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Low temp. evapn. by heat pump - incorporating heat transfer from condenser to evaporator by compressor with expansion valve maintaining pressure difference

机译:低温逃避通过热泵-通过冷凝器将冷凝器到蒸发器的热传递与保持压力差的膨胀阀结合在一起

摘要

A plant for evapn. at low temp., partic. for concentrating solns. which are sensitive to temp. e.g. pharmaceutical and food prods., comprises two heat exchangers and a heat pump. The first exchanger is for the evapn. of the soln. being processed. The second is for the condensn. of the vapour sepd. from the soln. The heat pump consists of a compressor and an expansion valve. The compressor takes in a heat transfer fluid which has passed through the condenser and forces it through the evaporator. The expansion valve maintains a fixed pressure difference over the circuit returning the heat transfer fluid from the evaporator to the condenser. The heat transfer fluid is any refrigerating fluid, e.g. ammonia or dichlorfluormethane. The plant consumes less energy than existing plants in which the condenser water is sub-cooled by a refrigerating machine or in which the vapour is recompressed by a jet system. Only electrical energy is required so that expenditure on installating a boiler is avoided. The cost of energy is low, 50-100 kWh. per tonne of water evaporated, four to ten times lower than that of a conventional evaporator operating at the same temp.
机译:蒸发植物。在低温下,颗粒状。用于浓缩溶液。对温度敏感。例如药品和食品产品包括两个热交换器和一个热泵。第一个交换器用于蒸发。的正在处理。第二个是冷凝。的蒸气从Soln。热泵由压缩机和膨胀阀组成。压缩机吸收传热流体,该传热流体已通过冷凝器并迫使其通过蒸发器。膨胀阀在回路上保持固定的压差,该回路将传热流体从蒸发器返回到冷凝器。传热流体是任何制冷流体,例如。氨或二氯氟甲烷。与现有设备相比,该设备消耗的能源更少,在现有设备中,冷凝器水通过制冷机进行过冷或蒸汽通过喷射系统进行再压缩。仅需要电能,从而避免了安装锅炉的费用。能源成本低,为50-100千瓦时。每吨蒸发的水,比在相同温度下运行的传统蒸发器低四到十倍。

著录项

  • 公开/公告号FR2419093A1

    专利类型

  • 公开/公告日1979-10-05

    原文格式PDF

  • 申请/专利权人 KESTNER APPAREILS EVAPORATEURS;

    申请/专利号FR19780006356

  • 发明设计人

    申请日1978-03-06

  • 分类号B01D1/00;F25B29/00;

  • 国家 FR

  • 入库时间 2022-08-22 19:30:35

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