Absorption Chillers

TGG, TBG, TEG, TUG, 3.9 TBS, Gene-Link series

Stable Chilled Water Outlet TemperaturePID control is applied to maintain constant chilled water outlet temperature. When the cooling load changes, the chiller adjuststhe amount of heat used to regenerate the desiccant. Temperature control is +/- 1.0ᵒC.

Automatic De-crystallization SystemTo prevent crystallization, the concentration of the LiBr solution is controlled by adjusting the heat input. The chiller monitors the temperature of Chilled Water, Cooling Water,and Solution for this purpose.If the Cooling Water temperature decreases or the load decreases, the chiller will automatically decrease the heat input to prevent crystallization.

Easy Setting of Chilled Water Outlet TemperatureSetpoints can be changed from the HMI on the chiller or remotely through LonWorks communication.

High Airtight StructureThe body of the chiller is robotically welded and checked for leaks by filling with helium in a controlled space. No sight glasses and the minimum number of valves and screws havebeen used to achieve maximum airtightness. This prolongs the life of the chiller and decreases the maintenance.

Standard Features:Automatic restart in case of a power failure Maximum operating pressure of 784 kPa (114 psi)No requirement for operation of Chilled/Cooling Water Pump during the diluting operation of the desiccant.

Optional Items:Oil fired combustion Inverter control for solution pumpsDual fuel combustion - switching from oil to natural gas LonWorks for BASMarine waterboxes Remote controlLarge temperature difference to reduce the powe of auxiliary pumps

Scope of SupplyPPI Factory Provided Field Provided

Piping WorkElectric Power & Primary Interlock Wiring

Factory - required

Field

FieldFieldField

Field

Factory - required

Factory - optional

Commissioning by PPI with contractor in attendance.Start-up and Commissioning at Job SiteUtilities Required for Commissioning

Item NotesFor larger machines, LiBr will ship separately.

Under a separate contract.

LiBr Solution & Refrigerant WaterThermal InsulationSpare PartsAuxiliary Equipment (Pumps, Cooling Tower)

Direct Fired

Sigma Ace TGG, TBG, TEG, TUG seriesSupply of Chilled and Hot Water by Means of Highly Efficient Combustion.

The patented Reverse Cycle design provides the world's Save even more fuel when optional Inverter Control for thehighest efficiency. Solution Pump is applied.Fuel gas consumption can be reduced as follows compared to conventional models: TBG series: 9%

TEG series: 15%TUG series: 22%

Note Note

1. The standard calorific value of gas applied above is HHV=1237 BTU/scf. 1. 1.4 Series and 1.2R Series are equipped with inverter control as standard.

2. The capacity of the chiller in the above simulation is 210 USRT. 2. It is assumed that cooling water inlet temp is 89.6ᵒF at 100% load, 80.6ᵒF at

0% load and it varies proportionally while the load is changing.

3. The above graph shows plotted points of maximum COP and the actual

measured value may vary depending on site conditions.

Very Efficient Design Even More Savings at Part Load

Fuel Consumption Rate (scfm) Part Load COP

20.0

25.0

30.0

35.0

Conventional TBG series TEG series TUG series 0.8

1

1.2

1.4

1.6

0% 20% 40% 60% 80% 100%

1.4 series (with inverter)

1.3 series (with inverter)

1.2R series (with inverter)

1.2 series (with inverter)

1.2 series (no inverter)

Conventional

Less fuel consumption... Saves you money.

High

er C

OP

Direct Fired

Sigma Ace TGG, TBG, TEG, TUG seriesSupply of Chilled and Hot Water by Means of Highly Efficient Combustion.

Cooling Cycle Heating Cycle

Direct FiredSigma Ace 1.2R TBG series

TBG- 80A 100A 120A 150A 180A 210A 250A 300A 360A 400A 450A 500A 560A 630A 700A 830A 1000AkW 281 352 422 528 633 739 879 1055 1266 1407 1583 1759 1970 2216 2462 2919 3517RT 80 100 120 150 180 210 250 300 360 400 450 500 560 630 700 830 1000kW 236 294 353 442 530 618 736 883 1060 1178 1325 1472 1649 1855 2061 2452 2954

