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Double-effect absorption refrigeration system

机译:双效吸收式制冷系统

摘要

PROBLEM TO BE SOLVED: To prevent a capability of freezing device from being reduced at an initial time of cooling operation, shorten a diluting operation time at the end of cooling operation and eliminate a circulation of absorbing liquid during an absorbing cycle when a heating operation is carried out. SOLUTION: An absorbing liquid of a low concentration is separated into an absorbing liquid of a middle concentration and a refrigerant by a high temperature regenerator 1 heated by a gas burner B, the absorbing liquid of the middle concentration is separated into an absorbing liquid of a high concentration and the refrigerant by a low temperature regenerator 2, a refrigerant liquid is dispersed in an evaporating coil 41 of an evaporator 4 to cool cold water within the evaporating coil 41 of the evaporator 4, the absorbing liquid of the high concentration is dispersed in a cooling coil 31 of an absorbing device 3, the refrigerant is absorbed to produce an absorbing liquid of a low concentration and further it is returned back to the high temperature regenerator 1 by an absorbing liquid pump P1. A bottom section 24 of a high concentration absorbing liquid receiving section 23 of the low temperature regenerator 2 and a bottom section 33 of the absorbing device 3 are connected by a high concentration absorbing liquid bypass flow passage 62 and then a bypass valve 61 is controlled to be opened at an initial time of cooling operation, an end of cooling operation and a heating time. When the bypass valve 61 is opened, the high concentration absorbing liquid in the low temperature regenerator 2 is flowed into the absorbing device 3.
机译:解决的问题:为了防止冷冻装置在制冷操作的初始时间降低能力,缩短制冷操作结束时的稀释操作时间,并在加热操作进行时的吸收循环中消除吸收液的循环。执行。解决方案:低浓度的吸收液通过由气体燃烧器B加热的高温再生器1分离为中等浓度的吸收液和制冷剂,中等浓度的吸收液分离为中等浓度的吸收液。高浓度的制冷剂和通过低温再生器2产生的制冷剂,制冷剂液体分散在蒸发器4的蒸发盘管41中,以冷却蒸发器4的蒸发盘管41内的冷水,高浓度的吸收液分散在在吸收装置3的冷却盘管31上,制冷剂被吸收以产生低浓度的吸收液,并且进一步通过吸收液泵P1返回到高温再生器1。低温蓄冷器2的高浓度吸收液接收部23的底部24和吸收装置3的底部33通过高浓度吸收液旁通流路62连接,然后控制旁通阀61,以将旁通阀61控制为高。在制冷操作的初始时间,制冷操作的结束和加热时间打开门。当旁通阀61打开时,低温再生器2中的高浓度吸收液流入吸收装置3。

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