96.
    发明专利
    未知

    公开(公告)号:DE3427979A1

    公开(公告)日:1986-01-30

    申请号:DE3427979

    申请日:1984-07-28

    Applicant: BASF AG

    Abstract: But-2-enes are obtained from C4-hydrocarbon mixtures which contain but-1-ene and may or may not contain but-2-enes by catalytic isomerization of the but-1-ene to but-2-enes in an isomerization zone at elevated temperatures by a process in which the isomerization is carried out in combination with a distillative separation zone, the said hydrocarbon mixture being fed to the isomerization zone and/or distillative separation zone, the isomerization mixture obtained from the isomerization zone is passed into the distillative separation zone, a but-1-ene-containing fraction is removed above the lower third of the distillative separation zone and passed into the isomerization zone, and the but-2-enes or a fraction containing these are or is removed in the lower third of the distillative separation zone.

    99.
    发明专利
    未知

    公开(公告)号:DE3305805A1

    公开(公告)日:1984-08-23

    申请号:DE3305805

    申请日:1983-02-19

    Applicant: BASF AG

    Abstract: The subject invention relates to a process for regenerating silver-containing carrier catalysts used in the preparation of ethylene oxide which comprises treating a deactivated catalyst with a solution comprising a potassium, rubidium, or cesium compound and a reducing agent. The subject process provides improved catalyst regeneration.

    100.
    发明专利
    未知

    公开(公告)号:DE3304479A1

    公开(公告)日:1984-08-23

    申请号:DE3304479

    申请日:1983-02-10

    Applicant: BASF AG

    Abstract: C2-C4-olefins are prepared by catalytic conversion of methanol and/or dimethyl ether in the presence of a zeolite catalyst at elevated temperatures, by a process in which the catalyst used is a pure borosilicate zeolite which has been tableted or extruded without a binder and treated with hydrofluoric acid and hydrochloric acid. The treatment of the catalyst with hydrofluoric acid is carried out using 0.001-1N HF, and that with hydrochloric acid is carried out using 3-25% strength acid. The time-on-stream of the catalyst is improved.

Patent Agency Ranking