MMBTU/h 805 1003 1205 1509 1809 2109 2512 3014 3618 4021 4522 5024 5628 6331 7034 8369 10082Cooling ᵒFHeating ᵒFFlow Rate gpm 213 266 320 399 479 559 667 799 959 1065 1198 1331 1491 1677 1864 2210 2663Pressure Loss psi 8.9 9.4 8.3 8.6 9.8 10.2 10.9 11.9 10.7 11.1 10.3 10.8 6.7 7.2 9.5 6.5 6.7Retained Water gal 32 37 42 50 69 77 90 100 124 132 156 166 185 198 217 272 325Inlet Temp. ᵒFOutlet Temp. ᵒFFlow Rate gpm 352 440 528 660 793 925 1101 1321 1585 1761 1981 2201 2466 2774 3082 3654 4403Pressure Loss psi 6.9 8.4 11.0 13.4 8.5 9.5 9.5 11.4 8.7 9.9 9.6 12.1 16.9 17.6 22.5 15.7 16.2Retained Water gal 69 77 92 108 153 169 190 211 288 301 388 412 462 494 531 713 880Cooling MMBTU/h 874 1092 1311 1638 1976 2290 2730 3276 3928 4369 4915 5461 6113 6877 7642 9072 10928Heating MMBTU/h 952 1191 1433 1792 2147 2505 2983 3577 4294 4771 5369 5959 6676 7512 8345 9963 12000Gas Inlet Pressure psi 0.3 0.3 0.3 0.3 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 14.2 14.2 14.2 14.2Capacity KVA 4.6 5 6.2 6.2 6.9 7.8 10.5 10.5 11.7 11.7 16.2 16.2 16.2 18.8 21 24.8 30.6Current A 7.4 8.1 9.8 9.8 10.8 12.2 16.1 16.1 17.8 17.8 24.2 24.2 24.2 28 31.2 36.7 45.1Total Motor Power KW 1.7 2.05 2.8 2.8 3.35 4.4 5.9 5.9 6.8 6.8 9.9 9.9 9.9 11.7 13.5 15.5 19.5Ch. W. In/Out A 100 100 125 125 150 150 200 200 200 200 200 200 250 250 250 250 300Co. W. In/Out A 125 125 125 125 150 150 200 200 250 250 250 250 300 300 300 350 350Fuel Gas Inlet A 50 50 50 50 50 50 50 50 50 50 50 50 80 50 50 50 50Exh Gas Outlet in 5.5x12.8 5.5x12.8 5.5x12.8 5.5x12.8 6.3x15.1 6.3x15.1 8.3x17.4 8.3x17.4 9.8x21.1 9.8x21.1 10.6x25.5 10.6x25.5 11.4x27.7 11.4x27.7 11.4x30.8 11.4x30.8 11.4x30.8Length in 112.8 112.8 144.3 144.3 150.3 149.1 197.2 197.2 201.3 201.3 205.2 205.2 248.5 248.5 272.2 270.5 270.5Width in 67.7 67.7 67.7 67.7 81.6 81.3 86.1 86.1 96.7 99.4 111.9 111.8 116.3 116.4 120.5 124.9 137.8Height in 84.4 84.4 84.4 84.4 90.8 90.8 90.7 90.7 97.5 97.5 107.4 107.4 107.4 107.4 107.4 128.0 137.2Operation Wt. lbs 9408 10080 12096 12768 16800 17696 22400 23520 29792 30688 36960 38528 44352 45920 50400 62496 74816Shipping Wt. lbs 8736 8960 10976 11648 14784 15456 19936 21056 26208 27104 32256 33600 38752 40096 43904 54208 56000

Notes1. Heating value and supply pressure for fuel gas at standard conditions are shown in the table below. 5. The fouling factor of both Chilled/Hot Water and Cooling Water is 8.6 x 10-5 m2 K/W.2. Performance tolerance is based on JIS B8622-2002. 6. The cooling water inlet temperature shall not be lower than 59ᵒF.3. Operation load range is from 10% to 100%. 7. For TBG1000, LiBr solution will be shipped separately and the shipping weight shown above is shown 4. The maximum operating pressure is 114 psi (gauge) for both Chilled/Hot Water and Cooling Water. without LiBr solution.

Unit NGBTU/scf 1237 Fuel Gas Consumption Rate <m3

N>cfm 24.69 = (Heat Input for Each Model <MJ/h>)cfm 14.36 (HHV of Fuel Gas <MJ/m3

N>)

Heating Value Based on higher heating valueExhaust Gas Volume Exhaust gas volume per scfm of fuel gas to 392ᵒF of Exhaust gasRequired Air Volume Minimum required air volume per scfm of fuel as at 77ᵒF of air temperature.

