Product Data 6DNH 0% Energy Saving Model, Direct-Fired, Double Effect, Hermetic Absorption Liquid Chiller/Heater 50 to 650 minal Tons (57 to 580 kw) Copyright 009 Carrier China Operations 6DNH Carrier s 6DNH direct-fired, double effect, hermetic absorption liquid chiller/heater offers a viable alternative to traditional electric driven chillers. Fired by natural gas or. oil, the 6DNH reduces costly electricity bills and qualifies for utility rebates and incentives as a gas cooling product. The 6DNH can operate in the heating mode to provide hot water, thereby reducing the size of the required boiler or even eliminating the need for a boiler. no CFCs; environmentally friendly two-stage high efficiency design reduces energy costs fired by clean burning natural gas or. oil operates as a chiller or heater quiet. vibration-free operation few moving parts equates to high reliability Features/Benefits Direct-fired, double effect absorption provides efficient, economical water chilling or heating with minimal use of electricity. Cost-effective cooling and heating Alternative-energy chiller/heater The 6DNH offers an alternative for building owners who want to avoid the high operating costs associated with electric-driven chillers. Fired by natural gas or. oil, the Carrier 6DNH direct-fired, double effect, absorption chiller/heater not only reduces or eliminates electric demand, but also allows the owner to take advantage of gas cooling rebates and incentive programs offered by many utility companies. Several configurations of heating mode
operation provide hot water for a variety of applications. High-efficiency, double effect, Absorption cooling cycle The 6DNH design incorporates a hightemperature generator and a lowtemperature generator (double effect) tandard that provide stages of solution reconcentration and adds a flue gas heat exchanger and condensate heat exchanger to recover heat. The 6DNH use brazed plate heat exchanger to get high efficiency than 6DN, Carrier s efficiency. As a result of this high efficiency double-effect cycle, the 6DNH has lower operating costs than single-effect and standard doubleeffect machines. When using natural gas, full load cooling operation results in a COP (coefficient of performance) of at standard ARI (Air Conditioning and Refrigeration Institute) operating conditions. Superior part-load performance The 6DNH s standard concentration control system allows stable, part-load operation at cooling water temperatures as low as 60.8 F (6 C) without the need for a cooling tower bypass. For maximum efficiency, a variable frequency drive pump automatically maintains optimum solution flow to the high- and low-temperature generators at all operating conditions. This will result in improved part-load efficiency and eliminate the need for manual setup adjustments of the solution flow. The 6DNH has a continuous operating range from 00% to 0% capacity for gas fired series and 00%-30% for oil fired series based on minimum fire requirements for the burner. Operates in the heating mode for additional savings In the heating mode, the 6DNH can deliver hot water for space heating or other applications to reduce or eliminate dependency on existing or supplemental boilers. Operation in the heating mode can be done instead of cooling mode operation. When operated as a heater, hot water temperatures of 40 F (60 C) are standard and do not require additional components. In the heating mode, the evaporator is used as the heating bundle and the machine is configured as a - pipe system with the chilled water nozzles serving as hot water nozzles. Quick changeover from cooling to heating is accomplished by switching the positions of two hand valves, draining the absorber-condenser water circuit, and putting the machine into heating mode by selecting a heating mode operation from the control panel. Application versatility Ideal for new or retrofit applications Whether intended for replacement of existing chiller and/or boiler systems or for new construction purposes, the 6DNH is well suited to meet the needs of most cooling/heating applications for which a supply of natural gas or. oil is available. The 6DNH s 8 model sizes, spanning a capacity range of 50 to 650 tons, make the 6DNH directfired, double effect, absorption chiller/heater the ideal choice for comfort cooling and /or light industrial applications. Carrier s computerized performance ratings assist in the selection of the correct size machine to meet exact job requirements. Dependable operation, as well as low sound and vibration levels, ensures occupant comfort, even when the machine is installed on upper floors. Table of contents Combined use of absorption and electric-driven chillers Utilizing both absorption and electric chillers in a central plant offers the flexibility to base load one chiller, while using the other to handle peak load requirements. Hybrid chiller systems have proven to be an economical solution for many comfort cooling installations. In many geographical areas, operating the electric chiller as the base loaded machine, while using the absorption chiller during peak load conditions, reduces or avoids electric demand charges. Depending on utility rate structures, the 6DNH direct-fired absorption chiller/heater used in conjunction with an electric-driven chiller may be the most efficient and cost-effective combination available. Page Features/Benefits...-8 Model Number menclature.. Options and Accessories..9 Machine Components...9 Physical Data..0- Dimensions.. Performance Data 3-5 Application Data.....6-0 Typical Control Sequence -7 Guide Specifications...8-33 Model number nomenclature 6 DNH 08 Unit Size Direct-Fired Double Effect, High COP Absorption Chiller
Location and installation savings Ease of installation All 6DNH units are completely fabricated, assembled, and wired in the factory as single-piece units. Standard shipping configuration is either or piece, depending on size. Refer to the 6DNH Standard Shipping Configuration table below. 6DNH STANDARD SHIPPING CONFIGURATION UNIT SIZE -PIECE ASSEMBLY -PIECE ASSEMBLY BURNER/GAS TRAIN ASSEMBLY 05-066 X Factory Installed 080-65 X Field Installed Factory-installed burner Every 6DNH machine below 700 tons is shipped from the factory with the burner, refractory assembly, and gas train installed in the high-temperature generator to simplify the chiller/heater installation. This facilitates easier and quicker installation and reduces field costs. It also ensures that all burner-related components are properly installed and wired to the main chiller center for proper control. 6DNH BURNER ASSEMBLY TYPICAL 6DNH -PIECE SHIPMENT The 6DNH05-066 machines are shipped completely assembled as a standard feature with an option for -piece shipment and the 6DNH080-65 machines are shipped by - piece. The -piece is ideal for retrofit or replacement installations where access into the equipment room may be limited. On 6DNH05-066 machines, the burner and gas train are installed at the factory to minimize field assembly. 6DNH080-65 machines, the burner and gas train are installed on field because of multiple pieces shipment. Job-site reassembly and alignment of machines shipped in multiple sections is simplified by pre-erecting the machine in the 3 factory and by incorporating weld-type assembly flanges on all interconnecting piping. Flanged water box nozzles To simplify chiller installation and field piping, all water box nozzles on the evaporator, absorber, and condenser are factory-supplied with ANSI (American National Standards Institute) raised face (RF) flanges. On Single-point box electrical connection Installation costs are further reduced by eliminating field wiring between machine components. On units shipped as a single assembly, all unit-mounted electrical items, including the burner control center, are factory-wired to the chiller microprocessor control center. Only a single-point electrical connection to the machine from the building s electrical service is required. When units are shipped in multiple pieces, a wiring harness is provided for interconnection between the burner control center and chiller control center. A multi-tap transformer, mounted in the chiller control center, provides secondary, single-phase power for the 6DNH controls. Low noise and vibration allows location flexibility Low sound and vibration levels are characteristic of absorption chillers, primarily due to the fact that the only rotating parts are the refrigerant and solution pumps. The overall sound level of a Carrier 6DNH is typically 80 dba. This allows the machines to be installed near occupied spaces or in areas with strict sound requirements. Low vibration levels also make it possible to install the chiller/heater on upper floors without special consideration for vibration dampening systems.
