Transalkylation of benzene in a moving bed
    5.
    发明授权
    Transalkylation of benzene in a moving bed 失效
    苯在移动床中的烷基转移

    公开(公告)号:US5087783A

    公开(公告)日:1992-02-11

    申请号:US610950

    申请日:1990-11-09

    IPC分类号: C07C2/66 C07C6/12

    摘要: An improved process for the alkylation of benzene in the presence of an alkylation catalyst. The catalyst bed may be caused to move in a direction countercurrent to the movement of the benzene and olefin, or a portion of the catalyst bed is periodically removed and replaced. A regeneration step, whereby the catalyst is heated in a controlled oxygen atmosphere in order to reactivate the catalyst, is also described.

    摘要翻译: 在烷基化催化剂存在下烷基化苯的改进方法。 可以使催化剂床沿与苯和烯烃的运动逆流的方向移动,或者催化剂床的一部分被周期性地去除和更换。 还描述了再生步骤,其中催化剂在受控氧气氛中加热以使催化剂再活化。

    Alkylation of benzene in a moving bed
    6.
    发明授权
    Alkylation of benzene in a moving bed 失效
    苯在移动床中的烷基化

    公开(公告)号:US4973780A

    公开(公告)日:1990-11-27

    申请号:US186959

    申请日:1988-04-27

    摘要: An improved process for the alkylation of benzene in the presence of an alkylation catalyst. The catalyst bed may be caused to move in a direction countercurrent to the movement of the benzene and olefin, or a portion of the catalyst bed is periodically removed and replaced. A regeneration step, whereby the catalyst is heated in a controlled oxygen atmosphere in order to reactivate the catalyst, is also described.

    摘要翻译: 在烷基化催化剂存在下烷基化苯的改进方法。 可以使催化剂床沿与苯和烯烃的运动逆流的方向移动,或者催化剂床的一部分被周期性地去除和更换。 还描述了再生步骤,其中催化剂在受控氧气氛中加热以使催化剂再活化。

    Solvent refining of residues
    7.
    发明授权
    Solvent refining of residues 失效
    残留物的溶剂精制

    公开(公告)号:US4795551A

    公开(公告)日:1989-01-03

    申请号:US754776

    申请日:1985-07-15

    CPC分类号: C10G21/28 C10C3/08 C10G21/003

    摘要: In the solvent refining of a residual oil, a mixture of refined oil and refining solvent, and a mixture of pitch impurities and refining solvent are introduced into separate zones of a combination tower operated at a pressure of no greater than 100 psig to recover refining solvent from each of the mixtures. The combination tower is preferably A modified crude distillation tower from a preexisting crude unit, whereby idle crude units may be converted to solvent refining.

    摘要翻译: 在残油的溶剂精制中,将精炼油和精制溶剂的混合物以及沥青杂质和精制溶剂的混合物引入在不大于100psig的压力下操作的组合塔的分离区域中,以回收澄清溶剂 从每个混合物。 组合塔优选是来自预先存在的粗单元的经改性的原油蒸馏塔,由此空闲的粗单元可以转化为溶剂精制。