A cold double-effect lithium bromide jet absorption refrigeration cycle system
A technology of absorption refrigeration and circulation system, applied in refrigerators, refrigeration components, refrigeration and liquefaction, etc., can solve the problems of condensing pressure and condensing temperature cannot be increased independently, can not meet the application conditions of lithium bromide, etc.
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specific Embodiment approach 1
[0032] Specific implementation mode one: combine figure 1 Describe this embodiment, this embodiment includes a generator 1, a condenser 2, an evaporator 3, a first absorber 4, a second absorber 5, a solution heat exchanger 6, a first throttling expansion device 8, a second section Flow expansion device 9, first solution pump 10, first refrigerant water vapor pipeline 11, first refrigerant water passage 12, second refrigerant water passage 13, second refrigerant water vapor pipeline 15, second rich Solution pipeline 16, second dilute solution pipeline 17, first dilute solution pipeline 18, first concentrated solution pipeline 19, throttle valve 28, injector 29, boiler 30, first connecting pipe 31, second The connecting pipe 32, the liquid storage device 33, the refrigerant water pump 34 and the third connecting pipe 42, the refrigerant water passage of the condenser 2 is divided into three paths, one of which: the condenser 2 passes through the first refrigerant water passage ...
specific Embodiment approach 2
[0038] Specific implementation mode two: combination figure 2 Describe this embodiment, the difference between this embodiment and specific embodiment one is that it also adds a second solution heat exchanger 7, and the second solution heat exchanger 7 is arranged on the second concentrated solution pipeline 16 and the second dilute solution pipe on road 17. The second solution heat exchanger 7 enables heat exchange between the concentrated and dilute solutions flowing into and out of the first absorber 4, thereby improving the efficiency of the refrigeration cycle. Other components and connections are the same as those in the first embodiment.
specific Embodiment approach 3
[0039] Specific implementation mode three: combination image 3 Describe this embodiment, the difference between this embodiment and specific embodiment 1 is that it also adds a second solution heat exchanger 7, and the second solution heat exchanger 7 is located between the second dilute solution pipeline 17 and the second absorber 5 Between, and the second solution heat exchanger 7 is arranged on the first dilute solution pipeline 18 and the first concentrated solution pipeline 19 . The second solution heat exchanger 7 enables heat exchange between the concentrated and dilute solutions flowing into and out of the second absorber 5, thereby improving the efficiency of the refrigeration cycle. Other components and connections are the same as those in the second embodiment.
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