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29 条记录 (耗时 0.046 秒)

    Gradual oxidation with heat transfer
    1.
    发明授权
    Gradual oxidation with heat transfer 有权
    用热传递逐渐氧化

    公开(公告)号：US09353946B2

    公开(公告)日：2016-05-31

    申请号：US13417140

    申请日：2012-03-09

    申请人： Douglas Hamrin ,  Richard Martin ,  Jeffrey Armstrong

    发明人： Douglas Hamrin ,  Richard Martin ,  Jeffrey Armstrong

    IPC分类号： F23N5/00 ,  F23R3/00 ,  F02C9/40 ,  F23G7/06

    CPC分类号： F23N5/00 ,  F02C9/40 ,  F23C2202/10 ,  F23C2203/10 ,  F23C2203/20 ,  F23G7/066 ,  F23G2206/202 ,  F23R3/005 ,  F23R2900/00002 ,  Y02E20/366 ,  Y02T50/677

    摘要： Described herein are embodiments of systems and methods for oxidizing gases. In some embodiments, a reaction chamber is configured to receive a fuel gas and maintain the gas at a temperature within the reaction chamber that is above an autoignition temperature of the gas. The reaction chamber may also be configured to maintain a reaction temperature within the reaction chamber below a flameout temperature. In some embodiments, heat and product gases from the oxidation process can be used, for example, to drive a turbine, reciprocating engine, and injected back into the reaction chamber.

    摘要翻译： 这里描述了用于氧化气体的系统和方法的实施例。 在一些实施例中，反应室被配置为接收燃料气体并将气体保持在反应室内高于气体自燃温度的温度。 反应室也可以被配置为将反应室内的反应温度保持在熄火温度以下。 在一些实施例中，可以使用来自氧化过程的热和产物气体，例如驱动涡轮机，往复式发动机，并将其注入反应室。

    GRADUAL OXIDATION WITH HEAT CONTROL
    2.
    发明申请
    GRADUAL OXIDATION WITH HEAT CONTROL 审中-公开
    粗加工与热控制

    公开(公告)号：US20130236845A1

    公开(公告)日：2013-09-12

    申请号：US13417095

    申请日：2012-03-09

    申请人： Douglas HAMRIN ,  Steve LAMPE

    发明人： Douglas HAMRIN ,  Steve LAMPE

    IPC分类号： F27D7/00

    CPC分类号： F23C6/04 ,  F02C3/22 ,  F22B1/18 ,  F23C9/00 ,  F23C2202/10 ,  F23C2203/10 ,  F23C2203/30 ,  F23G5/46 ,  F23G7/066 ,  F23G2206/202 ,  F23R2900/00002 ,  Y02E20/366

    摘要： Described herein are embodiments of systems and methods for oxidizing gases. In some embodiments, a reaction chamber is configured to receive a fuel gas and maintain the gas at a temperature within the reaction chamber that is above an autoignition temperature of the gas. The reaction chamber may also be configured to maintain a reaction temperature within the reaction chamber below a flameout temperature. In some embodiments, heat and product gases from the oxidation process can be used, for example, to drive a turbine, reciprocating engine, and injected back into the reaction chamber.

    摘要翻译： 这里描述了用于氧化气体的系统和方法的实施例。 在一些实施例中，反应室被配置为接收燃料气体并将气体保持在反应室内高于气体自燃温度的温度。 反应室也可以被配置为将反应室内的反应温度保持在熄火温度以下。 在一些实施例中，可以使用来自氧化过程的热和产物气体，例如驱动涡轮机，往复式发动机，并将其注入反应室。

    High-temperature regenerator
    7.
    发明授权
    High-temperature regenerator 失效

    公开(公告)号：US5862679A

    公开(公告)日：1999-01-26

    申请号：US848117

    申请日：1997-04-28

    申请人： Makoto Nakamura ,  Atsushi Shitara ,  Hidetoshi Arima ,  Hitoshi Kanuma ,  Masahiro Furukawa ,  Eiichi Enomoto ,  Toshihiro Yamada

    发明人： Makoto Nakamura ,  Atsushi Shitara ,  Hidetoshi Arima ,  Hitoshi Kanuma ,  Masahiro Furukawa ,  Eiichi Enomoto ,  Toshihiro Yamada

    IPC分类号： F25B33/00

    CPC分类号： F25B33/00 ,  F23C2203/10 ,  F25B2333/003 ,  Y02E20/366

    摘要： In a high-temperature regenerator which has vertical liquid pipe groups in the proximity of which a combustion flame and combustion gas from a burner pass and a double can wall which communicates with upper and lower portions of liquid pipes forming the vertical liquid pipe groups and is arranged at a position of a furnace wall and which heats and concentrates a diluted absorption solution passing through the vertical liquid pipe groups and the double can wall, a solution inlet for sprinkling the diluted absorption solution in an open state is provided above liquid pipes arranged on a side opposite to the burner. Since the sprinkled diluted absorption solution collects the heat of an exhaust gas while it falls to increase its temperature, when it flows into the other liquid pipes, it boils immediately and its circulation flow is activated by boiling. Therefore, total heat transfer coefficient can be increased, a local rise in the temperature of the liquid pipe groups and the can wall can be avoided, and such inconvenience as a corrosion accident and the crystallization of a solution caused by this rise in temperature can be prevented.