Features/Benefits (cont) Low maintenance Standard features allow simple maintenance procedures Every 6DNH machine has numerous standard design features that provide for convenient and simple maintenance. Hinged waterbox cover on the absorber, and condenser facilitate tube and waterbox inspection. A flange type refractory door on the high-temperature generator simplifies inspection and cleaning of the combustion chamber and smoke tubes. In addition, epoxy coating of the waterboxes and covers, standard on all machines, protects against corrosion and extends machine life. All moving parts are easily accessible for inspection or replacement, as required. VIEW OF TYPICAL HERMETIC PUMP/MOTOR ASSEMBLIES Factory-trained service organization Carrier s extensive service organization offers trained and experienced service technicians in every major city. In addition to routine maintenance and repair services, Carrier also offers a wide array of preventative maintenance, full maintenance, and/or extended service contracts that can be custom tailored to any level of service. Leak-proof hermetic pumps/motors cut maintenance costs Carrier s proven solution auxiliary and refrigerant pumps/ motors are leak-proof, completely self-contained, and hermetically sealed. The hermetic design eliminates the need for a separate, complicated, and possibly leak-prone seal water system while providing leak tightness and longer machine life. Specially designed bearings absorb both radial and axial thrusts to ensure correct fit at all times. There is no possibility of external contamination since the fluid being pumped lubricates and cools the pump and motor assemblies. In addition, both the rotor and the stator are separated by a stainless steel liner that protects the windings from the fluid being pumped. As an additional safety feature, thermal overload switches are embedded in the stator to protect against high winding temperatures. The pumps are field serviceable. Inspection is recommended after 5 years or 0,000 hours of operation, whichever comes first. Pump isolation valves are included on 6DNH machines to make field service easy, if required. 4
Reliable operation PD5 control center continuously monitors machine operation, ensuring precise control Each Carrier 6DN H direct-fired chiller/heater includes a factory mounted and wired PD5 control center that is functionally tested prior to shipment. Continuous monitoring and control of machine operation are performed automatically. A multi-language display on the front of the control center identifies operational status and fault indication. All control center components and the assembly will meet local codes of GB where appropriate and include a main board, a NRCP board, tow Aux. boar ds, molded case circuit breaker, pump contactors, ambient compensated 3-phase pump overload protection, multi-tap control power transformer, and all other necessary safeties and controls. As part of the start-up sequence, the chiller PD5 control center and the burner combustion controller initiate a selfdiagnostic system check to verify that all sensors are in range. Other standard features include a remote start/stop switch and a key-locked control center door that protects against unauthorized access. 6DNH PD5 CONTROL CENTER Superior corrosion protection Absorption chillers must be protected from the possibility of internal corrosion that is always present when lithium bromide solution is in contact with internal machine surfaces. The Carrier 6DNH absorption chiller/heater incorporates a highly effective corrosion inhibitor to provide an extra margin of protection against internal corrosion. Other inhibitors may require the use of exotic 5 tube materials in certain heat exchangers since they are less effective and require frequent maintenance and analysis. The superior corrosion protection of the Carrier inhibitor allows for the use of standard copper tubes throughout the machine (except for the high-temperature generator fire tubes that are made of carbon steel). This results in long machine life and dependable operation. Rugged machine construction Every Carrier 6DNH chiller/heater offers numerous standard features designed to provide reliable, trouble-free operation. The machine is fabricated to meet stringent manufacturing and design requirements and is Carrier-listed to ensure product safety and machine integrity. n-clogging, corrosion proof spray nozzles protect the 6DNH from corrosion and blockage for continuous, reliable operation. Horizontally-positioned, carbon steel fire tubes with flue gas on the inside and lithium bromide on the outside are located above the combustion chamber to allow easy soot removal and tube cleaning. This design feature also prevents the flame inside the combustion chamber from direct contact with the fire tubes to ensure maximum life and reliability. A heated palladium cell is provided as a optional feature. As part of the purge system, the heated palladium cell assists in the removal of hydrogen gas from inside the 6DNH. This action minimizes the need for manual evacuation of the purge storage chamber. The above standard features are evidence of Carrier s commitment to building a direct-fired, double effect chiller/heater able to withstand the most rigorous comfort cooling or light industrial applications. Automatic, motorless purge system extends machine life and ensures optimum efficiency and performance The purge system of an absorption chiller is critical to ensuring efficient operation and long machine life. Even when machines are vacuum tight or properly inhibited, all absorption chillers generate hydrogen and other noncondensable gases in small quantities. Since these gases are present in sufficient volume to interfere with proper machine operation, they must be removed to protect the unit from internal corrosion, lithium bromide solution crystallization, and/or a reduction