Process for production of H
    1.
    发明授权

    公开(公告)号:US12122967B1

    公开(公告)日:2024-10-22

    申请号:US17073648

    申请日:2020-10-19

    IPC分类号: C10J3/10 C10J3/16 C10J3/72

    摘要: Materials, methods to prepare, and methods of use for producing an H2 rich synthesis gas stream from coal free of nitrogen is described. One embodiment of the method comprises. The method includes an oxygen carrier at least partially reduced using a fuel in a reactor forming a reduced metal oxide comprised of first series—3d block-transition metals or mixture thereof. The reduced metal oxide is reacted with the solid fuel/steam to produce H2 and CO2/CO in the reactor; and the reduced metal oxide is added separately or simultaneously with a solid fuel while not impregnating the solid fuel with the reduced metal oxide.

    Method for cooling a hot synthesis gas
    5.
    发明申请

    公开(公告)号:US20180050910A1

    公开(公告)日:2018-02-22

    申请号:US15560766

    申请日:2016-03-24

    发明人: Michael DICHAND

    IPC分类号: C01B3/54 C10K1/04

    摘要: In a method for cooling a hot synthesis gas containing at least one condensable constituent part, in particular tar, during which the synthesis gas in a multi-stage cooling process passes through a first cooling stage, a second cooling stage and a third cooling stage one after the other and the synthesis gas after an at least partial cooling is at least subjected to a separation step for separating the at least one condensable constituent part, the synthesis gas is cooled in the first cooling stage to a temperature above the condensation temperature of the at least one condensable constituent part and the second cooling stage comprises the recirculating of a part quantity of synthesis gas branched off after the third cooling stage and the at least one separation step into the synthesis gas flow.

    SYSTEM AND METHOD FOR GASIFICATION

    公开(公告)号:US20170275544A1

    公开(公告)日:2017-09-28

    申请号:US15080043

    申请日:2016-03-24

    摘要: A system includes a first reactor that may gasify a first feed to generate a first syngas. The first feed has a first particle size distribution (PSD1). The system also includes a second reactor that may receive the first feed, a second feed, and at least a portion of the first syngas. The second reactor may gasify the second feed to generate additional syngas, and the second feed has a second particle size distribution (PSD2) that is different from the first PSD. The second reactor includes an elutriation zone disposed on a first end of the second reactor. The elutriation zone may receive the first and second feed. The second reactor also includes a fluidized bed disposed at a second end of the second reactor that is substantially opposite the first end. The fluidized bed is fluidly coupled to the first reactor and may receive the portion of the first syngas via a syngas inlet. The system also includes a gas-solids separation section fluidly coupled to the first and second reactors. The gas-solids separation section may receive the first feed and partially reacted particles of the second feed from the elutriation zone and may feed a combined feed consisting of the first feed and the partially reacted particles of the second feed to the first reactor.