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    Gas generator and pressure/reaction regulator for use therewith
    24.
    发明授权
    Gas generator and pressure/reaction regulator for use therewith 失效
    气体发生器和压力/反应调节器

    公开(公告)号：US5244640A

    公开(公告)日：1993-09-14

    申请号：US699683

    申请日：1991-05-13

    Applicant: J. Harvey Crawford

    Inventor： J. Harvey Crawford

    IPC: B01J7/02 ,  B01J37/02 ,  C01B3/08

    CPC classification number: C01B3/08 ,  B01J37/02 ,  B01J7/02 ,  Y02E60/36

    Abstract: An gas generator is disclosed that generates gas from a pressure-producing reaction of reactant pieces and reactant fluid. The generator includes a pressure/reaction regulator for use with a reaction chamber. The regulator includes a reactant-fluid accumulator in communication with the reaction chamber via a reactant-fluid port for adjusting pressure in the chamber relative to a preselected threshold pressure. The regulator also includes at least one body extending substantially into the reaction chamber from the reactant-fluid port. The body is formed with holes for letting fluid under pressure into and out of the chamber. Also disclosed is such a regulator that is usable with a reaction chamber having plural reactant-fluid ports and includes plural bodies, one for each port. Certain bodies each have an associated check valve for allowing fluid into the reaction chamber, and certain other bodies each have an associated check valve with a counterweight for allowing fluid to exit the reaction chamber if pressure rises by a preselected increment above the preselected threshold pressure. The gas generator also includes a first and second condenser, with the latter being connected downstream of the former via a gas-exit port. The second condenser includes a spinner rotatably mounted in it for moving heavy, contaminant gases away from the gas-exit outlet under reaction pressure.

    Abstract translation: 公开了一种从反应物块和反应物流体的压力产生反应产生气体的气体发生器。 发生器包括用于与反应室一起使用的压力/反应调节器。 调节器包括经由反应物流体端口与反应室连通的反应物流体储存器，用于相对于预选的阈值压力调节室内的压力。 调节器还包括从反应物流体端口基本上延伸到反应室中的至少一个体。 主体形成有用于使流体在压力下进入和离开室的孔。 还公开了一种可用于具有多个反应物流体端口的反应室的调节器，并且包括多个主体，每个端口一个。 某些体各自具有相关联的止回阀，用于允许流体进入反应室，并且某些其它主体各自具有相关联的止回阀，该配重具有用于允许流体在超过预选阀值压力的情况下以预选的增量上升的方式离开反应室。 气体发生器还包括第一和第二冷凝器，后者通过气体出口连接在前者的下游。 第二冷凝器包括可旋转地安装在其中的旋转器，用于在反应压力下将重的污染气体从气体出口排出。

    Support cobalt-silica coprecipitated hydrogenation catalyst
    25.
    发明授权
    Support cobalt-silica coprecipitated hydrogenation catalyst 失效
    支持钴 - 二氧化硅共沉淀氢化催化剂

    公开(公告)号：US4439544A

    公开(公告)日：1984-03-27

    申请号：US162810

    申请日：1980-06-24

    Applicant: James L. Carter ,  Allan E. Barnett

    Inventor： James L. Carter ,  Allan E. Barnett

    IPC: B01J21/08 ,  B01J23/70 ,  B01J23/75 ,  B01J23/755 ,  B01J35/10 ,  B01J37/02 ,  B01J37/03 ,  B01J23/74

    CPC classification number: B01J37/031 ,  B01J23/75 ,  B01J35/10 ,  B01J37/02 ,  B01J21/08 ,  B01J23/70 ,  B01J23/755 ,  B01J35/0053 ,  B01J35/1019

    Abstract: Supported coprecipitated cobalt-silica hydrogenation catalysts are disclosed. The catalysts are prepared by: preparing an aqueous reaction mixture containing cobalt cations, silicate anions and solid porous carrier particles under agitation to form a coprecipitate of the cobalt and silicate ions onto said solid porous support particles; heating the aqueous reaction mixture; and adding an alkaline precipitating agent to further precipitate the cobalt and silicate ions onto said solid porous carrier particles. The aqueous reaction mixture may additionally include copper cations.