in chiller capacity. Carrier s motorless purge system protects 6DNH machines from these potential hazards by working continuously during machine operation. Motorless purge system operation During operation, noncondensables tend to accumulate in the absorber section, which operates at the lowest internal pressure. A slip-stream of lithium bromide solution from the solution pump discharge flows through an eductor, creating a suction that draws noncondensables from the absorber. The noncondensables are then entrained by the solution flowing through the eductor. The eductor discharges the solution and noncondensables into a separator in a purge chamber, where the noncondensables are separated from the solution. The noncondensables flow to a storage tank, while the solution returns to the absorber sump. Typically, most of the noncondensable gas is composed of hydrogen, which is automatically dissipated to the atmosphere through a heated palladium cell (when used). As noncondensables accumulate in the external storage tank, they are isolated from the chiller and cannot reenter the machine (even during shutdown). These gases must periodically be exhausted (as required) from the storage tank by a simple procedure performed while the machine is running. Evacuation is performed by a unit-mounted vacuum pump that
Features/Benefits (cont) is connected to the purge evacuation valve. Evacuation through the vacuum pump is necessary because the palladium cell will be damaged if wetted by the lithium bromide solution. Therefore, pressurizing the purge tank above atmospheric pressure with lithium bromide solution is not permitted. The unit-mounted vacuum pump can also be used during chiller maintenance or service to remove noncondensables directly from the machine. TYPICAL MOTORLESS PURGE OPERATION SCHEMATIC 6
Anti-crystallization controls maintain proper solution concentration The 6DNH automatically limits solution concentration in several ways to avoid both crystallization and overdilution to provide dependable, trouble-free operation. Crystallization of the lithium bromide solution depends on the combination of temperature and concentration. Carrier s concentration control system automatically monitors the refrigerant water level in the evaporator in conjunction with the solution temperature returning to the absorber. Because concentration varies with the amount of water in the lithium bromide solution, a rising evaporator level indicates less water in the solution and thus a higher solution concentration. When the refrigerant in the evaporator rises to a weir level, water is transferred from the evaporator to the absorber thus preventing overconcentration to ensure continuous, reliable operation even at cooling water temperature as low as 60.8 F (6 C). Overdilution (and possible refrigerant pump cavitation) shall be controlled by transferring an additional amount of refrigerant from the condenser to the evaporator. The 6DNH also incorporates a simple, passive method of control to correct any crystallization that would typically start to occur on the shell-side of the low temperature solution heat exchanger under abnormal conditions. As the hot solution begins to back up in the generator, as a result of any shell-side blockage, it rises above the overflow pipe and returns directly to the absorber. It is subsequently pumped through the tubeside (heating the shell-side) to restore proper operation. In addition, the 6DNH automatic dilution cycle ensures proper concentration after unit shutdown so that the unit will not crystallize when the machine cools to ambient or machine room temperature. The dilution cycle controls operation of the pumps for a set period of time after shutdown to dilute the solution to prevent an overconcentration condition. 6DNH high COP, direct-fired, double effect, absorption cooling cycle The 6DNH high COP, directfired double effect, absorption chiller/heater consists of an evaporator, absorber, condenser, high and low-temperature generators, solution heat exchangers(bphe), condensate and flue gas heat exchangers, refrigerant/solution/auxiliary. solution pumps, burner and gas train assembly, purge, controls and auxiliaries. Water is used as the refrigerant in vessels maintained under low absolute pressure (vacuum). In the cooling mode, the chiller operates on the principle that under vacuum, water boils at a low temperature. In this case water boils at approximately 40 F (4.4 C), thereby cooling the chilled water circulating through the evaporator tubes. A refrigerant pump is used to circulate the refrigerant water over the evaporator tubes to improve heat transfer. To make the cooling process continuous, the refrigerant vapor must be removed as it is produced. To accomplish this, a lithium bromide solution (which has a high affinity for water) is used to absorb the water vapor. As this process continues, the lithium bromide becomes diluted, reducing its absorption capacity. A solution pump then transfers this weak (diluted) solution to the generators where it is reconcentrated in stages to boil off the previously absorbed water. A variable frequency drive pump automatically maintains optimum solution flow to the generators at all operating conditions for maximum efficiency. The diluted solution is pumped to the high-temperature generator where it is heated and reconcentrated to a medium concentration solution by the heat from the combustion of natural gas or. oil. The medium concentration solution from the hightemperature generator flows to the low-temperature generator where it is heated and reconcentrated to a strong solution by the high temperature water vapor released from the solution in. 6DNH ABSORPTION COOLING CYCLE 7
