TRICYANOHEXANE PURIFICATION METHODS
    3.
    发明公开

    公开(公告)号:US20230416192A1

    公开(公告)日:2023-12-28

    申请号:US18462780

    申请日:2023-09-07

    IPC分类号: C07C253/34

    CPC分类号: C07C253/34

    摘要: Provided herein are processes for purifying TCH in a feed stream, such as an adiponitrile process stream. The processes include a first separating step of separating the adiponitrile process stream to form a first overhead stream comprising low-boiling components and high-boiling components and a first bottoms stream comprising high-boiling components. The processes also include a second separating step of separating the first overhead stream in one or more distillation columns to form a lights stream comprising low-boiling components, a heavies stream comprising high-boiling components, and a TCH stream.

    POLYAMIDE ELASTOMERS WITH HIGH MELTING POINTS

    公开(公告)号:US20230365753A1

    公开(公告)日:2023-11-16

    申请号:US18315153

    申请日:2023-05-10

    IPC分类号: C08G69/28

    CPC分类号: C08G69/28

    摘要: A method of producing a polyamide elastomer comprising feeding a salt solution having a solids content of greater than or equal to 80% to a reactor having a phosphorous containing catalyst having a phosphorous level from 5 to 1000 part by million based on the total weight of the catalyst, feeding a polyether amine to the reactor, and reducing the pressure in the reactor once a target temperature is reached to polymerize the salt solution and the polyether amine to form the polyamide elastomer. The polyamide elastomer has particular uses as a cable tie and demonstrates improved cold-temperature applications while maintaining high strength, good flammability rating, and excellent processability.

    ACETONITRILE SEPARATION PROCESS
    10.
    发明公开

    公开(公告)号:US20230192600A1

    公开(公告)日:2023-06-22

    申请号:US18068645

    申请日:2022-12-20

    IPC分类号: C07C253/34

    CPC分类号: C07C253/34

    摘要: A process for producing acetonitrile, the process comprising dehydrating a feedstock stream comprising acetonitrile, acrylonitrile, allyl alcohol, and water (and optionally methanol) in a dehydration (first) column to yield a dehydrated acetonitrile stream comprising acetonitrile and acrylonitrile, less than 1 wt % allyl alcohol, and less than 50 wt % water, and optionally hydrogen cyanide; distilling the dehydrated acetonitrile stream in a lights (second) column to yield a distillate stream comprising lights, and a bottoms stream comprising acetonitrile, acrylonitrile, water, and optionally hydrogen cyanide and acrylonitrile; extracting the distillation bottoms stream in an extraction (third) column to yield a raffinate stream comprising acetonitrile and less than 200 ppm acrylonitrile and an extract stream comprising water and acrylonitrile; purifying the raffinate stream to yield a product acetonitrile stream.