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    A process containing HF alkylation and selective hydrogenation
    1.
    发明公开
    A process containing HF alkylation and selective hydrogenation 失效
    包含HF碱化和选择性氢化的方法

    公开(公告)号：EP0320094A3

    公开(公告)日：1989-08-09

    申请号：EP88309426.0

    申请日：1988-10-10

    申请人： UOP

    发明人： Hammerschaimb, Harold U. ,  Spinner, Joel B.

    IPC分类号： C07C2/62 ,  C07C5/05

    CPC分类号： C07C2/62 ,  C07C9/16 ,  C07C2527/1206

    摘要： The invention concerns a process in which monoolefins are used to alkylate isoparaffins in the presence of an HF catalyst. An olefinic feed (14) containing dienes is selectively hydrogenated in zone (2) to reduce its diene content, and used for the HF alkylation of isoparaffin feed (26) in alkylation reactor (8). The reactor effluent (40) is passed to isostripper (32) for separation of product alkylate (54). The proportion of C₃ hydrocarbons in the alkylation reactor feed (30) is minimized by passing the selective hydrogenation product (24), the isoparaffin feed (26) and a recycle stream (28) into an alkylation feed stripper (23), providing an overhead C₃ stream (78, 86) and a bottoms (30) used as alkylation reactor feed. The recycle stream (28) is obtained from the overhead (58) of isostripper (32) after passing through HF stripper (12).

    A process containing HF alkylation and selective hydrogenation
    3.
    发明公开
    A process containing HF alkylation and selective hydrogenation 失效
    方法包括在HF的存在及其选择性氢化的烷基化。

    公开(公告)号：EP0320094A2

    公开(公告)日：1989-06-14

    申请号：EP88309426.0

    申请日：1988-10-10

    申请人： UOP

    发明人： Hammerschaimb, Harold U. ,  Spinner, Joel B.

    IPC分类号： C07C2/62 ,  C07C5/05

    CPC分类号： C07C2/62 ,  C07C9/16 ,  C07C2527/1206

    摘要： The invention concerns a process in which monoolefins are used to alkylate isoparaffins in the presence of an HF catalyst.
    An olefinic feed (14) containing dienes is selectively hydrogenated in zone (2) to reduce its diene content, and used for the HF alkylation of isoparaffin feed (26) in alkylation reactor (8). The reactor effluent (40) is passed to isostripper (32) for separation of product alkylate (54).
    The proportion of C₃ hydrocarbons in the alkylation reactor feed (30) is minimized by passing the selective hydrogenation product (24), the isoparaffin feed (26) and a recycle stream (28) into an alkylation feed stripper (23), providing an overhead C₃ stream (78, 86) and a bottoms (30) used as alkylation reactor feed. The recycle stream (28) is obtained from the overhead (58) of isostripper (32) after passing through HF stripper (12).

    摘要翻译： 本发明涉及在其中单烯烃的工艺被用于烷基化的异链烷烃在催化剂上HF存在下进行。 在烯属原料（14）含二烯烃被选择性氢化在服务区（2），以减少它的内容，并且用于在烷基化反应器进料的异链烷烃（26）（8）的HF烷基化。 反应器流出物（40）被传递到isostripper（32），用于烷基化产物中分离（54）。 在烷基化反应器进料C3烃的（30）的比例通过使选择性加氢产物（24），所述异链烷烃进料（26）和再循环料流（28）插入在烷基化进料汽提器（23）最小化，开销提供上 C3料流（78，86），并用作烷基化反应器进料的塔底（30）。 该再循环料流（28）从isostripper（32）的开销（58）穿过HF汽提器（12）后获得的。