Features/Benefits (cont) the high-temperature generator. Since the low-temperature generator acts as the condenser acts as the condenser for the high-temperature generator, the heat energy first applied in the high-temperature generator is used again in the low-temperature generator thus reducing the heat input by approximately 45% as compared to an absorption chiller with a single stage of reconcentration. The water vapor released in the shellside of the low-temperature generator, in addition to the new condensed water vapor from the tubeside of the low-temperature generator, enters the condenser to be cooled and returned to a liquid state. The refrigerant water then returns to the evaporator to begin a new cycle. To remove heat from the machine, relatively cool water from a cooling tower or other source is first circulated through the tubes of the absorber to remove the heat of vaporization. The water is then circulated through the tubes of the condenser. The strong (reconcentrated) solution from the low-temperature generator flows back to the absorber to begin a new cycle. For efficiency reasons, the medium concentration solution from the high-temperature generator is passed through the hightemperature solution heat exchanger to pre-heat the weak solution, while pre-cooling the medium concentration solution. The strong solution from the low-temperature generator is passed through the low-temperature solution heat exchanger to pre-cool the solution before being returned to the absorber. The efficiency is further improved by use of two additional components. One is the flue gas heat exchanger which transfers additional heat from flue gas to the weak solution before entering high-stage generator, another is a condensate heat exchanger which transfers additional heat from the vapor condensate leaving low-stage generator to the weak solution. 6DNH high COP, direct-fired, double effect, absorption heating cycle The 6DNH high COP, directfired, double effect, absorption chiller/heater can also be operated in a non-simultaneous heating (only) mode to provide 40 F (60 C) hot water for space heating or other purposes without any additional components. In this mode, the cycle follows a different vapor flow path than that undertaken for cooling and does not use the absorption process. In addition, the absorber-condenser cooling water circuit is drained, and thus not operated, since all heat rejection from the machine is designed to take place through the evaporator (now the heating bundle) in a classic -pipe system which utilizes only the evaporator nozzles. High temperature water vapor produced in the high-temperature generator section is passed directly to the evaporator via absorber where it condenses and transfers its heat to the water circulating through the evaporator tubes. This condensed water then flows to the absorber section where it mixes with the concentrated solution returning from the hightemperature generator. The diluted solution is then pumped back to the high-temperature generator to repeat the vapor generation phase for the heating function. 8
Options and accessories ITEM OPTION* ACCESSORY+ 50 psig (74 kpa)/300 psig (068 kpa) Water boxes X Special Tubing X Unit Voltage (08, 30, 400, 460, or 575-3-60/50) X Dual-Fuel Burner X FM/IRI Approved Burner X Low NO X X Shipping Configuration ( or -piece) X X Condenser Water Flow Switch X Isolation Package 9Machine components FM IRI LEGEND Factory Mutual Industrial Risk Insurers *Factory installed. +Field installed. Machine components TYPICAL 6DNH 3 9 5 8 7 0 6 4 9 LEGEND Low-Temperature Generator High-Temperature Generator 3 Exhaust Gas Outlet/ Flue Gas Heat Exchanger 4 Burner Assembly and Control Center 5 Chiller/Heater Control Center 6 Solution Heat Exchanger 7 Absorber 8 Evaporator 9 Condenser 0 Auxiliary Solution Pump
Physical data ENGLISH Unit 6DNH 05 08 0 04 08 033 NOMINAL COOLING CAPACITY (ton) 50 80 0 40 80 330 RIGGING WEIGHT* (lb) Absorber/Evaporator/G/Condenser G (Includes Burner) Total 8737 974 73 903 3355 390 0695 3358 405 0 *Standard shipping configuration is -piece for sizes 05-066 and -piece for sizes 080-65. 43 3843 556 3596 40 785 OPERATING WEIGHT (lb) 536 640 8843 0348 4958 653 LITHIUM BROMIDE SOLUTION CHARGE (lb) 896 094 35 668 489 4365 REFRIGERANT (WATER) CHARGE (Ib) 88 860 838 794 455 433 CHILLED/HOT WATER (Evap) Pipe Connection Size (in.). Passes COOLING WATER Pipe Connection Size (in.). Passes Absorber Condenser 4 3 5 4 3 5 5 3 6 5 3 6 6 8 49 4775 8904 GAS-TRAIN INLET Standard Pipe Connection Size, NPT (in.).5.5.5.5.5.5 EXHAUST GAS OUTLET minal Flange Connection Size (in.) 9 9 4 4 4 4 Unit 6DNH 036 040 045 050 060 066 NOMINAL COOLING CAPACITY (ton) 360 400 450 500 600 660 RIGGING WEIGHT* (lb) Absorber/Evaporator/G/Condenser G (Includes Burner) Total 503 5787 003 6938 6385 33 9709 7374 7084 004 798 8005 308 0046 40858 OPERATING WEIGHT (lb) 8045 3039 3438 3553 5587 6067 LITHIUM BROMIDE SOLUTION CHARGE (lb) 4409 4630 639 656 809 899 REFRIGERANT (WATER) CHARGE (Ib) 367 33 389 367 83 359 CHILLED/HOT WATER (Evap) Pipe Connection Size (in.). Passes COOLING WATER Pipe Connection Size (in.). Passes Absorber Condenser 6 8 6 8 8 0 8 0 8 6 8 3408 0950 43358 GAS-TRAIN INLET Standard Pipe Connection Size, NPT (in.).5.5.0.0.0.5 EXHAUST GAS OUTLET minal Flange Connection Size (in.) 4 4 4 4 6 6 6 6 6 3 6 37 Unit 6DNH 080 00 0 35 50 65 NOMINAL COOLING CAPACITY (ton) 800 000 00 350 500 650 RIGGING WEIGHT* (lb) Absorber/Evaporator/G/Condenser G (Includes Burner) Total 37809 3867 5676 43387 66 5950 54895 950 77844 580 465 887 65 669 938 8 68850 78 9667 OPERATING WEIGHT (lb) 7308 84480 048 779 30733 38978 LITHIUM BROMIDE SOLUTION CHARGE (lb) 0406 60 6953 8386 9467 098 REFRIGERANT (WATER) CHARGE (Ib) 7 690 465 5093 5997 6570 CHILLED/HOT WATER (Evap) Pipe Connection Size (in.). Passes COOLING WATER Pipe Connection Size (in.). Passes Absorber Condenser 0 4 GAS-TRAIN INLET Standard Pipe Connection Size, NPT (in.).5.5 3 3 3 3 EXHAUST GAS OUTLET minal Flange Connection Size (in.) 37 37 43 43 50 50 G High-Temperature Generator G Low-Temperature Generator 0 4 6 6 4 6 4 6
