PROCESS TO PRODUCE ALKENES FROM SHALE GAS

    公开(公告)号:US20210395169A1

    公开(公告)日:2021-12-23

    申请号:US17352601

    申请日:2021-06-21

    Abstract: Systems and processes for producing one or more alkenes from shale gas. The process includes at least two dehydrogenation reactors whereby propane, or a mixture of propane and butane, can be dehydrogenated in a first reactor and ethane can be dehydrogenated in a second reactor. The lighter components which serve as chemical inert and thermal mass are separated from the dehydrogenated product after each reactor.

    ELECTRICALLY HEATED DEHYDROGENATION PROCESS

    公开(公告)号:US20210395170A1

    公开(公告)日:2021-12-23

    申请号:US17352632

    申请日:2021-06-21

    Abstract: Systems and processes for dehydrogenating one or more alkanes using electrically heated dehydrogenation reactors. The source of electric energy or power can be a power grid, solar panel, windmill, hydropower, nuclear power, fuel cell, gas turbines, steam turbines, portable generator or the like. The systems and processes provided herein result in a simpler dehydrogenation process which is particularly beneficial at a small scale and at remote locations, including the well site.

    Electrically heated dehydrogenation process

    公开(公告)号:US11578019B2

    公开(公告)日:2023-02-14

    申请号:US17352632

    申请日:2021-06-21

    Abstract: Systems and processes for dehydrogenating one or more alkanes using electrically heated dehydrogenation reactors. The source of electric energy or power can be a power grid, solar panel, windmill, hydropower, nuclear power, fuel cell, gas turbines, steam turbines, portable generator or the like. The systems and processes provided herein result in a simpler dehydrogenation process which is particularly beneficial at a small scale and at remote locations, including the well site.

    Process to produce alkenes from shale gas

    公开(公告)号:US11434184B2

    公开(公告)日:2022-09-06

    申请号:US17352601

    申请日:2021-06-21

    Abstract: Systems and processes for producing one or more alkenes from shale gas. The process includes at least two dehydrogenation reactors whereby propane, or a mixture of propane and butane, can be dehydrogenated in a first reactor and ethane can be dehydrogenated in a second reactor. The lighter components which serve as chemical inert and thermal mass are separated from the dehydrogenated product after each reactor.

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