ENVIRONMENTALLY FRIENDLY TECHNOLOGY
Cooling cycle
Figure 9. Cooling cycle
Exhaust Gas
Condenser | Low Temperature Generator |
Cooling Water outlet |
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Absorber |
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A Valve | High Temperature |
Evaporator | Generator |
Chilled Water
Burner
C
Valve
Refrigerant Pump |
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| Purge Unit |
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| Heat Exchanger |
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| Absorbent Pump | Cooling Water Inlet |
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| Concentrated Solution |
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| Liquid Refrigerant |
| Chilled Water | |
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| Intermediate Solution |
| Refrigerant Vapor | Open | |||
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| Diluted Solution |
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| Cooling Water | Close | |
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Graph 10. D¨uhring diagram
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| 40% 45% | 50% | 55%D | 60% | 65% | 760 |
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| 700 |
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| 68% |
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| 500 |
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| 80 |
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| 400 |
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| 300 |
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(° C) | 70 |
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| Concentrations |
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| 200 |
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Temperature of refrigerant |
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60 |
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| 160 | Pressure (Torr) | |||||
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| Constant |
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50 |
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40 |
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30 |
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| 0 | 10 | 20 | 30 | 40 | 50 | 60 | 70 |
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| 100 | 110 | 120 | 130 | 140 | 150 | 160 | 170 |
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| Temperature of absorbent (° C) |
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SUPER ABSORPTION
Heating cycle
In the absorption heating cycle (Figure 10), the unit is essentially acting as a | heat transfer tubes removes the sensible heat of the condensed refrigerant |
boiler. Diluted solution is heated in the high temperature generator releasing | and transfers the heat to the hot water loop. The condensed refrigerant is |
refrigerant vapor from the absorbent. | mixed with the intermediate solution creating diluted solution. The diluted |
The refrigerant vapor flows to the absorber/evaporator and condenses on | solution is pumped back to the high temperature generator where the cycle |
the heat transfer tubes of the evaporator. The water through the evaporator | is started again. |
Figure 10. Heating cycle |
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Condenser | Exhaust Gas |
Low Temperature Generator |
Absorber |
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A Valve | High Temperature |
Evaporator | Generator |
Hot Water
Burner
C
Valve
Refrigerant Pump | Purge Unit |
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| Heat Exchanger |
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| Absorbent Pump |
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| Intermediate Solution |
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| Liquid Refrigerant |
| Hot Water |
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| Open |
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| Diluted Solution |
| Refrigerant Vapor |
| Close |
16 | 17 |