    Abstract translation: 公开了负载型共沉淀钴 - 二氧化硅氢化催化剂。 催化剂通过以下步骤制备：在搅拌下制备含有钴阳离子，硅酸盐阴离子和固体多孔载体颗粒的水性反应混合物，以在所述固体多孔载体颗粒上形成钴和硅酸盐离子的共沉淀物; 加热含水反应混合物; 并加入碱性沉淀剂以进一步将钴和硅酸盐离子沉淀到所述固体多孔载体颗粒上。 含水反应混合物可另外包括铜阳离子。

    Process and catalyst for the preparation of ketones and/or aldehydes from olefines
    26.
    发明授权
    Process and catalyst for the preparation of ketones and/or aldehydes from olefines 失效
    用于从烯烃制备酮和/或醛的方法和催化剂

    公开(公告)号：US3925481A

    公开(公告)日：1975-12-09

    申请号：US27342872

    申请日：1972-07-20

    Applicant: STAMICARBON

    Inventor： GEUS JOHN W

    IPC: B01J23/28 ,  B01J37/00 ,  B01J37/02 ,  C07C45/34 ,  C07C45/35 ,  C07C45/02

    CPC classification number: C07C45/35 ,  B01J23/28 ,  B01J37/00 ,  B01J37/02 ,  C07C45/34 ,  C07C49/08

    Abstract: There is provided a process for the production of ketones and a catalyst for increasing the proportion of ketone produced by the process, wherein an olefine, molecular oxygen and steam are passed over a catalyst containing discrete particles of tin oxide, a majority of such particles being of a size of at most 50 A, homogeneously distributed over a particulate supporting material, the tin oxide particles being covered by a substantially monomolecular layer of molybdenum oxide.

    Abstract translation: 提供了一种制备酮的方法和一种用于增加由该方法生产的酮的比例的催化剂，其中烯烃，分子氧和蒸汽通过含有离散的氧化锡颗粒的催化剂，大部分这样的颗粒是 尺寸为至多50的均匀分布在颗粒状支撑材料上的氧化锡颗粒被氧化钼的基本单分子层覆盖。

    Process for the purification of light paraffinic petroleum distillates
    27.
    发明授权
    Process for the purification of light paraffinic petroleum distillates 失效
    轻质石油馏分的纯化方法

    公开(公告)号：US3827974A

    公开(公告)日：1974-08-06

    申请号：US19038671

    申请日：1971-10-18

    Applicant: LABOFINA SA

    Inventor： AGA R ,  CAHEN R ,  DEBUS H

    IPC: B01J23/40 ,  B01J23/42 ,  B01J37/02 ,  B01J37/03 ,  C10G45/52 ,  C10G23/02 ,  C10G23/04

    CPC classification number: B01J23/40 ,  B01J23/42 ,  B01J37/02 ,  B01J37/03 ,  C10G2400/02

    Abstract: A CONTINUOUS PROCESS FOR THE PURIFICATION OF LIGHT PARAFFINIC FRACTION BOILING IN THE RANGE OF 25* TO 100*C. AND CONTAINING AS MAJOR PORTION STRAIGHT CHAIN PARAFFINS, BRANCHED PARAFFINS AND CYCLOPARAFFINS AND AS A MINOR PORTION AN IMPURITY SELECTED FROM THE GROUP CONSISTING OF AROMATIC HYDROCARBONS, SULPHUR-CONTAINING COMPOUNDS, NITROGEN-CONTAINING COMPOUNDS, AND OTHER NON--HYDROCARBON IMPURITIES, AND MIXTURES THEREOF, THE SULPHUR CONTENT BEING NO GREATER 500 P.P.M., SAID PROCESS COMPRISING: HYDROGENATION SAID LIGHT PARAFFINIC FRACTION AT A TEMPERATURE IN THE RANGE OF 150 TO 375*C., UNDER A PARTIAL PRESSURE OF HYDROGEN OF 10 TO 100 KG./CM.2, AT A S VELOCITY OF 0.5 TO 20 V./V./H. AND A HYDROGEN TO HYDROCARBON RATIO OF 100 TO 3,000 NM.3/M.3, IN THE PRESENCE OF A HYDROGENATING CATALYST CONTAINING BETWEEN 0.1 AND 2% OF PLATINUM ON A SILICA-ALUMINA CARRIER, SILICA BEING IN MAJOR QUANTITY, AND AT LEAST 30% OF THE PLATINUM BEING DISTRIBUTED ON THE CATALYST SURFACE WHICH IS ACCESSIBLE TO THE REACTANTS, FRACTIONATING THE PRODUCTS OF THE HYDROGENATION TO SEPARATE THE HYDROGENATED SULPHUR- AND NITROGEN-CONTAINING COMPOUNDS AND TO RECOVER A PARAFFINIC FRACTION SUBSTANTIALLY CONTAINING ONLY PARAFFINIC HYDROCARBONS WITH AN INCREASED CONTENT OF CYCLOPARAFFINS.

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