中科微点-全球专利检索

  1. Login
  2. Sign Up

Search Results

6 records (took 0.02 seconds)

    HYDROCARBON SYNTHESIS METHODS, APPARATUS, AND SYSTEMS
    1.
    发明申请
    HYDROCARBON SYNTHESIS METHODS, APPARATUS, AND SYSTEMS 有权
    油气合成方法，装置和系统

    公开(公告)号：US20140046104A1

    公开(公告)日：2014-02-13

    申请号：US13934713

    申请日：2013-07-03

    Applicant: SarTec Corporation

    Inventor： Clayton V. McNeff ,  Larry C. McNeff ,  Daniel Thomas Nowlan ,  Bingwen Yan ,  Peter G. Greuel

    IPC: C10G3/00

    CPC classification number: C10G3/44 ,  B01J21/063 ,  B01J21/066 ,  B01J23/30 ,  B01J23/34 ,  B01J23/755 ,  B01J35/023 ,  B01J35/1014 ,  B01J35/1038 ,  B01J35/1061 ,  C10L1/04 ,  C10L9/086 ,  Y02P30/20

    Abstract: Embodiments of the invention include apparatus and systems for hydrocarbon synthesis and methods regarding the same. In an embodiment, the invention includes a process for creating a hydrocarbon product stream comprising reacting a reaction mixture in the presence of a catalyst inside of a reaction vessel to form a product mixture, the reaction mixture comprising a carbon source and water. The temperature inside the reaction vessel can be between 450 degrees Celsius and 600 degrees Celsius and the pressure inside the reaction vessel can be above supercritical pressure for water. In an embodiment, the invention includes an extrusion reactor system for creating a hydrocarbon product stream. The temperature inside the extrusion reactor housing between 450 degrees Celsius and 600 degrees Celsius. Pressure inside the reaction vessel can be above supercritical pressure for water. Other embodiments are also included herein.

    Abstract translation: 本发明的实施方案包括用于烃合成的装置和系统及其方法。 在一个实施方案中，本发明包括用于产生烃产物流的方法，包括在反应容器内部的催化剂存在下使反应混合物反应以形成产物混合物，所述反应混合物包含碳源和水。 反应容器内的温度可以在450摄氏度至600摄氏度之间，反应容器内的压力可能超过水的超临界压力。 在一个实施方案中，本发明包括用于产生烃产物流的挤出反应器系统。 挤压反应器内部的温度在450摄氏度到600摄氏度之间。 反应容器内的压力可超过水的超临界压力。 本文还包括其它实施例。

    Hydrocarbon synthesis methods, apparatus, and systems
    6.
    发明授权
    Hydrocarbon synthesis methods, apparatus, and systems 有权
    烃合成方法，装置和系统

    公开(公告)号：US09388345B2

    公开(公告)日：2016-07-12

    申请号：US13934713

    申请日：2013-07-03

    Applicant: SarTec Corporation

    Inventor： Clayton V. McNeff ,  Larry C. McNeff ,  Daniel Thomas Nowlan ,  Bingwen Yan ,  Peter G. Greuel

    IPC: C10G3/00 ,  C10L1/04 ,  C10L9/08 ,  B01J21/06 ,  B01J23/30 ,  B01J23/34 ,  B01J23/755 ,  B01J35/02 ,  B01J35/10

    CPC classification number: C10G3/44 ,  B01J21/063 ,  B01J21/066 ,  B01J23/30 ,  B01J23/34 ,  B01J23/755 ,  B01J35/023 ,  B01J35/1014 ,  B01J35/1038 ,  B01J35/1061 ,  C10L1/04 ,  C10L9/086 ,  Y02P30/20

    Abstract: Embodiments of the invention include apparatus and systems for hydrocarbon synthesis and methods regarding the same. In an embodiment, the invention includes a process for creating a hydrocarbon product stream comprising reacting a reaction mixture in the presence of a catalyst inside of a reaction vessel to form a product mixture, the reaction mixture comprising a carbon source and water. The temperature inside the reaction vessel can be between 450 degrees Celsius and 600 degrees Celsius and the pressure inside the reaction vessel can be above supercritical pressure for water. In an embodiment, the invention includes an extrusion reactor system for creating a hydrocarbon product stream. The temperature inside the extrusion reactor housing between 450 degrees Celsius and 600 degrees Celsius. Pressure inside the reaction vessel can be above supercritical pressure for water. Other embodiments are also included herein.

    Abstract translation: 本发明的实施方案包括用于烃合成的装置和系统及其方法。 在一个实施方案中，本发明包括用于产生烃产物流的方法，包括在反应容器内部的催化剂存在下使反应混合物反应以形成产物混合物，所述反应混合物包含碳源和水。 反应容器内的温度可以在450摄氏度至600摄氏度之间，反应容器内的压力可能超过水的超临界压力。 在一个实施方案中，本发明包括用于产生烃产物流的挤出反应器系统。 挤压反应器内部的温度在450摄氏度到600摄氏度之间。 反应容器内的压力可超过水的超临界压力。 本文还包括其它实施例。

Patent Agency Ranking