Remarks

Cool

ingW

ater 89.6

99.1

Heat

Inpu

t (G

as F

iring

)El

ectr

icity

400

V

60Hz

Conn

ectio

nDi

men

sions

Wei

ght

Item

Model

Cooling Capacity

Heating Capacity

Chill

ed (H

ot)

Wat

er

53.6->44.6132.4->140

Interlock WiringGas Fired / Gene-Link

SymbolsSymbol

CHPCOPCTVFELB

FCSMS Electromagnetic SwitchOCR

XWLRLOL Malfunction Indicator

Overcurrent RelayAuxiliary RelayPower IndicatorOperation Indicator

Name

FuseGround Fault BreakerVentiliation FanCooling Tower FanCooling Water PumpChilled Water Pump

Operation Switch

Operation Sequence Chart Gas Combustion

Operation Sequence Chart Gas Combustion

Thermal Insulation

80 100 120 150 180 210 250 300 360 400 450 500 560 630 700 830 1000

50 HTG Shell 3.7 3.9 5.4 5.7 6.5 6.7 8.3 8.6 10.5 10.8 12.9 13.1 15.9 16.1 19.3 22.1 26.4Solution Outlet from HTG

Smokebox of HTGLTG Shell

LTG HeaderHeat ExchangerFloating ValveSolution Piping

Refrigerant Vapor PipingRefrigerant Drain Piping

25 Chilled Water Header 1.5 1.5 1.5 1.5 2.4 2.4 2.4 2.4 2.8 2.8 3.5 3.5 3.5 3.5 3.5 4.6 5.7

10Evaporator Shell

Refrigerant Pump 1.7 1.7 2.5 2.5 2.9 2.9 4.2 4.2 4.4 4.4 5.3 5.3 6.6 6.6 7.3 8.1 9.7

Glass Wool (with aluminum foil) 25

Refrigerant Piping Chilled Water Nozzle Refrigerant

Blow Piping 0.8 0.8 0.8 0.8 1 1 1.1 1.1 1.5 1.5 1.6 1.6 1.7 1.7 1.7 2.1 2.4The above values are for the TBG 1.2R series.

Soft Polyurethane Foam

Glass Wool (with aluminum foil)

Heat

Insu

latio

nCo

ld In

sula

tion

PartThicknessMaterial

25 26.4 27.3 29.4 34.6 38.923.58.7 8.7 10.1 10.1 13 13.1 15.4 15.4 19.3 19.3 23.2

Area (m2)

Piping Procedure

Direct Fired Gene-Link

Steam AbsorptionThe Stop valve shall be installed in the Inlet/Outlet piping for Chilled/Hot Water,

Cooling Water, and Waste Heat Hot Water.Pressure gauges and thermometers shall be installed near Inlet/Outlet piping for both

Chilled/Hot Water and Cooling Water.The flow rates shall be controlled to be stable. If the Chilled/Hot Water Flow Rate

drops suddenly, the chiller may stop for safety reasons.The positions of the pumps and expansion tanks shall be designed taking into

consideration their pump head, static water head, and the maximum operatingpressure of the Chiller.

Do not exceed the maximum operating pressure of the chiller.Install the air vent valve in the appropriate place for all water circuits. Pipe to drain pit.Waterboxes contain drain valves for service. Allow for access and drain to floor.Two stop valves shall be installed for chemical cleaning of the Cooling Water System.Necessary measures shall be taken to avoid freezing of water in the piping and inside the

Chiller during non-operationg of the Chiller in winer.The piping shall be removable for service. See Detail A.If the Chiller is installed at the same level as the Cooling Tower, it is required to take

measues to prevent reverse flow drainage during non-operation.The necessary measures shall be taken to avoid the combustion exhaust gas from entering

the Cooling Tower or fresh air intake.Heat resistant piping shall be installed for the Cooling Water System if the Chiller is also

used for heating. The Cooling Water temperature may go up to approx. 90ᵒC duringthe heating mode.

Cooling Water Control

1. Take care so that the cooling water inlet temperature is above 22ᵒC.2. Install blow-down valve in the cooling water piping before the cooling tower to prevent excess concentration of contaminants in the cooling water.3. Clean the cooling tower periodically to reduce biological growth that will reduce performance and shorten equipment life.4. Cooling water control shall be done in accordance with the guideline of JRA (JRA-GL-02=1994) or in consultation with specialized water treatment chemical dealer.