Process for hydrocarbon cracking using a tungsten-rhenium catalyst
    1.
    发明授权
    Process for hydrocarbon cracking using a tungsten-rhenium catalyst 失效
    使用钨酸镉催化剂进行烃开采的方法

    公开(公告)号:US3773656A

    公开(公告)日:1973-11-20

    申请号:US3773656D

    申请日:1971-12-01

    Inventor: HEAD B MARTIN G

    CPC classification number: C10G47/12 B01J23/36 B01J35/08

    Abstract: Heavy hydrocarbon feed oils such as heavy gas oils, residium, topped crude oils and the like are hydrocracked by mixing hydrogen with the feed oil in the ratio of hydrogen to feed oil in the range from 4000 to 10,000 SCF of hydrogen per barrel of feed oil and contacting this mixture under hydro-treating conditions with a supported micro-spherical catalyst having 5-20 weight per cent tungsten and 0.5 to 5.0 weight per cent rhenium. Increased isoparaffin and aromatic content in the cracked product is obtained.

    Process for the upgrading of heavy cracking residues by hydrogenation
    2.
    发明授权
    Process for the upgrading of heavy cracking residues by hydrogenation 失效
    通过加氢提高重型裂缝残渣的工艺

    公开(公告)号:US3764521A

    公开(公告)日:1973-10-09

    申请号:US3764521D

    申请日:1971-10-18

    Inventor: WING M MATHEWS G HEAD B

    CPC classification number: C10G45/50

    Abstract: Process for the hydrogenation of heavy hydrocarbon residues boiling in the range from about 220* F to about 650*F and containing up to 10 percent by weight of tars and gums wherein the hydrocarbon is mixed with hydrogen, passed through a hydrogenation zone under a pressure of 100-1,000 psig, a temperature of 100*C to 200*C, and in the presence of a supported platinum or palladium catalyst and cooled. The hydrogenated product is then distilled to produce a high grade gasoline blend stock as the overhead and the bottoms are useful as a fuel oil.

    Abstract translation: 在约220°F至约650°F范围内沸腾的重质烃残余物氢化的方法,并含有至多10重量%的焦油和树胶,其中烃与氢气混合,在压力下通过氢化区 100-1,000psig,温度为100℃至200℃,并在负载的铂或钯催化剂存在下进行冷却。

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