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12 条记录 (耗时 0.011 秒)

    Process for producing a catalyst by depositing molybdenum removed from a waste catalyst
    1.
    发明授权
    Process for producing a catalyst by depositing molybdenum removed from a waste catalyst 失效
    通过沉积从废催化剂中除去的钼来生产催化剂的方法

    公开(公告)号：US4350609A

    公开(公告)日：1982-09-21

    申请号：US238538

    申请日：1981-02-26

    申请人： Donald C. Cronauer ,  Robert B. Bjorklund

    发明人： Donald C. Cronauer ,  Robert B. Bjorklund

    IPC分类号： B01J23/28 ,  B01J23/92

    CPC分类号： B01J23/92 ,  B01J23/28

    摘要： This invention relates to a method for selectively removing molybdenum values from a spent catalyst and producing a fresh molybdenum-containing catalyst. Such a method preferably contacts anhydrous gaseous hydrogen chloride at an elevated temperature with the metal containing catalyst which is substantially free of carbonaceous material to selectively remove molybdenum therefrom, and producing a fresh molybdenum-containing catalyst by depositing molybdenum from the vapor phase onto a fresh support in the presence of air. At least 50 weight percent and generally as much as 95 weight percent of the molybdenum is removed while other metals such as iron, titanium, cobalt and nickel along with the supporting alumina or silica are not affected.

    摘要翻译： 本发明涉及从废催化剂中选择性除去钼值并生产新鲜的含钼催化剂的方法。 这种方法优选在高温下与含有金属的催化剂的无水氯化氢接触，所述催化剂基本上不含碳质材料以从其中选择性地除去钼，并通过将钼从气相沉积到新鲜载体上来生产新鲜的含钼催化剂 在有空气的情况下。 除去钼的至少50重量％和通常多达95重量％的钼，而其他金属如铁，钛，钴和镍以及支撑氧化铝或二氧化硅不受影响。

    Denitrogenation of shale oil
    2.
    发明授权
    Denitrogenation of shale oil 失效
    页岩油脱氮

    公开(公告)号：US4238320A

    公开(公告)日：1980-12-09

    申请号：US031630

    申请日：1979-04-19

    申请人： Donald C. Cronauer ,  Roger F. Vogel ,  Richard A. Flinn

    发明人： Donald C. Cronauer ,  Roger F. Vogel ,  Richard A. Flinn

    IPC分类号： C10G25/02 ,  C10G67/06 ,  C10G45/08

    CPC分类号： C10G67/06 ,  C10G25/02

    摘要： A process for upgrading crude shale oil containing nitrogen which comprises contacting crude shale oil in a hydrogenation zone with hydrogen in the presence of a hydrogenation catalyst to remove a selected portion of the nitrogen and then contacting the resulting product with an ion exchange resin to obtain a shale oil of substantially lower nitrogen content.

    摘要翻译： 一种用于升级含有氮的粗页岩油的方法，该方法包括在氢化催化剂存在下将粗页岩油与氢气在氢化催化剂存在下接触以除去选定部分的氮气，然后使所得产物与离子交换树脂接触，得到 页岩油含氮量显着降低。

    Process for the conversion of carbonaceous materials
    5.
    发明授权
    Process for the conversion of carbonaceous materials 失效
    碳质材料转化工艺

    公开(公告)号：US3957619A

    公开(公告)日：1976-05-18

    申请号：US482077

    申请日：1974-06-24

    申请人： Sun W. Chun ,  Donald C. Cronauer ,  Thomas W. Leslie

    发明人： Sun W. Chun ,  Donald C. Cronauer ,  Thomas W. Leslie

    IPC分类号： B01J8/02 ,  B01J8/06 ,  C10G1/08 ,  C10G1/06

    CPC分类号： C10G1/083 ,  B01J8/02 ,  B01J8/06 ,  B01J2208/0053

    摘要： A process is provided for the conversion (including upgrading) of solid carbonaceous materials, and in particular for the hydrogenation of coal slurries. The process comprises passing a slurry composed of solid carbonaceous material and solvent, together with hydrogen, through a reaction vessel that contains a plurality of reaction zones separated by porous partitions. A portion of said zones is adapted to contain a solid particulate hydrogenation catalyst which will not pass through said porous partitions. The remainder of said zones forms substantially unobstructed passageways through said reaction vessel. The volumetric proportion of substantially unobstructed passageways to catalyst zones is preferably from about 20:1 to about 1:10.

    摘要翻译： 提供了用于固体碳质材料的转化（包括升级），特别是用于煤浆的氢化的方法。 该方法包括将由固体碳质材料和溶剂组成的浆料与氢气一起通过包含多个由多孔隔板隔开的多个反应区域的反应容器。 所述区域的一部分适于容纳固体颗粒氢化催化剂，其不会通过所述多孔隔板。 所述区域的其余部分形成通过所述反应容器的基本上无阻碍的通道。 基本上无障碍通道到催化剂区域的体积比例优选为约20:1至约1:10。

    Coal liquefaction process using soluble molybdenum-containing organophosphorodithioate catalyst
    6.
    发明授权
    Coal liquefaction process using soluble molybdenum-containing organophosphorodithioate catalyst 失效
    煤液化过程中使用可溶性含钼有机二硫代磷酸酯催化剂

    公开(公告)号：US5246570A

    公开(公告)日：1993-09-21

    申请号：US865837

    申请日：1992-04-09

    申请人： Donald C. Cronauer ,  April J. Swanson ,  Joseph T. Joseph ,  Arunabha Basu ,  Simon G. Kukes

    发明人： Donald C. Cronauer ,  April J. Swanson ,  Joseph T. Joseph ,  Arunabha Basu ,  Simon G. Kukes

    IPC分类号： C10G1/08

    CPC分类号： C10G1/086

    摘要： A coal liquefaction process employing a first stage liquefaction step catalyzed by a soluble molybdenum-containing organophosphorodithioate catalyst is disclosed. In some embodiments, two consecutive liquefaction steps employ a molybdenum-containing organophosphorodithioate catalyst operating at a relatively high liquefaction temperature. In other embodiments, a second liquefaction process step operating at a relatively low temperature employs a hydrocracking catalyst to upgrade materials obtained from the first soluble catalyst liquefaction step. In some embodiments, an interstage gas separator removes gases such as carbon dioxide produced in the first liquefaction step from a partially liquefied mixture prior to further liquefying the mixture in the second liquefaction step.

    摘要翻译： 公开了采用由可溶性含钼有机二硫代磷酸酯催化剂催化的第一阶段液化步骤的煤液化方法。 在一些实施方案中，两个连续的液化步骤使用在较高液化温度下操作的含钼有机二硫代磷酸酯催化剂。 在其它实施方案中，在较低温度下操作的第二液化工艺步骤使用加氢裂化催化剂来升级从第一可溶性催化剂液化步骤获得的材料。 在一些实施例中，级间气体分离器在第二液化步骤中进一步液化混合物之前从部分液化的混合物中除去在第一液化步骤中产生的二氧化碳等气体。