知搜-全球专利检索

  1. Login
  2. Sign Up

Search Results

16 records (took 0.015 seconds)

    CATALYTIC REACTOR FOR THE CONVERSION OF CARBON DIOXIDE AND HYDROGEN TO SYNGAS
    3.
    发明公开
    CATALYTIC REACTOR FOR THE CONVERSION OF CARBON DIOXIDE AND HYDROGEN TO SYNGAS 审中-公开

    公开(公告)号：US20240058778A1

    公开(公告)日：2024-02-22

    申请号：US18445557

    申请日：2023-10-12

    Applicant: Infinium Technology, LLC

    Inventor： Dennis Schuetzle ,  Robert Schuetzle ,  Anja Rumplecker Galloway ,  Orion Hanbury ,  James Bucher ,  Ramer Rodriguez

    IPC: B01J8/00 ,  B01J8/02 ,  C01B3/06 ,  C01B5/00 ,  C01B32/40 ,  C01B32/50

    CPC classification number: B01J8/004 ,  B01J8/008 ,  B01J8/0285 ,  C01B3/06 ,  C01B5/00 ,  C01B32/40 ,  C01B32/50

    Abstract: The present invention is generally directed to a reactor for the production of low-carbon syngas from captured carbon dioxide and renewable hydrogen. The hydrogen is generated from water using an electrolyzer powered by renewable electricity or from any other method of low-carbon hydrogen production. The improved catalytic reactor is energy efficient and robust when operating at temperatures up to 1800° F. Carbon dioxide conversion efficiencies are greater than 75% with carbon monoxide selectivity of greater than 98%. The catalytic reactor is constructed of materials that are physically and chemically robust up to 1800° F. As a result, these materials are not reactive with the mixture of hydrogen and carbon dioxide or the carbon monoxide and steam products. The reactor materials do not have catalytic activity or modify the physical and chemical composition of the conversion catalyst. Electrical resistive heating elements are integrated into the catalytic bed of the reactor so that the internal temperature decreases by no more than 100° F. from the entrance at any point within the reactor. The catalytic process exhibits a reduction in performance of less than 0.5% per 1000 operational hours.

Patent Agency Ranking