Physical data SI Unit 6DNH 05 08 0 04 08 033 NOMINAL COOLING CAPACITY (kw) 58 633 739 844 985 6 RIGGING WEIGHT* (kg) Absorber/Evaporator/G/Condenser G (Includes Burner) Total G High-Temperature Generator 3963 349 53 4097 5 560 485 53 6374 577 743 690 667 94 808 OPERATING WEIGHT (kg) 695 7440 8547 930 3 035 LITHIUM BROMIDE SOLUTION CHARGE (kg) 860 950 050,0,900,980 REFRIGERANT (WATER) CHARGE (kg) 400 390 380 360 660 650 CHILLED/HOT WATER (Evap) Pipe Connection Size (mm.). Passes COOLING WATER Pipe Connection Size (mm.). Passes Absorber Condenser 00 3 5 GAS-TRAIN INLET Standard Pipe Connection Size, NPT (mm.) 40 40 40 40 40 40 EXHAUST GAS OUTLET minal Flange Connection Size (mm.) 00 3 5 5 3 50 5 3 50 50 00 6409 66 8575 90 485 90 485 90 600 90 600 90 600 90 600 Unit 6DNH 036 040 045 050 060 066 NOMINAL COOLING CAPACITY (kw) 66 407 583 758 0 3 RIGGING WEIGHT* (kg) Absorber/Evaporator/G/Condenser G (Includes Burner) Total 6896 65 957 7683 896 0579 8940 3345 85 9083 360 703 3976 4557 8533 OPERATING WEIGHT (kg) 7 4079 5485 63 5343 7337 LITHIUM BROMIDE SOLUTION CHARGE (kg) 000 00 830 960 3670 4050 REFRIGERANT (WATER) CHARGE (kg) 60 600 630 60 990 070 CHILLED/HOT WATER (Evap) Pipe Connection Size (mm.). Passes COOLING WATER Pipe Connection Size (mm.). Passes Absorber Condenser 50 00 50 00 00 50 00 50 00 300 50 00 4700 4967 9667 GAS-TRAIN INLET Standard Pipe Connection Size, NPT (mm.) 40 40 50 50 50 65 EXHAUST GAS OUTLET minal Flange Connection Size (mm.) 350 600 350 600 406 670 406 670 406 80 406 930 Unit 6DNH 080 00 0 35 50 65 NOMINAL COOLING CAPACITY (kw) 83 356 40 4747 574 580 RIGGING WEIGHT* (kg) Absorber/Evaporator/G/Condenser G (Includes Burner) Total 750 690 3440 9680 730 6990 4900 040 3530 6400 70 37570 9580 870 4450 OPERATING WEIGHT (kg) 3350 3830 50090 53430 59300 63040 LITHIUM BROMIDE SOLUTION CHARGE (kg) 470 570 7690 8340 8830 9570 REFRIGERANT (WATER) CHARGE (kg) 00 0 0 30 70 980 CHILLED/HOT WATER (Evap) Pipe Connection Size (mm.). Passes COOLING WATER Pipe Connection Size (mm.). Passes Absorber Condenser 50 350 50 350 300 400 300 400 350 400 00 300 330 60 43850 GAS-TRAIN INLET Standard Pipe Connection Size, NPT (mm.) 65 65 80 80 80 80 EXHAUST GAS OUTLET minal Flange Connection Size (mm.) 5 930 5 930 55 080 55 080 55 60 55 60 G Low-Temperature Generator *Standard shipping configuration is -piece for sizes 05-066 and -piece for sizes 080-65. 350 400
Dimensions 6DNH SIZES 00-65 DIMENSIONS (ft-in.) UNIT 6DNH 05/08 0/04 08/033 036/040 045/050 060 066 080 00 0 35 50 65 Overall LengthA - - 5-8 -9 6-0 8-6 0-0-6 3-0 -5 4- -9 4-4 Overall Width B 6-6-9 6-0 7-6 8-0 9-5 9-5 0-8 0-8 3-7 3-7 5-5 5-5 Overall HeightC 6-9 7-7 7-0 8-8 9-3 0-0- - - - - -8-8 Width D* 3-3 3-0 3-4-4 4-6 5-5- 6 6 8-6 8-6 9-9- DIMENSIONS (mm) UNIT 6DNH 05/08 0/04 08/033 036/040 045/050 060 066 080 00 0 35 50 65 Overall LengthA 363 3679 4780 479 4867 5640 64 644 759 6843 7333 694 744 Overall Width B 880 034 077 96 444 866 866 34 34 439 439 4694 4694 Overall HeightC 056 33 38 630 80 30 30 3400 3400 3639 3639 3850 3850 Width D* 00 56 95 38 368 56 56 83 83 58 58 3038 3038 *Standard shipping configuration is -piece for sizes 05-066. Dimension D is width of absorber, evaporator, condenser, G section for -piece shipment. The G assembly is shipped separately. NOTES:. All dimensions in mm are accurate and take into account absorbercondenser crossover piping.. For routine maintenance, allow 3 ft ( m) clearance on all sides and 6 in. (50 mm) above chiller. 3. For service access, allow clearance as follows: a. For tube removal, allow space equal to A dimension (length) at either end of the chiller. b. To open waterbox cover, allow clearance space equal to half of D dimension (width) on the waterbox end of the chiller.
Performance data ENGLISH UNIT 6DNH 05 08 0 04 08 033 COOLING CAPACITY (ton) 50 80 0 40 80 330 HEATING CAPACITY (MBh) 78 533 789 044 385 8 CHILLED WATER Flow Rate (gpm) Pressure Drop (fth O) COOLING WATER Flow Rate (gpm) Pressure Drop (ft) HOT WATER Flow Rate (gpm) Pressure Drop (fth O) FUEL CONSUMPTION Natural Gas (ft 3 ph). Oil (gph) COEFFICIENT OF PERFORMANCE (COP) Natural Gas. Oil UNIT 6DNH 036 040 045 050 060 066 COOLING CAPACITY (ton) 360 400 450 500 600 660 HEATING CAPACITY (MBh) 3067 3407 3833 459 5 56 CHILLED WATER Flow Rate (gpm) Pressure Drop (fth O) COOLING WATER Flow Rate (gpm) Pressure Drop (fth O) HOT WATER Flow Rate (gpm) Pressure Drop (ft) FUEL CONSUMPTION Natural Gas (ft 3 ph). Oil (gph) COEFFICIENT OF PERFORMANCE (COP) Natural Gas. Oil UNIT 6DNH 080 00 0 35 50 65 COOLONG CAPACITY (ton) 800 000 00 350 500 650 HEATING CAPACITY (MBh) 685 858 0 500 777 4055 CHILLED WATER Flow Rate (gpm) Pressure Drop (fth O) COOLING WATER Flow Rate (gpm) Pressure Drop (ft) HOT WATER Flow Rate (gpm) Pressure Drop (fth O) FUEL CONSUMPTION Natural Gas (ft 3 ph). Oil (gph) COEFFICIENT OF PERFORMANCE (COP) Natural Gas. Oil 399 9.9 6 7.9 399 9.9 96 6.9 957 7.7 490 6.9 957 7.7 306 6.5 30 7.9 33 3.8 30 7.9 54 36.6 479 9.9 745 7.9 479 9.9 53 8. 065 7. 656 6. 065 7. 56 8.3 663 45.9 439 50.5 663 45.9 6405 45.7 559 9.9 869 7.9 559 9.9 345 9.6 98 9.5 86 35. 98 9.5 88 0.6 395 3.8 4967 43.0 395 3.8 7686 54.9 639 9.9 993 7.9 639 9.9 537.0 33 9. 069 35. 33 9. 30.9 3595 4.3 5587 54.5 3595 4.3 8646 6.8 746 8.7 59 8.5 746 8.7 793.8 598 33.5 483 36.7 598 33.5 3843 7.4 3994 3.8 608 44.6 3994 3.8 9607 68.6 879 9.0 366 9. 879 9.0 4 5. 758 33.8 73 36.7 758 33.8 47 30. 4394 40.7 689 54.5 4394 40.7 0568 75.5 3 LEGEND ARI Air Conditioning and Refrigeration Institute HHV Higher Heating Value MBh Btu/h in thousands te: Ratings are based on ARI 560, latest edition, 54/44 F (.4 gpm/ton) chilled water; 85 F (4.0 gpm/ton) cooling water; 30/40 F hot water; fouling factor.0005 ft -hr- o F/Btu for absorber and condenser,.000 ft -hr- o F/Btu for evaporator; natural gas heating value,000 Btu/ft 3 (HHV); oil heating value 40,000 Btu/gal. Higher Heating Capacity is Available.
