period one
Absorption Refrigeration Cycle
notes
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1 psia |
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| 1.5 psia | % |
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0.1 psia | $ |
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[0.69 kPa] |
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50°F | 100°F |
| 150°F | 200°F | LiBr solution | |||
[10°C] | [37.8°C] |
| [65.6°C] | [93.3°C] | Figure 20 | |||
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Starting at the absorber, the dilute lithium bromide solution leaves the absorber ($) at 105°F [40.6ºC] and 59% concentration. This solution passes through the heat exchanger, where it is preheated to 175°F [79.4°C] (%). (Notice that there is no change in concentration as the solution passes through the heat exchanger.) In the generator, the solution absorbs heat from the steam or hot water flowing through the tubes. Initially, this only sensibly heats the solution to &, that is, the temperature of the solution increases while the concentration stays the same. At this point, the refrigerant begins to boil (vaporize) and separate from the solution. This increases the concentration of the lithium bromide solution as the temperature continues to increase (').
The concentrated solution ('), now at 215°F [101.7ºC] and 64.5%, passes through the heat exchanger where it is cooled to 135°F [57.2ºC] ((). This cooled, concentrated solution (() is then mixed with dilute solution from the absorber ($), and this intermediate solution ()) (118°F [47.8ºC] and 62% concentration) is pumped to the absorber spray trees. In the absorber, refrigerant vapor is absorbed by the intermediate solution, decreasing its concentration to 59%, while heat is transferred to the cooling water. The resulting cooled, dilute solution ($) returns to the generator to repeat the cycle.
This chart also can be used to demonstrate the operating pressures of the cycle. In this example, the
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