METHOD FOR PRODUCING AND PURIFYING TRIFLUOROETHYLENE, AND COMPOSITION OBTAINED THEREFROM

    公开(公告)号:US20240400479A1

    公开(公告)日:2024-12-05

    申请号:US18689101

    申请日:2022-09-22

    Applicant: Arkema France

    Abstract: A method for producing trifluoroethylene in a reactor with a fixed catalytic bed comprising a catalyst, comprises the steps of: a) reacting chlorotrifluoroethylene with hydrogen in the presence of the catalyst and in the gas phase, to produce a flow of product comprising trifluoroethylene; b) treating the flow of product obtained in step a) in order to recover a stream A comprising trifluoroethylene, chlorotrifluoroethylene and an additional compound selected from the group consisting of 1,1-difluoroethylene, 1,1,1,2-tetrafluoroethane, 1,1,1-trifluoroethane and ethane; wherein the total content by weight of the additional compound is less than 0.5%; c) distilling stream A to recover a stream B comprising at least 99% by weight of trifluoroethylene and less than 0.2% by weight of one or more additional compounds. A composition comprising at least 99% by weight of trifluoroethylene and from 0.1 to 1000 ppm of ethane, and/or from 0.1 to 1000 ppm of 1,1,1,2-tetrafluoroethane, based on the total weight of the composition is disclosed.

    PROCESS FOR THE PRODUCTION OF TRIFLUOROETHYLENE

    公开(公告)号:US20230391693A1

    公开(公告)日:2023-12-07

    申请号:US18250620

    申请日:2021-10-27

    Applicant: ARKEMA FRANCE

    CPC classification number: C07C17/23 B01J23/44

    Abstract: The present invention relates to a process for the production of trifluoroethylene in a reactor equipped with a fixed catalytic bed comprising a catalyst, said process comprising a stage a) of reaction of chlorotrifluoroethylene with hydrogen in the presence of the catalyst and in the gas phase in order to produce a stream comprising trifluoroethylene; said stage a) being carried out at a temperature of the fixed catalytic bed T1 of between 50° C. and 250° C.; said process being characterized in that, during stage a), the temperature of the fixed catalytic bed T1 is increased provided that it does not exceed 300° C.

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