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    Process for hydrotreatment of a fuel gas stream containing more than 4% olefins
    62.
    发明授权
    Process for hydrotreatment of a fuel gas stream containing more than 4% olefins 有权

    公开(公告)号：US10597593B2

    公开(公告)日：2020-03-24

    申请号：US16301539

    申请日：2017-09-11

    Applicant: Haldor Topsøe A/S

    Inventor： Jens Michael Poulsen ,  Lene Boas ,  Max Thorhauge

    IPC: C10G70/02 ,  C10G45/00

    Abstract: A process for the hydrotreatment of a fuel gas stream containing up to 15% olefins comprises the steps of introducing the fuel gas stream into at least one co-current reactor, where the stream is split into two flow fractions, of which one fraction is routed through an olefin treatment section, while the other fraction is routed through another section, subjecting the sections to heat exchange, combining the two flows, thereby equalizing temperatures and compositions, cooling the combined flow over a heat exchanger and reacting the combined flow to equilibrium in an adiabatic hydrotreatment reactor. A second co-current reactor with intercooling arranged in series after the first cocurrent reactor and before the final adiabatic reactor is used if the fuel gas stream contains more than 8% olefins.

    HYDROISOMERIZATION CATALYST
    64.
    发明申请
    HYDROISOMERIZATION CATALYST 审中-公开

    公开(公告)号：US20200048565A1

    公开(公告)日：2020-02-13

    申请号：US16492222

    申请日：2018-03-13

    Applicant: HALDOR TOPSØE A/S

    Inventor： Marie GRILL

    IPC: C10G45/64 ,  B01J29/74 ,  B01J35/00 ,  B01J37/02 ,  B01J37/18

    Abstract: The present disclosure relates to a precursor for a catalytically active material or a catalytically active material comprising platinum, a molecular sieve and a metal oxide support, characterized in at least 80%, 90% or 95% of said platinum being dispersed on said molecular sieve and at least 80%, 90% or 95% of said platinum being dispersed in clusters having a size below 2 nm or 1 nm, as well as a method of producing such materials and process for hydroisomerization involving such materials. The disclosure has the associated benefit of such a catalytically active material being highly active and selective towards hydroisomerization.

    Methanol synthesis process layout for large production capacity
    66.
    发明授权
    Methanol synthesis process layout for large production capacity 有权

    公开(公告)号：US10478798B2

    公开(公告)日：2019-11-19

    申请号：US16083549

    申请日：2017-03-23

    Applicant: Haldor Topsøe A/S

    Inventor： Hassan Modarresi

    IPC: B01J8/06 ,  B01J19/24 ,  C07C29/152 ,  B01J8/02

    Abstract: A process layout for large scale methanol synthesis comprises one or more boiling water reactors and one or more radial flow reactors in series, the boiling water reactor(s) being fed with approximately fresh make-up syngas. The methanol synthesis loop comprises a make-up gas compressor K1, a recycle gas compressor K2, two or more boiling water converters for methanol synthesis (A1, A2, . . . ), a radial flow converter (B) for methanol synthesis, a steam drum (V1), a high pressure separator (V2), a low pressure separator (V3), feed effluent heat exchangers (E1 and E2), a wash column (C), an air cooler (E3) and a water cooler (E4).

    CO Rich Synthesis Gas Production
    69.
    发明申请
    CO Rich Synthesis Gas Production 审中-公开

    公开(公告)号：US20190151813A1

    公开(公告)日：2019-05-23

    申请号：US16308677

    申请日：2017-06-07

    Applicant: HALDOR TOPSØE A/S

    Inventor： Peter Mølgaard MORTENSEN ,  Martin ØSTBERG ,  Per Juul DAHL

    IPC: B01J8/04 ,  B01J8/06 ,  B01J19/00 ,  C01B3/48 ,  C10K3/02

    Abstract: The invention relates to a chemical reactor and reformer tubes for reforming a first feed stream comprising a hydrocarbon gas and steam. The chemical reactor comprises a shell with a heat source and one or more reformer tubes. The reformer tube is arranged to house catalyst material and is arranged to being heated by the heat source. The reformer tube comprises a first inlet for feeding said first feed stream into a first reforming reaction zone of the reformer tube, and a feed conduct arranged to allow a second feed stream into a second reforming reaction zone of the reformer tube. The second reforming reaction zone is positioned downstream of the first reforming reaction zone. The feed conduct is configured so that the second feed stream is only in contact with catalyst material in the second reforming reaction zone. The invention also relates to a process of producing CO rich synthesis gas at low S/C conditions.

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