利索-全球专利检索

  1. 登录
  2. 注册

搜索结果

69 条记录 (耗时 0.023 秒)

    ABSORPTION HEAT PUMP FOR EXTREME OPERATING CONDITIONS
    3.
    发明申请
    ABSORPTION HEAT PUMP FOR EXTREME OPERATING CONDITIONS 审中-公开
    吸收热泵用于极端操作条件

    公开(公告)号：US20100275622A1

    公开(公告)日：2010-11-04

    申请号：US12768497

    申请日：2010-04-27

    申请人： Marco GUERRA

    发明人： Marco GUERRA

    IPC分类号： F25B15/00 ,  F25B13/00

    CPC分类号： F25B15/04 ,  F25B30/04 ,  F25B2315/002 ,  Y02A30/277 ,  Y02B30/62

    摘要： An absorption heat pump with a system for improving its efficiency under extreme conditions by bleeding off refrigerant downstream of the condenser and mixing it with the rich solution after this latter has been at least partially heated by the absorber and before it is fed into the desorber.

    摘要翻译： 一种吸收式热泵，其具有在极端条件下通过将冷凝器下游的制冷剂排出并将其与富溶液混合的系统来提高其效率，后者已经被吸收器至少部分地被吸收器加热并且在其被送入解吸器之前。

    Absorption cycle with integrated heating system
    8.
    发明申请
    Absorption cycle with integrated heating system 失效
    集成供暖系统的吸收循环

    公开(公告)号：US20020069665A1

    公开(公告)日：2002-06-13

    申请号：US09734538

    申请日：2000-12-12

    发明人： Donald C. Erickson

    IPC分类号： F25B027/00

    CPC分类号： F25B15/02 ,  F01K23/10 ,  F01K25/065 ,  F02C6/18 ,  F25B33/00 ,  F25B2315/002 ,  Y02B30/625

    摘要： An absorption system powered by low temperature heat for producing at least one of refrigeration and power is disclosed, wherein a low-pressure drop heat reclaimer 1 reclaims heat from the source into a heating agent, which in turn supplies heat to the absorption cycle desorber 5 via internal coils 7. The extra temperature differential normally present in closed cycle heating systems is avoided by using the absorption working fluid as the heating agent, in an integrated system.

    摘要翻译： 公开了一种由低温热驱动的用于产生制冷和动力中的至少一种的吸收系统，其中低压降热回收器1将热量从源回收到加热剂中，加热剂又将热量供应到吸收循环解吸器5 通过内部线圈7.通常在封闭循环加热系统中存在的额外的温差通过在集成系统中使用吸收工作流体作为加热剂来避免。

    Heat cascading regenerative sorption heat pump
    10.
    发明授权
    Heat cascading regenerative sorption heat pump 失效

    公开(公告)号：US5463879A

    公开(公告)日：1995-11-07

    申请号：US177291

    申请日：1994-01-04

    申请人： Jack A. Jones

    发明人： Jack A. Jones

    IPC分类号： F25B15/00 ,  F25B15/02 ,  F25B17/08 ,  F17C11/00

    CPC分类号： F25B17/086 ,  F25B15/006 ,  F25B15/02 ,  F25B17/083 ,  F25B2315/002 ,  Y02B30/52 ,  Y02B30/62 ,  Y02B30/64

    摘要： A simple heat cascading regenerative sorption heat pump process with rejected or waste heat from a higher temperature chemisorption circuit ("HTCC") powering a lower temperature physisorption circuit ("LTPC") which provides a 30% total improvement over simple regenerative physisorption compression heat pumps when ammonia is both the chemisorbate and physisorbate, and a total improvement of 50% or more for LTPC having two pressure stages. The HTCC contains ammonia and a chemisorbent therefor contained in a plurality of canisters, a condenser-evaporator-radiator system, and a heater, operatively connected together. The LTPC contains ammonia and a physisorbent therefor contained in a plurality of compressors, a condenser-evaporator-radiator system, operatively connected together. A closed heat transfer circuit ("CHTC") is provided which contains a flowing heat transfer liquid ("FHTL") in thermal communication with each canister and each compressor for cascading heat from the HTCC to the LTPC. Heat is regenerated within the LTPC by transferring heat from one compressor to another. In one embodiment the regeneration is performed by another CHTC containing another FHTL in thermal communication with each compressor. In another embodiment the HTCC powers a lower temperature ammonia water absorption circuit ("LTAWAC") which contains a generator-absorber system containing the absorbent, and a condenser-evaporator-radiator system, operatively connected together. The absorbent is water or an absorbent aqueous solution. A CHTC is provided which contains a FHTL in thermal communication with the generator for cascading heat from the HTCC to the LTAWAC. Heat is regenerated within the LTAWAC by transferring heat from the generator to the absorber. The chemical composition of the chemisorbent is different than the chemical composition of the physisorbent, and the absorbent. The chemical composition of the FHTL is different than the chemisorbent, the physisorbent, the absorbent, and ammonia.