Cool double-effect lithium bromide absorption type refrigeration cycle system

An absorption refrigeration and circulation system technology, applied in refrigerators, adsorption machines, refrigeration and liquefaction, etc., can solve the problem that the outlet temperature of saturated dilute solution is low and the first cooling heat source cannot meet the application conditions of lithium bromide absorption refrigeration circulation system, etc. problems, to achieve remarkable energy-saving effects, reliable system performance, and high inlet temperature

Active Publication Date: 2014-12-03
HARBIN INST OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The present invention solves the problem that the outlet temperature of the saturated dilute solution of the second absorber and the temperature of the first cooling heat source are relatively low during the operation of the traditional lithium bromide absorption refrigeration cycle system, so that the relatively high temperature of the first cooling heat source cannot satisfy lithium bromide absorption. In order to solve the problem of the application conditions of the refrigerating cycle system, a cold double-effect lithium bromide absorption refrigerating cycle system is provided.

Method used

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  • Cool double-effect lithium bromide absorption type refrigeration cycle system
  • Cool double-effect lithium bromide absorption type refrigeration cycle system
  • Cool double-effect lithium bromide absorption type refrigeration cycle system

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specific Embodiment approach 1

[0041] 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 first throttling expansion device 8, a second throttling expansion device 9, a first A solution pump 10, a first refrigerant water vapor pipeline 11, a first refrigerant water passage 12, a second refrigerant water passage 13, a second refrigerant water vapor pipeline 15, a second concentrated solution pipeline 16, a The second dilute solution pipeline 17, the first dilute solution pipeline 18 and the first concentrated solution pipeline 19, the generator 1 communicates with the condenser 2 through the first refrigerant water vapor pipeline 11, and the refrigerant water passage of the condenser 2 Divided into two paths, one of which: the condenser 2 communicates with the evaporator 3 through the first refrigerant water passage 12, the first throttling expansion device 8 is arrange...

specific Embodiment approach 2

[0046] Specific implementation mode two: combination Figure 2 to Figure 5 Describe this embodiment, the difference between this embodiment and specific embodiment one is that it also adds a solution heat exchanger, and the solution heat exchanger is arranged on the first dilute solution pipeline 18 and the first concentrated solution pipeline 19 or the second On the concentrated solution pipeline 16 and the second dilute solution pipeline 17. The dilute solution flowing into the generator 1 is heat-exchanged through the solution heat exchanger, and the concentrated and dilute solutions flowing into and out of the generator 1, the second absorber 5 or the first absorber 4 are exchanged through the solution heat exchanger, This improves the efficiency of the refrigeration cycle. Other components and connections are the same as those in the first embodiment.

specific Embodiment approach 3

[0047] Specific implementation mode three: combination figure 2 Describe this embodiment, the solution heat exchanger of this embodiment adopts the first solution heat exchanger 6, the first solution heat exchanger 6 is located between the first solution pump 10 and the generator 1, and the first solution heat exchanger 6 It is arranged on the first dilute solution pipeline 18 and the first concentrated solution pipeline 19 . The dilute solution flowing into the generator 1 is heat-exchanged in the first solution heat exchanger 6, and through the first solution heat exchanger 6, the concentrated and dilute solutions flowing into and out of the generator 1 are exchanged heat, thereby improving the refrigeration cycle s efficiency. Other components and connections are the same as those in the second embodiment.

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Abstract

The invention relates to a cool double-effect lithium bromide absorption type refrigeration cycle system. A generator is communicated with a condenser, the condenser is communicated with an evaporator through a first refrigerant water passage, one end of a second refrigerant water passage is communicated with the condenser, the other end of the second refrigerant water passage passes through a first absorber to be communicated with a second absorber, the first absorber is communicated with the evaporator through a second refrigerant water vapor pipeline, one end of a first dilute solution pipeline and one end of a second dilute solution pipeline are communicated with the second absorber, the other ends of the first dilute solution pipeline and the second dilute solution pipeline are communicated with the generator, one end of a second concentrated solution pipeline is communicated with the first absorber, the other end of the second concentrated solution pipeline is communicated with a first concentrated solution pipeline, one end of the second dilute solution pipeline is communicated with the first absorber, the other end of the second dilute solution pipeline is communicated with the first dilute solution pipeline, a first solution pump is arranged on the first dilute solution pipeline, the generator is heated by a first high-altitude heat source, the condenser is cooled by a second cooling heat source, the evaporator is heated by a low-altitude heat source, and the absorbers are cooled by a first cooling heat source. The system is used in an absorption type water source heat pump system.

Description

technical field [0001] The invention relates to an absorption refrigeration cycle system, in particular to a cold double-effect lithium bromide absorption refrigeration cycle system. Background technique [0002] Traditional absorption refrigeration cycle systems such as Figure 23 As shown, it is mainly composed of a generator 1, a condenser 2, an evaporator 3, a second absorber 5, a solution heat exchanger 6, a first solution pump 10 and connected pipelines. Under the action of an external heat source, the generator 1 concentrates the lithium bromide solution in it to generate high-temperature and high-pressure refrigerant water vapor, which enters the condenser 2 through the first refrigerant water vapor pipeline 11 to condense, and the condensed low-temperature The refrigerant water enters the evaporator 3 through the first refrigerant water channel 12 after throttling and depressurizing through the first throttling expansion device 8, and in the evaporator 3, the refrig...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F25B29/00F25B15/06
CPCY02A30/27Y02B30/62
Inventor 张承虎李亚平闫艳艳
Owner HARBIN INST OF TECH
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