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    • 5. 发明申请
    • DIRECT EVAPORATOR APPARATUS AND ENERGY RECOVERY SYSTEM
    • 直接蒸发器装置和能量回收系统
    • US20110120129A1
    • 2011-05-26
    • US12624636
    • 2009-11-24
    • Thomas Johannes FreyMatthew Alexander Lehar
    • Thomas Johannes FreyMatthew Alexander Lehar
    • F01K25/08
    • F01K25/10F22B1/18F22B35/001F22B35/002
    • In one aspect, the present invention provides a direct evaporator apparatus for use in an organic Rankine cycle energy recovery system, comprising: (a) a housing comprising a heat source gas inlet, and a heat source gas outlet, the housing defining a heat source gas flow path from the inlet to the outlet; and (b) a heat exchange tube disposed within the heat source flow path, the heat exchange tube being configured to accommodate an organic Rankine cycle working fluid, the heat exchange tube comprising a working fluid inlet and a working fluid outlet. The direct evaporator apparatus is configured such that at least a portion of a heat source gas having contacted at least a portion of the heat exchange tube is in thermal contact with heat source gas entering the direct evaporator apparatus via the heat source gas inlet. An organic Rankine cycle energy recovery system and a method of energy recovery are also provided.
    • 一方面,本发明提供了一种用于有机朗肯循环能量回收系统的直接蒸发器装置,包括:(a)壳体,包括热源气体入口和热源气体出口,所述壳体限定热源 从入口到出口的气体流动路径; 和(b)设置在所述热源流路内的热交换管,所述热交换管构造成容纳有机朗肯循环工作流体,所述热交换管包括工作流体入口和工作流体出口。 直接蒸发器装置被配置为使得至少部分热源气体与热交换管的至少一部分接触,与通过热源气体入口进入直接蒸发器装置的热源气体热接触。 还提供了有机朗肯循环能量回收系统和能量回收方法。
    • 6. 发明申请
    • ORGANIC RANKINE CYCLE SYSTEM AND METHOD
    • 有机RANKINE循环系统和方法
    • US20100281865A1
    • 2010-11-11
    • US12436269
    • 2009-05-06
    • Matthew Alexander LeharSebastian W. FreundGiacomo Seghi
    • Matthew Alexander LeharSebastian W. FreundGiacomo Seghi
    • F01K25/00
    • F01K23/10F01K25/08
    • An ORC system configured to limit temperature of a working fluid below a threshold temperature is provided. The ORC system includes a heat source configured to convey a waste heat fluid. The ORC system also includes a heat exchanger coupled to the heat source. The heat exchanger includes an evaporator configured to receive the waste heat fluid from the heat source and vaporize the working fluid, wherein the evaporator is further configured to allow heat exchange between the waste heat fluid and the vaporized working fluid at an elevated temperature and further produce an evaporator outlet flow including a lower temperature waste heat fluid. The heat exchanger also includes a superheater configured to receive the lower temperature waste heat fluid from the evaporator, wherein the superheater is further configured to allow heat exchange between the lower temperature waste heat fluid and a relatively higher temperature working fluid contained in the superheater and further produce a superheater outlet flow comprising an elevated temperature waste heat fluid. The heat exchanger further includes a preheater configured to receive the elevated temperature waste heat fluid from the superheater and allow heat exchange with a relatively lower temperature working fluid in a liquid state contained in the preheater.
    • 提供了一种被配置为将工作流体的温度限制在阈值温度以下的ORC系统。 ORC系统包括被配置为传送废热流体的热源。 ORC系统还包括耦合到热源的热交换器。 热交换器包括蒸发器,该蒸发器构造成从热源接收废热流体并蒸发工作流体,其中蒸发器进一步构造成允许废热流体和蒸发的工作流体在升高的温度下进行热交换,并进一步产生 包括较低温度废热流体的蒸发器出口流。 热交换器还包括过热器,其被配置为从蒸发器接收较低温度的废热流体,其中过热器进一步构造成允许低温废热流体与包含在过热器中的相对较高温度的工作流体之间的热交换 产生包括高温废热流体的过热器出口流。 热交换器还包括预热器,其构造成从过热器接收高温废热流体,并允许与包含在预热器中的处于液态的相对较低温度的工作流体进行热交换。