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    MONITORING OF HEATED TUBES
    52.
    发明申请
    MONITORING OF HEATED TUBES 审中-公开

    公开(公告)号：US20200333274A1

    公开(公告)日：2020-10-22

    申请号：US16095736

    申请日：2017-05-03

    Applicant: HALDOR TOPSØE A/S

    Inventor： Søren Gyde Thomsen

    IPC: G01N25/72 ,  F28F27/00

    Abstract: A method and an apparatus for detailed continuous monitoring of the thermal environment for a tube or a plurality of tubes and calculation and prediction of remaining lifetime of said tubes.

    PROCESS FOR PURIFICATION OF HYDROCARBONS
    53.
    发明申请
    PROCESS FOR PURIFICATION OF HYDROCARBONS 审中-公开

    公开(公告)号：US20200332204A1

    公开(公告)日：2020-10-22

    申请号：US16643103

    申请日：2018-10-09

    Applicant: HALDOR TOPSØE A/S

    Inventor： Muhammad ILYAS ,  Liza LINDMARK ,  Ole Frej ALKILDE

    IPC: C10G53/08 ,  C10G67/14 ,  B01D53/14 ,  B01D53/18

    Abstract: Processes and equipment for purification of a sour hydrocarbon mixture or a gas mixture including hydrocarbons and sour gas, at least including the steps of directing the gas mixture to contact an absorbent liquid having affinity for sour gas, providing a purified off-gas mixture, directing the purified off-gas mixture to contact a liquid hydrocarbon mixture, providing an enriched liquid hydrocarbon mixture, with the associated benefit of such a process having a high recovery of hydrocarbons from the gas mixture to the enriched liquid hydrocarbon mixture, while being efficient in removing hydrogen sulfide from the gas mixture. The gas mixture to be purified may either be a natural gas, a fuel gas or an intermediate gas stream, e.g. from naphtha, kerosene, diesel or condensate hydrotreatment or hydrocracking, and it may also include further constituents, typically hydrogen.

    Induction Heated Reactor
    54.
    发明申请
    Induction Heated Reactor 审中-公开

    公开(公告)号：US20200330944A1

    公开(公告)日：2020-10-22

    申请号：US16095725

    申请日：2017-03-28

    Applicant: HALDOR TOPSØE A/S

    Inventor： Peter Mølgaard MORTENSEN ,  Poul Erik HØJLUND NIELSEN ,  Kim AASBERG-PETERSEN ,  Martin ØSTBERG

    IPC: B01J8/06 ,  B01J8/02 ,  B01J12/00

    Abstract: A tube heat exchange reactor for carrying out an endothermic catalytic reaction. The tube heat exchange reactor includes: an outer tube with a first and a second end, where the first end is an inlet end and where the second end is a closed end, an inner tube coaxially arranged within the outer tube and spaced apart from the outer tube, where at least a part of the inner tube holds a bed of catalyst material susceptible for induction heating and where the inner tube has an inlet end and an outlet end, an induction coil placed within the annular space confined between the outer and the inner tube, and a power source arranged to supply alternating current to the induction coil in order to generate an alternating magnetic field within at least a part of the inner tube.

    SYSTEM AND PROCESS FOR PRODUCTION OF SYNTHESIS GAS
    56.
    发明申请
    SYSTEM AND PROCESS FOR PRODUCTION OF SYNTHESIS GAS 审中-公开

    公开(公告)号：US20200290868A1

    公开(公告)日：2020-09-17

    申请号：US16753501

    申请日：2018-11-15

    Applicant: HALDOR TOPSØE A/S

    Inventor： Peter Mølgaard MORTENSEN ,  Kim AASBERG-PETERSEN

    IPC: C01B3/38 ,  B01J19/24 ,  B01J19/00

    Abstract: A system for production of a synthesis gas, including: a synthesis gas generation reactor arranged for producing a first synthesis gas from a hydrocarbon feed stream; a post converter including a catalyst active for catalyzing steam methane reforming, methanation and reverse water gas shift reactions; the post converter including a conduit for supplying a CO2 rich gas stream into a mixing zone of the post converter, where the CO2 rich gas stream in the conduit upstream the mixing zone is in heat exchange relationship with gas flowing over the catalyst downstream the mixing zone; a pipe combining the at least part of the first synthesis gas and the CO2 rich gas stream to a mixed gas, in a mixing zone being upstream the catalyst; wherein the post converter further includes an outlet for outletting a product synthesis gas from the post converter. Also, a corresponding process.

    PARTICLE RETAINING EQUIPMENT
    57.
    发明申请
    PARTICLE RETAINING EQUIPMENT 审中-公开

    公开(公告)号：US20200261874A1

    公开(公告)日：2020-08-20

    申请号：US16647597

    申请日：2018-10-19

    Applicant: HALDOR TOPSØE A/S

    Inventor： Emir ZAHIROVIC ,  Daniel MORTON ,  Marc ROGATO ,  Flemming Plougstrup NIELSEN

    IPC: B01J8/00

    Abstract: A means for retaining particulate matter, for use in process equipment operated with a fluid, including: a particle retention chamber, a means of suspension, a means of fastening, a support, wherein the particle retention chamber is configured to be suspended from the support by the means of suspension; the means of fastening is configured to fasten the means of suspension to the support.

    HIGH TAP DENSITY LITHIUM POSITIVE ELECTRODE ACTIVE MATERIAL, INTERMEDIATE AND PROCESS OF PREPARATION
    58.
    发明申请
    HIGH TAP DENSITY LITHIUM POSITIVE ELECTRODE ACTIVE MATERIAL, INTERMEDIATE AND PROCESS OF PREPARATION 审中-公开

    公开(公告)号：US20200243858A1

    公开(公告)日：2020-07-30

    申请号：US16839564

    申请日：2020-04-03

    Applicant: HALDOR TOPSØE A/S

    Inventor： Jon Fold VON BÜLOW ,  Søren DAHL ,  Jonathan HØJBERG ,  Jakob Weiland HØJ

    IPC: H01M4/505 ,  H01M10/0525 ,  C01G53/00 ,  H01M4/525

    Abstract: A lithium positive electrode active material intermediate including less than 80 wt % spinel phase and a net chemical composition of LixNiyMn2-yO4-δ wherein 0.9≤x≤1.1; 0.4≤y≤0.5; and 0.1≤δ. Further, a process for the preparation of a lithium positive electrode active material with high tap density for a high voltage secondary battery where the cathode is fully or partially operated above 4.4 V vs. Li/Li+, comprising the steps of a)heating a precursor in a reducing atmosphere at a temperature of from 300° C. to 1200° C. to obtain a lithium positive electrode active material intermediate; b)heating the product of step a. in a non-reducing atmosphere at a temperature of from 300° C. to 1200° C.; wherein the mass of the product of step b. increases by at least 0.25% compared to the mass of the product of step a.

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