Adolph geiger
    101.
    发明授权

    公开(公告)号:US600067A

    公开(公告)日:1898-03-01

    申请号:US600067D

    CPC classification number: B01J3/04

    robie
    102.
    发明授权
    robie 失效

    公开(公告)号:US560327A

    公开(公告)日:1896-05-19

    申请号:US560327D

    CPC classification number: B01J3/04

    Dental vulcanizer
    103.
    发明授权

    公开(公告)号:US487647A

    公开(公告)日:1892-12-06

    申请号:US487647D

    CPC classification number: B01J3/04

    Dental vulcanizer
    105.
    发明授权

    公开(公告)号:US411449A

    公开(公告)日:1889-09-24

    申请号:US411449D

    CPC classification number: B01J3/04

    Soda-water apparatus
    106.
    发明授权

    公开(公告)号:US264586A

    公开(公告)日:1882-09-19

    申请号:US264586D

    CPC classification number: B01J3/04

    Method and System for Steamcracking
    108.
    发明公开

    公开(公告)号:US20240158702A1

    公开(公告)日:2024-05-16

    申请号:US18548889

    申请日:2022-03-08

    Applicant: LINDE GMBH

    CPC classification number: C10G9/36 B01J3/04

    Abstract: A method of steam cracking using a steam cracking system includes a first steam cracking furnace unit or a plurality of first steam cracking furnace units and a second steam cracking furnace unit or a plurality of second steam cracking furnace units. The first steam cracking furnace unit or each of the plurality of first steam cracking furnace units comprises one or more fired steam cracking furnaces. The second steam cracking furnace unit or each of the plurality of second steam cracking furnace units comprises one or more electric steam cracking furnaces. The first steam cracking furnace unit or each of the plurality of first steam cracking furnace units further includes means for preheating at least a part of combustion air provided to its fired steam cracking furnace or furnaces to a temperature level of at least 100° C.

    PROCESS FOR BENEFICIATING AND CLEANING BIOMASS
    109.
    发明公开

    公开(公告)号:US20230348805A1

    公开(公告)日:2023-11-02

    申请号:US18219479

    申请日:2023-07-07

    Abstract: A process for cleaning and beneficiating biomass is described which may allow removal of entrained salts and light volatiles from biomass materials. The process may also minimize energy use through capturing steam and flue gases for re-use. The process may generally comprise the following steps: prewashing and/or preheating a biomass, pressurizing the biomass in a steam explosion vessel, rapidly depressurizing the steam explosion vessel, releasing the steam from the steam explosion vessel entrained with fine lignin-enriched particles into a cyclone-type gas expansion vessel, routing the steam from the gas expansion vessel to the input hopper, subjecting the biomass to a second washing step, mechanically removing a portion of the water from the biomass, and evaporatively heating the biomass.

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