会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 25. 发明授权
    • Method and apparatus for the indirect cooling of hot gases,
particularly, coke oven gases
    • 用于间接冷却热气体,特别是焦炉气体的方法和装置
    • US4045970A
    • 1977-09-06
    • US732958
    • 1976-10-15
    • Kurt Tippmer
    • Kurt Tippmer
    • B01J19/00C10B27/00C10K1/04F25B15/16F25B27/00F25D17/06F25B7/00F25D17/02
    • C10B27/00F25B15/16F25B27/00
    • A method for the indirect cooling of hot gases, particularly, coke oven gases using a gas cooler having a cooling chamber with three different heat exchangers arranged therein, comprises directing the gases to be cooled through first one of the heat exchangers while circulating a coolant through the first heat exchanger which comprises a heater agent taken from the desorber stage of an absorber-desorber-type refrigerating machine. The gases are then directed through the second heat exchanger while circulating ordinary cooling water therethrough and, thereafter, the gases are directed through a third heat exchanger while the heating agent from an evaporator stage of the refrigerating machine is circulated through the third heat exchanger. The apparatus includes a gas cooler housing having the various first, second and third heat exchangers therein, and with a refrigerating machine connected in a circuit for supplying a higher temperature transfer medium to the first heat exchanger and a coolant medium below the temperature of the cooling water to the third heat exchanger.
    • 使用具有布置在其中的具有三个不同热交换器的冷却室的气体冷却器间接冷却热气体,特别是焦炉气体的方法包括通过第一个热交换器引导要冷却的气体,同时使冷却剂循环 所述第一热交换器包括从吸收器 - 解吸器型制冷机的解吸器阶段获取的加热剂。 然后将气体引导通过第二热交换器,同时使普通的冷却水循环通过,之后气体被引导通过第三热交换器,同时来自制冷机的蒸发器级的加热剂循环通过第三热交换器。 该装置包括其中具有各种第一,第二和第三热交换器的气体冷却器壳体,以及连接在用于向第一热交换器供应较高温度的转移介质的回路中的冷冻机以及低于冷却温度的冷却剂介质 水到第三换热器。
    • 27. 发明公开
    • ENERGY STORAGE SYSTEM
    • EP3400375A1
    • 2018-11-14
    • EP17700304.3
    • 2017-01-04
    • University of Newcastle Upon Tyne
    • BAO, HuashanROSKILLY, Anthony, Paul
    • F01K25/00F01K3/12
    • F01K25/08F01K3/12F01K25/00F25B15/16F25B17/08F25B27/02F25B2400/14
    • There is disclosed an energy storage system. In particular, there is disclosed a chemisorption based energy storage system, able to provide electricity, heating or cooling depending on the desired energy output. The energy storage system includes a first chemical reactor containing a first sorbent material and a second chemical reactor containing a second sorbent material. The first and second chemical reactors are in mutual fluid connection such that a refrigerant fluid can flow from the first chemical reactor to the second chemical reactor, and from the second chemical reactor to the first chemical reactor. The first and second chemical reactors are further provided with means for putting heat in to, or taking heat out of, the first and/or the second chemical reactors. A heat exchanger module is also provided. The heat exchanger module is configured to select from a plurality of available heat sources, a heat source having the highest temperature and an expander module selectively connected to the first chemical reactor and the second chemical reactor via the heat exchanger module. The heat source is arranged to heat the refrigerant fluid prior to the refrigerant fluid passing through the expander module, and the heat exchanger is configured to recover a surplus heat from the highest temperature heat source. The expander module is configured to expand the refrigerant fluid. The means for putting heat in to, or taking heat out of, the first and/or the second chemical reactors provides a flow of refrigerant fluid between the expander module and the first and second chemical reactors, and wherein the expander module is operable to expand the refrigerant fluid to provide a variable work output depending on energy storage requirements.