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热词
    • 1. 发明授权
    • Heat engine and method for operating the same
    • 热机及其运行方法
    • US08459030B2
    • 2013-06-11
    • US12571025
    • 2009-09-30
    • Matthias FinkenrathGabor AstMichael Adam BartlettVittorio Tola
    • Matthias FinkenrathGabor AstMichael Adam BartlettVittorio Tola
    • F01K13/00F01K25/08F01K25/00F01K23/04B01D47/00B01D53/56
    • F01K25/10F01K9/003Y02E20/326
    • A process fluid cooler can extract thermal energy from a process fluid including carbon dioxide. An absorber can transfer carbon dioxide from the process fluid to a removal fluid. A reboiler can heat the removal fluid so as to cause carbon dioxide to be released from the removal fluid and outputted as part of a reboiler output stream. The reboiler can also output a heating fluid. A stripper condenser can extract thermal energy from the reboiler output stream so as to cause condensation of water associated with the reboiler output stream and to remove carbon dioxide therefrom. A compression system can remove thermal energy from carbon dioxide received from the stripper condenser. A heat engine can be configured to operate according to an organic Rankine cycle, receiving thermal energy from the heating fluid and/or extracted at the process fluid cooler, at the stripper condenser, and/or at the compression system.
    • 工艺流体冷却器可以从包括二氧化碳的工艺流体中提取热能。 吸收器可将二氧化碳从工艺流体转移至去除流体。 再沸器可以加热去除流体,以便使二氧化碳从去除流体中释放并作为再沸器输出流的一部分输出。 再沸器还可以输出加热流体。 汽提冷凝器可以从再沸器输出流中提取热能,以使与再沸器输出流相关联的水冷凝并从其中除去二氧化碳。 压缩系统可以从汽提冷凝器接收的二氧化碳中去除热能。 热引擎可以被配置为根据有机朗肯循环操作,从加热流体接收热能和/或在过程流体冷却器处,在汽提冷凝器处和/或在压缩系统处提取。
    • 2. 发明申请
    • HEAT ENGINE AND METHOD FOR OPERATING THE SAME
    • 热发动机及其运行方法
    • US20110072820A1
    • 2011-03-31
    • US12571025
    • 2009-09-30
    • Matthias FinkenrathGabor AstMichael Adam BartlettVittorio Tola
    • Matthias FinkenrathGabor AstMichael Adam BartlettVittorio Tola
    • F02G5/02F02G1/043F01K23/02F01K25/08
    • F01K25/10F01K9/003Y02E20/326
    • A process fluid cooler can extract thermal energy from a process fluid including carbon dioxide. An absorber can transfer carbon dioxide from the process fluid to a removal fluid. A reboiler can heat the removal fluid so as to cause carbon dioxide to be released from the removal fluid and outputted as part of a reboiler output stream. The reboiler can also output a heating fluid. A stripper condenser can extract thermal energy from the reboiler output stream so as to cause condensation of water associated with the reboiler output stream and to remove carbon dioxide therefrom. A compression system can remove thermal energy from carbon dioxide received from the stripper condenser. A heat engine can be configured to operate according to an organic Rankine cycle, receiving thermal energy from the heating fluid and/or extracted at the process fluid cooler, at the stripper condenser, and/or at the compression system.
    • 工艺流体冷却器可以从包括二氧化碳的工艺流体中提取热能。 吸收器可将二氧化碳从工艺流体转移至去除流体。 再沸器可以加热去除流体,以便使二氧化碳从去除流体中释放并作为再沸器输出流的一部分输出。 再沸器还可以输出加热流体。 汽提冷凝器可以从再沸器输出流中提取热能,以使与再沸器输出流相关联的水冷凝并从其中除去二氧化碳。 压缩系统可以从汽提冷凝器接收的二氧化碳中去除热能。 热引擎可以被配置为根据有机朗肯循环操作,从加热流体接收热能和/或在过程流体冷却器处,在汽提冷凝器处和/或在压缩系统处提取。