (high temperature) generator temperature Operating hours of the chiller Indication of refrigerant, solution and purge pump's manual/auto operation Burner firing rate (in %) Number of starts of the chiller Number of purge cycles (Cumulative) The computer shall be complete with all hardware and software necessary to enable remote monitoring of all data through the addition of only a simple, optional, phone modem and terminal. The microcomputer shall be complete with an RS232 “local” communications port and an RS485 long distance differential communications port. The microcomputer shall also accept a remote start and stop signal, and a 0 - 5 VDC chilled water temperature reset signal. The microcomputer shall be able to transmit all the operating, setpoint and shutdown information to a remote terminal. This transmission occurs as needed and can be printed. The microcomputer shall store a history data of the last eight safety shutdowns. Chilled water limit - If the leaving chilled water temperature reduces below the low setpoint value, the microcomputer shall shut off the refrigerant pump. The pump shall be restarted automatically when the chilled water temperature rises above the high setpoint value. Shutdown controls 1. Safety shutdown : The microcomputer shall be preprogrammed to shut down the unit when any one or more of the following conditions occur: • • • • • • • • • • • • Refrigerant or absorbent pump current overload High motor temperature cut-out for absorbent pump motor Burner alarm/failure High stack temperature Chilled water flow switch trip Chilled water differential pressure switch trip Freeze protection thermostat trip Low cooling water entering temperature First stage (high temperature) generator high temperature First stage (high temperature) generator high pressure Sensor failure monitoring Power failure (when “automatic restart after power failure” setting is not utilized) In case of safety shutdown controls, a manual operation to restart the unit is required. Whenever a safety shutdown occurs, the computer shall record the following information and store it in its memory: • Day and time of shutdown • Reason for shutdown 2. Cycling shutdown: Capacity control The computer shall automatically vary the burner firing rate in order to maintain the leaving chilled water setpoint for variable cooling loads. The following parameters shall be programmable directly from the keypad using a security access code, for safe operation: • • • • Chilled water leaving temperature in increments of 0.1°F Chilled water leaving temperature reset based on 0 - 5 VDC signal Package control based on 7 day weekly schedule with up to 8 holiday schedules Ramp-up of unit capacity on start-up Proactive controls for unit protection Cooling water limits - The microcomputer shall restrict the burner firing rate in case the cooling water entering temperature exceeds lower or upper limits. In case of a cycling shutdown, automatic restart of the unit occurs. The following conditions are included under the cycling shutdown condition: • Low leaving chilled water temperature • Power failure (when automatic restart setting is utilized) • Loss of condenser water flow (Optional) • Scheduling of unit operation set for shutdown 1. In addition to the standard temperatures, the Microcomputer can monitor the following temperatures: • Entering chilled water temperature • Condensed refrigerant temperature (at the U-tube) • Strong solution leaving temperature from the heat exchanger 2. Optional modem can be provided for remote monitoring of the unit with a terminal or personal computer. 19 3. Under voltage and phase sequence protection relay. 4. Unit disconnect switch with external handle. 5. Inverter drive for absorbent pump: A fully microprocessor-based inverter drive can be offered on the Dunham-Bush Absorption Chiller. The inverter drive suitably varies the flow of the dilute solution from the absorber to the high temperature generator, thus limiting the input energy to the generator and assisting in achieving superior part load performance. Specifications subject to change without notice. July 2000 101 Burgess Road, Harrisonburg, VA 22801 Phone: (540) 434-0711 Fax: (540) 434-4595 www.dunham-bush.com Printed in U.S.A. Form No. 6066A
* Your assessment is very important for improving the work of artificial intelligence, which forms the content of this project
advertisement