Drying methods
    3.
    发明授权

    公开(公告)号:US10406494B2

    公开(公告)日:2019-09-10

    申请号:US15558877

    申请日:2016-03-17

    摘要: A process for drying resinous materials, comprising: delivering, by way of a plurality of resin channels, resin fluid comprising polymer and solvent into at least first and second steam channels (101) having within a flow of steam, the first and second steam channels (101) each receiving resin fluid from a plurality of resin channels, the first and second steam channels each (101) being received by a stage 1 manifold (121), the steam and resin being delivered under conditions so as to separate at least some of the solvent from the resin fluid; and collecting at least some of the polymer from the resin fluid.

    PROCESS TO PREPARE HIGH HEAT POLYCARBONATES
    7.
    发明申请
    PROCESS TO PREPARE HIGH HEAT POLYCARBONATES 有权
    制备高热聚碳酸酯的方法

    公开(公告)号:US20160237210A1

    公开(公告)日:2016-08-18

    申请号:US15025504

    申请日:2014-09-30

    IPC分类号: C08G64/24 C08G64/12

    CPC分类号: C08G64/24 C08G64/12

    摘要: A catalyzed interfacial phosgenation process with controlled feed ratios and controlled reaction pH levels allows for the formation of high heat polycarbonate random copolymers having high loadings of bis (4-hydroxyphenyl)-2-phenylisoindolin-1-one (“PPPBP”) or a structurally related comonomer. The process produces a polycarbonate copolymer having improved hydrolytic stability.

    摘要翻译: 具有受控进料比和受控反应pH水平的催化界面光气化过程允许形成具有高负载双(4-羟苯基)-2-苯基异吲哚啉-1-酮(“PPPBP”)或结构上的高热聚碳酸酯无规共聚物 相关的共聚单体。 该方法产生具有改善的水解稳定性的聚碳酸酯共聚物。

    Process for converting a natural gas feedstock with inert content to chemical intermediates

    公开(公告)号:US10329215B2

    公开(公告)日:2019-06-25

    申请号:US16249405

    申请日:2019-01-16

    IPC分类号: C07C2/84

    摘要: A methane conversion process for producing C2+ hydrocarbons comprising (a) introducing a reactant mixture comprising methane (>20 mol %) and an inert compound to a reaction unit to produce a reactor effluent stream comprising C2+ hydrocarbons, methane, the inert compound, and water and/or carbon dioxide; (b) removing at least a portion of the water and/or at least a portion of the carbon dioxide from the reactor effluent stream to produce a demethanizer feed stream; (c) feeding at least a portion of the demethanizer feed stream to a demethanizer unit to produce two or more vapor streams (methane rich stream and inert rich stream), and at least one liquid stream (C2+ hydrocarbons); (d) withdrawing at least a portion of the inert rich stream as a purge stream; (e) recycling any remaining portion of the inert rich stream to the reaction unit; and (f) recycling the methane rich stream to the reaction unit.