Performance data (cont) SI UNIT 6DNH 05 08 0 04 08 033 COOLONG CAPACITY (kw) 57 633 738 844 985 60 HEATING CAPACITY (kw) 374 449 54 599 699 84 CHILLED WATER Flow Rate (L/s) Pressure Drop (kpa) COOLING WATER Flow Rate (L/s) Pressure Drop (kpa) HOT WATER Flow Rate (L/s) Pressure Drop (kpa) FUEL CONSUMPTION Natural Gas (M 3 /hr). Oil (L/hr) COEFFICIENT OF PERFORMANCE (COP) Natural Gas. Oil 5. 89. 39. 83.3 5. 89. 38.3 36.6 UNIT 6DNH 036 040 045 050 060 066 COOLONG CAPACITY (kw) 66 407 58 758 0 3 HEATING CAPACITY (kw) 899 999 3 48 498 648 CHILLED WATER Flow Rate (L/s) Pressure Drop (kpa) COOLING WATER Flow Rate (L/s) Pressure Drop (kpa) HOT WATER Flow Rate (L/s) Pressure Drop (kpa) FUEL CONSUMPTION Natural Gas (M 3 /hr). Oil (L/hr) COEFFICIENT OF PERFORMANCE (COP) Natural Gas. Oil 60.5 5.9 94.0 80.4 60.5 5.9 9.0 87.8 UNIT 6DNH 080 00 0 35 50 65 COOLONG CAPACITY (kw) 83 356 40 4747 574 580 HEATING CAPACITY (kw) 997 497 996 3370 3745 49 CHILLED WATER Flow Rate (L/s) Pressure Drop (kpa) COOLING WATER Flow Rate (L/s) Pressure Drop (kpa) HOT WATER Flow Rate (L/s) Pressure Drop (kpa) FUEL CONSUMPTION Natural Gas (M 3 /hr). Oil (L/hr) COEFFICIENT OF PERFORMANCE (COP) Natural Gas. Oil 34.4 83.3 08.9 98 34.4 83.3 04.4 95. 30. 89. 47.0 83.3 30. 89. 46.0 43.9 67. 5.0 04.4 78.4 67. 5.0 0. 97.6 68.0 37. 6. 50.9 68.0 37. 55.5 44.0 35.3 89. 5.8 83.3 35.3 89. 53.7 5. 75.6 88. 7.5 04.9 75.6 88. 5.0 09.8 0.6 98 33.3 8.4 0.6 98 306.6 9.7 40.3 89. 6.7 83.3 40.3 89. 6.3 58.5 84.0 87. 30.6 04.9 84.0 87. 7.7.0 6.8 6.4 35.5 6.7 6.8 6.4 344.9 39.3 47.0 55.9 73. 85.3 47.0 55.9 7.5 68.3 00.8 00.0 56.7 09.8 00.8 00.0 53.3 46.4 5.0 98 39.7 33.3 5.0 98.0 383. 356.9 55.4 56.8 86. 87. 55.4 56.8 84.3 80.5 0.9 00.9 7.3 09.8 0.9 00.9 68.8 6.0 77..5 430.8 6.7 77..5 4.6 40.5 4 LEGEND ARI Air Conditioning and Refrigeration Institute HHV Higher Heating Value te: Ratings are based on ARI 560, latest edition,./6.7 C (.043 L/s-kW) chilled water; 9.4 C (.07 L/s-kW) cooling water; 54.4/60 C hot water; fouling factor.000044 m -hr- o C/W for absorber and condenser,.000076 m -hr- o C/W for evaporator; natural gas heating value 8899 kcal/m 3 (HHV); oil heating value 930 kcal/l Higher Heating Capacity is available.
Fuel heating values In accordance with ARI 560, latest edition, performance ratings of the Carrier 6DNH are based on the gross or higher heating value (HHV) of the fuel employed which accounts for condensation of water vapor formed during the combustion process. In comparison, the net or lower heating value (LHV) is approximately 90% of the higher heating value, since it does not account for the latent heat of vaporization of water formed during combustion. The use of higher heating value is a customary practice in rth America. Typical HHVs are,000 Btu/ft 3 (8,889 kcal/m 3 ) and 40,000 Btu/gal (9,30 kcal/l) for. oil. Actual HHV may differ and will directly impact the required volumetric flow rate of the fuel. The required MBh (Btuh in thousands) input to the burner remains unchanged. Part-load performance To determine part-load performance, refer to the 6DNH Part- Load Performance curve shown below. This curve depicts Fuel Consumption Ratio (FCR) versus Percent Capacity at several cooling water temperatures and in accordance with the ARI load line which is based on a.5 F (.4 C) reduction in cooling water temperature for every 0% reduction in load. Fuel requirements at part-load can be calculated with one of the following equations: Gas: Fuel Consumption MBh = Full Load Consumption (MBh) x FCR x Percent Capacity Oil: Fuel Consumption (gph) = Full Load Oil Consumption (gph) x FCR x Percent Capacity Fuel consumption for natural gas, expressed as a volumetric flow rate (ft 3 /hr), is determined by dividing the fuel consumption (in units of Btuh) by the higher heating value of the natural gas (in units of Btu/ft 3 ). As shown on the part-load performance curve, the continuous operating range for the 6DNH is approximately 5 to 00% of full load when operated on either natural gas or. oil, based on minimum fire requirements of the burner. Below 5% the burner will cycle on and off to meet the required load and water temperature. ARI 560, latest version, defines Integrated Part Load Value (IPLV) as a measure of part-load efficiency representing the weighted average of overall chiller performance calculated by the following equation: IPLV =.0A +.4B +.45C +.D Where A = COP at 00% B = COP at 75% C = COP at 50% D = COP at 5% or minimum load NOTE: COP is the Coefficient of Performance. Therefore, IPLV =.0 (.36) +.4 (.49) +.45 (.67) +. (.60) =.58 6DNH PART-LOAD PERFORMANCE. FUEL CONSUMPTION RATIO 0.9 0.8 ARI 5 0.7 0 0 0 30 40 50 60 70 80 90 00 PERCENT CAPACITY
