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34 条记录 (耗时 0.023 秒)

    Selective high conversion cracking process
    6.
    发明授权
    Selective high conversion cracking process 失效
    选择性高转化裂解过程

    公开(公告)号：US4137152A

    公开(公告)日：1979-01-30

    申请号：US850183

    申请日：1977-11-10

    申请人： Arthur W. Chester ,  Albert B. Schwartz ,  William A. Stover

    发明人： Arthur W. Chester ,  Albert B. Schwartz ,  William A. Stover

    IPC分类号： B01J29/08 ,  B01J29/12 ,  B01J29/18 ,  B01J29/80 ,  C10G11/05 ,  B01J8/24 ,  C07C15/02 ,  C10G11/04

    CPC分类号： C10G11/05 ,  B01J29/80 ,  B01J2229/26 ,  B01J2229/42 ,  B01J29/084 ,  B01J29/126 ,  B01J29/18

    摘要： A catalytic process is provided for cracking a hydrocarbon charge stock containing aromatic nuclei components and non-aromatic nuclei components which involves contacting such chargestock with a catalyst composition having an alkali metal content less than about 1.5 weight percent and containing a mixture of faujasite and mordenite in which contacting takes place under catalytic cracking conditions of such severity that the conversion level exceeds that attributable to conversion of the non-aromatic nuclei portion of the chargestock. Under such conditions, the coke yield is substantially lower than would be obtained with the same catalyst in the absence of mordenite at the same level of conversion.

    摘要翻译： 提供了一种催化方法，用于裂解含有芳族核组分和非芳族核组分的烃电荷原料，其包括使这些电荷与碱金属含量低于约1.5重量％的催化剂组合物接触并含有八面沸石和丝光沸石的混合物 该接触发生在催化裂解条件下，其严重程度使得转化率超过归因于电荷转运的非芳族核部分的转化率。 在这种条件下，焦炭产量基本上低于在不存在丝光沸石时相同催化剂在相同转化水平下获得的焦炭产量。

    Hydrocarbon conversion over activated erionite
    8.
    发明授权
    Hydrocarbon conversion over activated erionite 失效
    碳氢化合物转化为活化的白云石

    公开(公告)号：US4021332A

    公开(公告)日：1977-05-03

    申请号：US586130

    申请日：1975-06-12

    申请人： Robert C. Wilson, Jr. ,  Albert B. Schwartz

    发明人： Robert C. Wilson, Jr. ,  Albert B. Schwartz

    IPC分类号： B01J29/56 ,  C10G11/02 ,  C10G45/64 ,  B01J29/06 ,  C10G11/04

    CPC分类号： C10G45/64 ,  B01J29/56

    摘要： This invention is directed to the shape selective conversion of a hydrocarbon charge over erionite which has been activated by the steps comprising calcining the erionite as a first step, contacting with a solution of an ammonium salt, contacting with a solution of metal salt containing a metal such as calcium, calcining again, contacting again with a solution of an ammonium salt and then with a solution of a metal salt containing nickel or another similar metal, and finally calcining. It is also directed to the catalyst utilized in affecting said conversion and to the method for preparing such catalyst.

    摘要翻译： 本发明涉及通过以下步骤活化的烃电荷在毛沸石上的形状选择性转化：包括煅烧作为第一步的毛沸石的步骤，与铵盐溶液接触，与含有金属的金属盐的溶液接触 例如钙，再次煅烧，再次与铵盐溶液接触，再与含有镍或其它类似金属的金属盐溶液接触，最后煅烧。 还涉及用于影响所述转化率的催化剂和制备这种催化剂的方法。

    Moving bed catalytic cracking process with platinum group metal or rhenium supported directly on the cracking catalyst
    10.
    发明授权
    Moving bed catalytic cracking process with platinum group metal or rhenium supported directly on the cracking catalyst 失效
    用铂族金属或铼直接负载在裂化催化剂上的移动床催化裂解过程

    公开(公告)号：US4473658A

    公开(公告)日：1984-09-25

    申请号：US524103

    申请日：1983-08-17

    申请人： Albert B. Schwartz

    发明人： Albert B. Schwartz

    IPC分类号： B01J29/06 ,  B01J29/90 ,  B01J38/22 ,  B01J29/38 ,  B01J21/20 ,  C10G11/05 ,  C10G11/16

    CPC分类号： B01J29/061 ,  B01J29/90 ,  B01J38/22

    摘要： An improved moving bed continuous catalytic cracking process for cracking hydrocarbon feedstocks, such as gas oil, in the absence of added hydrogen, which includes the use of a minute amount of dispersed platinum supported directly on a cracking catalyst. The trace of platinum induces a substantial increase in the heat efficiency with which coke on catalyst is converted to CO.sub.2 in the regenerator section with minimal or no detriment to the cracking reaction.

    摘要翻译： 一种改进的移动床连续催化裂化方法，用于在没有加入氢气的情况下裂化烃原料如瓦斯油，其包括使用微量的分散的铂直接负载在裂化催化剂上。 铂的痕迹导致热效率的显着增加，在该热效率下，催化剂上的焦炭在再生器部分中转化为CO 2，同时对裂解反应的影响最小或没有损害。