Application data Vent and drain connections All vents and drain connections are found on the waterbox covers. Connection size is 3/4-in. FPT. Provide high points of the machine piping system with vents and the low points with drains. If shutoff valves are provided in the main water pipes near the unit, a minimum amount of the system water is lost when the heat exchangers are drained. It is recommended that pressure gages be provided at points of entering and leaving water to measure pressure drop through the heat exchanger. Gages may be installed as shown in the table below. Pressure gages installed at the vent and drain connections do not include nozzle pressure losses. Use a reliable manometer to measure pressure differential when determining water flow. Regular gages are insensitive and do not provide accurate measurement of flow conditions. NUMBER OF PASSES GAGE LOCATION, 3 One gage in each water box, 4 Two gages in water box with nozzles Range of application The 6DNH absorption chiller/heater is designed for standard water chilling applications of 50 to 650 tons (57 to 580 kw) at standard ARI rating conditions. UL or CE listing (Optional) The burner assembly, unit control center, machine mounted controls, wiring, and the entire chiller/heater are listed together as a whole, in accordance with the requirements of UL or CE standards. Rupture disk piping The 6DNH is equipped with a fusible plug or a rupture disk (optional) on the low-temperature generator. It is recommended that piping from these devices be routed to appropriate areas away from the machine in accordance with Carrier s written installation instructions, the current version of ANSI/ASHRAE 5 (American Society of Heating, Refrigeration, and Air Conditioning Engineers), and any local jurisdictional requirements that may apply. Piping should be adequately supported and the proper fittings should be provided to allow periodic inspection of the disk. Refer to Carrier certified drawings for exact location of the rupture disk on the chiller. UNIT SIZE 6DNH05-65 LEGEND RF Raised Face RUPTURE DISK CONNECTION SIZE 6 in. 300 psig RF flange MATERIAL SPECIFICATIONS ITEM MATERIAL SPECIFICATIONS SHELL: Evaporator Steel Q35B Absorber Steel Q35B Condenser Steel Q35B G Steel Q35B G Steel Q35B TUBESHEET: Evaporator Steel Q35B Absorber Steel Q35B Condenser Steel Q35B G Steel 0g G Steel Q35B WATERBOX: Evaporator Steel Q35B Absorber Steel Q35B Condenser Steel Q35B G Steel 0g G Steel Q35B TUBES: Evaporator Copper C0T-/H Absorber Copper C0T-/H Condenser Copper C0T-/H G Steel 0# G Copper C0T-0L PIPING Steel 0# LEGEND G -- High-Temperature Generator G -- Low-Temperature Generator Thermal insulation Application of cold/hot surface thermal insulation should be done after final installation at field and machine leak integrity has been verified. Refer to Carrier certified drawings for material specifications and recommended chiller/heater insulation requirements. 6 THERMAL INSULATION SURFACE AREA REQUIREMENTS ENGLISH (FT ) UNIT SIZE 05/08 0/04 08/033 036/040 045/050 060 066 080 00 0 35 50 65 COLD SURFACE 67 76 83 93 47 56 03 37 65 60 97 03 HOT SURFACE 64/7 86/95 6/36 57/68 300/33 395 47 545 580 699 749 840 897 THERMAL INSULATION SURFACE AREA REQUIREMENTS SI (m ) UNIT SIZE 05/08 0/04 08/033 036/040 045/050 060 066 080 00 0 35 50 65 COLD SURFACE 6. 7. 7.7 8.7 0.4 3.6 4.5 8.9.0 5.4 4.8 8.3 8.8 HOT SURFACE 5./5.9 7.3/8..0/.9 3.8/4.9 7.9/9. 36.7 38.7 50.7 53.9 65 69.6 78. 83.4
STANDARD WATERBOX AND CROSSOVER PIPE CONFIGURATION 6DNH UNIT EVAPORATOR ABSORBER CONDENSER CROSS- OVER Inlet Outlet Inlet Outlet Inlet Outlet PIPE 05- N N M M M M Included 65 LEGEND M -- Marine Waterbox N -- zzle-in-head Waterbox HEAT EXCHANGER MINIMUM/MAXIMUM FLOW RATES* -- ENGLISH (gpm) EVAPORATOR 6DNH -Pass -Pass 3-Pass 4-Pass SIZE Min Max Min Max Min Max Min Max 05 53 0 69 675 7 506 08 95 8 97 787 48 590 0 346 38 30 9 73 69 04 395 579 63 053 97 789 08 703 8 35 406 34 937 033 80 380 40 640 73 093 036 904 367 45 809 30 06 040 0 4048 506 04 337 349 045 096 4385 548 93 365 46 050 3 489 6 446 408 630 060 466 5866 733 933 066 466 5866 733 933 080 970 788 985 3940 00 970 788 985 3940 0 696 0786 348 5393 35 696 0786 348 5393 50 3338 3353 669 6677 65 3338 3353 669 6677 *Flow rates based on standard tubes. Minimum flow based on tube velocity of 3 ft/sec; maximum flow based on ft/sec. ABSORBER-CONDENSER 6DNH -Pass/-Pass SIZE Min Max 05 363 454 08 433 734 0 536 44 04 6 448 08 553 033 649 598 036 665 66 040 738 950 045 834 3337 050 95 3699 060 38 4554 066 38 4554 080 560 64 00 560 64 7 0 76 7047 35 76 7047 50 5 9005 65 5 9005 *Flow rates based on standard tubes. Minimum flow based on tube velocity of 3 ft/sec; maximum flow based on ft/sec. HEAT EXCHANGER STANDARD PASS AND NOZZLE ARRANGEMENT 6DNH EVAPORATOR ABSORBER CONDENSER UNIT Pass Inlet Pass Inlet Pass Inlet 05-04 3 L or R L L 08-65 L or R L L LEGEND L -- Left End Inlet R -- Right End Inlet HEAT EXCHANGER MINIMUM/MAXIMUM FLOW RATES* -- SI (L/s) EVAPORATOR 6DNH -Pass -Pass 3-Pass 4-Pass SIZE Min Max Min Max Min Max Min Max 05 6 64 43 8 3 08 9 74 50 9 37 0 87 5 58 44 04 5 00 7 66 50 08 44 77 89 5 59 033 5 07 6 03 7 69 036 57 8 9 4 9 76 040 64 55 3 8 85 045 69 77 35 38 3 9 050 77 309 39 54 6 03 060 93 370 46 85 066 93 370 46 85 080 4 497 6 49 00 4 497 6 49 0 70 680 85 340 35 70 680 85 340 50 84 05 4 65 84 05 4 *Flow rates based on standard tubes. Minimum flow based on tube velocity of.9 m/sec; maximum flow based on 3.6 m/sec. ABSORBER-CONDENSER 6DNH -Pass/-Pass SIZE Min Max 05 3 9 08 7 09 0 34 35 04 39 54 08 35 40 033 4 64 036 4 68 040 47 86 045 53 050 58 33 060 7 87 066 7 87 080 98 394 00 98 394 0 445 35 445 50 4 568 65 4 568 *Flow rates based on standard tubes. Minimum flow based on tube velocity of.9 m/sec; maximum flow based on 3.6 m/sec.
Application data (cont) Burner mounting Depending on unit size, burner assemblies on the 6DNH are either factory-installed as an integral part of the chiller or shipped as a separate component for field installation. The 6DNH05-066 models are shipped with the burner factoryinstalled in the high-temperature generator. On models where field-installation is required, rigging should be used to position both the front plate assembly and the burner assembly because of their heavy weights. For the front plate, either webbed strapping placed around the refractory or a lifting bar in the center opening may be used. For burner assemblies that do not have lifting lugs, place webbed strapping around a central balance area of the burner. Rig burner assemblies that have lifting lugs in accordance with standard rigging procedures. UNIT 6DN SOOKOOK GAS BURNER MODEL NO. STANDARD BURNER CONFIGURATION STANDARD GAS SOOKOOK SUPPLY OIL BURNER PRESSURE MODEL NO. RANGE MAXIMUM FIRING RATE GAS (ft 3 ph) MAXIMUM FIRING RATE OIL (gph) 05 P45M 40 to 0 in. wg PGR5 96 6.9 08 P60M 40 to 0 in. wg PGR5 53 8. 0 P60M 40 to 0 in. wg PGR5 345 9.6 04 P65M 40 to 0 in. wg PGR9 537.0 08 P7M 40 to 0 in. wg PGR9 793.8 033 P7M 40 to 0 in. wg PGR9 4 5. 036 P7M 40 to 0 in. wg PGR 306 6.5 040 P7M 40 to 0 in. wg PGR 56 8.3 045 P9M 40 to 0 in. wg PGR9 88 0.6 050 P9M 40 to 0 in. wg PGR9 30.9 060 P9M 40 to 0 in. wg PGR9 3843 7.4 066 P9M 40 to 0 in. wg PGR9 47 30. 080 PM 40 to 0 in. wg PGR8 54 36.6 00 PM 40 to 0 in. wg PGR8 6405 45.7 0 P3M 40 to 0 in. wg PGR36 7686 54.8 35 P50M 40 to 0 in. wg PGR50 8646 6.8 50 P50M 40 to 0 in. wg PGR50 9607 68.6 65 P50M 40 to 0 in. wg PGR50 0568 75.5 LEGEND NOTE: Actual gas train size is dependent on gas pressure, agency approvals, gas specifications, burner input and the required burner manifold gas pressure. Higher gas pressures than those listed above are available. TYPICAL BURNER MOUNTING BURNER LUG, WASHER, AND NUT BOLT MOUNTING GENERATOR BOLT MOUNTING 8 GASKET OR ROPE CONNECTION PIPE ASSEMBLY GASKET OR ROPE
Fuel systems The gas train and oil supply systems are supplied preassembled and with pre-installed interconnection fittings. Specific fuel system components and instrumentation will vary depending on local regulations, codes, and ordinances and on the particular job requirements. UL certification is standard on every system supplied with an option to provide FM (Factory Mutual), IRI (Industrial Risk Insurers) or other code requirements that may be necessary. TYPICAL GAS TRAIN 4 6 3 7 ITEM DESCRIPTION Ball Valve SSOV 3 SSOV 4 LOW GAS PRESSURE SWITCH 5 HIGH GAS PRESSURE SWITCH 6 REGULATOR 7 BURNER FLANGE 5 TYPICAL OIL SUPPLY SYSTEM 0 5 4 : Supply Line : Return Line 3 9 6 3 4 7 8 9 ITEM DESCRIPTION Oil Pump without Oil Solenoid Filter 3 Oil Solenoid 4 Oil Solenoid 5 zzle Holder with Integral Shutoff Device 6 Oil Solenoid 7 Oil Flow Regulator 8 Oil Pressure Switch 9 Oil Solenoid 0 zzle Supply Line zzle Return Line zzle Control Circuit 3 System Return Line 4 System Supply Line
Application data (cont) Combustion air supply An adequate supply of combustion air is required by the burner for proper, efficient operation and to ensure complete combustion. It is recommended that excess air be provided to the burner to account for variations in fuel properties and air/fuel supply rates. As a general rule, cu ft of combustion air should be supplied for every 000 Btu of fuel provided to the burner. This equates to approximately 0% excess air for natural gas and ensures complete combustion and efficient operation while minimizing smoke, soot, and the formation of carbon monoxide (CO) and nitrogen oxides ( x ). The source of combustion air to the burner should be in accordance with all local codes and regulations. Exhaust gas flue and stack recommendations Design and construction of the flue stack should comply with all municipal, state, and federal codes and regulations, as applicable. Typical exhaust gas temperature for the 6DNH is 375 F (90 C). However, the stack design temperature should be no less than 675 F (360). It is recommended that insulated, double-wall, round ducting be used in all applications. Flat-sided ducting should not be used since it has a tendency to flex. Flexing causes pulsations in the flue stack, inefficient combustion, and possibly erratic chiller/heater operation. Proper stack design should allow continuous flow by avoiding sharp bends and should be sized to maintain a static pressure between 0 to 0.0 in. wg (0 to 5 mm) at the stack entrance. Use of a barometric damper or sequential motorized draft control is required to properly regulate exhaust gas static pressure and maintain optimum performance. A vent cap, lighting arrestor, and provisions for a condensate drain are also required. Cross-sectional area of the stack is determined by calculating the volumetric flow rate of the exhaust gases and then selecting a diameter that results in an exhaust gas velocity of no greater that to 5 ft/sec (3.6 to 4.6 m/sec). Height of the stack is determined by the length of the horizontal run and the number of 90 degree bends. As a general rule, provide 7 in. (80 mm) of stack height for every ft (300 mm) of horizontal length and 4 ft (.0 m) for every 90 degree bend. The location, height, and positioning of the stack outside the building should consider roof patterns, projections, ancillary equipment, aesthetics, and wind flow. In situations where multiple machines will utilize a common exhaust gas flue stack, individual dampers and/or draft control systems for each unit are recommended. Connection of the stack to the 6DNH exhaust gas outlet flange should be made using a rectangular-to-round transition piece. Dimensions of the exhaust gas flange can be found on the appropriate 6DNH certified drawings. Service access To perform routine maintenance, allow 3 ft ( m) clearance on all sides of machine and 6 in. (50 mm) above the chiller/heater. For proper tube removal, a clearance equal to the overall length of the machine should be provided on each end of the 6DNH. To service the high-stage generator, provide a clearance equal to the length of the high stage generator assembly on both ends of the machine. To allow for opening of hinged waterbox cover, clearance area must be provided at the waterbox end of the chiller. The space opposite the water nozzle must be equal to half the width of dimension D on page. 0
Typical control sequence NORMAL START FLOW CHART (PART ) Start Request (6DN/DNH) Startup Routine Flowchart 008..8 Verify All sensors In range Inc Prestart satisfies Sensor Fault/ Prestart Alerts Start Chilled Water Pump Cooling Mode 0s Start Water Verify Timer Heating40 B Heating75 C Verify Chilled Water Flow Water Timer (configured In service) elapsed Chilled Water Fault (State 8) Recycle Condition (refer to 5.4) Monitor for Recycle Start Start Cooling Water Pump 0s Start Water Verify Timer Verify Cooling Water Flow Water Timer (configured In service) elapsed Cooling Water Fault (State 83) Power loss concentration protect Start Cooling Tower Control Start Sol Pump Recycle start and not the first startup Power loss restart E Power loss restart A Power loss concentration protect