Method of preparing supported oxidation catalysts for producing ethylene oxide
    12.
    发明授权
    Method of preparing supported oxidation catalysts for producing ethylene oxide 失效
    制备支持氧化乙烯的氧化催化剂的方法

    公开(公告)号:US3663455A

    公开(公告)日:1972-05-16

    申请号:US3663455D

    申请日:1969-11-19

    CPC classification number: C07D301/10 B01J23/48 Y02P20/52 Y10S502/512

    Abstract: A METHOD FOR PREPARING A SUPPORTED CATALYST FOR USE IN OXIDIZING ETHYLENE TO ETHYLENE OXIDE, SAID SUPPORTED CATALYST CONSISTING ESSENTIALLY OF SILVER TO THE EXTENT OF 7 TO 30% BY WEIGHT WITH RESPECT TO THE SUPPORT, AND OF A MEMBER SELECTED FROM THE GROUP CONSISTING OF PLATINUM, PALLADIUM AND GOLD TO AN EXTENT OF FROM 0.01 TO 1.0% BY WEIGHT WITH RESPECT TO SAID SILVER, WHICH COMPRISES: (A) IMPREGNATING A SOLID, INERT SUBDIVIDED SUPPORT, AT A TEMPERATURE OF FROM 60* C.TO 115* C., WITH A SOLUTION OF SILVER LACTATE IN LACTIC ACID CONTAINING IN SUSPENSION, CARBON AND AT LEAST ONE METAL SELECTED FROM THE GROUP CONSISTING OF PALLADIUM, PLATINUM AND GOLD, SAID LACTIC ACID BEING PRESENT IN A MOLAR EXCESS OF FROM 20% TO 200% WITH RESPECT TO THE NUMBER OF MOLS REQUIRED FOR COMPLETE SALIFICATION OF SAID SILVER. (B) DRYING THE PARTICLES THUS IMPREGNATED IN A STREAM OF AIR AT A TEMPERATURE RISING TO A MAXIMUM, BUT NOT EXCEEDING 130* C. FOR A PERIOD OF FROM 1 TO 3 HOURS, AND (C) SUBJECTING THE PARTICLES THUS IMPREGNATED TO A HEAT TREATMENT, SAID TEMPERATURE BEING RAISED GRADUALLY TO A MAXIMUM LEVEL OF BETWEEN 230* C. AND 360* C. OVER A PERIOD OF 10 TO 15 HOURS.

    Solid phosphoric acid catalysts
    14.
    发明授权
    Solid phosphoric acid catalysts 失效
    固体磷酸催化剂

    公开(公告)号:US3661801A

    公开(公告)日:1972-05-09

    申请号:US3661801D

    申请日:1970-02-02

    Abstract: SOLID PHOSPHORIC ACID IS THE NAME WHICH HAS COME INTO USE FOR A CALCINED MIXTURE OF AN ACID OF PHOSPHOROUS AND A POROUS SILICEOUS MATERIAL. SOLID PHOSPHORIC ACID CATALYSTS HAVE FOR YEARS BEEN VIRTUALLY THE ONLY CATALYST EFFECTIVE IN MANY REACTIONS INVOLVING OLEFINS, PARTICULARLY THE POLYMERIZATION OF OLEFINS TO FORM HIGH OCTAN FUELS. THESE CATALYSTS ARE WIDELY USE DESPITE THEIR LACK OF STRENGTH AND POOR WEARING QUALITIES. HIGH STRENGTH SOLID PHOSPHORIC ACID CATALYSTS ARE PROVIDED HEREIN, THE UNIQUENESS OF THE CATALYST BEING ATTRIBUTABLE TO THE METHOD OR PREPARATION. P2O5 IS DRY BLENDED WITH THE SILICA MATERIAL TO FORM THE PRECURSOR. THE PRECURSOR IS THEN SUBJECTED TO A STEAM-AIR TREATMENT TO BRING ABOUT THE HYDRATION OF THE P2O5. THIS FORMS A SILICO-PHOSPHOROUS MATRIX. THID MATRIX IS PRESERVED BY NOT PHYSICALLY CHANGING THE CATALYST DURING ITS PREPARATION. THIS IS ACCOMPLISHED BY FORMING SPHERES OF THE CATALYST MATERIAL BY TUMBLING AND SPRAYING THE TUMING MASS WITH PHOSPHORIC ACID.

    Process for the production of bead-like catalyst supports for high mechanical stressing
    15.
    发明授权
    Process for the production of bead-like catalyst supports for high mechanical stressing 失效
    用于生产用于高机械压力的珠状催化剂支撑体的方法

    公开(公告)号:US3642659A

    公开(公告)日:1972-02-15

    申请号:US3642659D

    申请日:1969-05-21

    Applicant: BAYER AG

    CPC classification number: B01J2/08 B01J21/16 B01J37/0072

    Abstract: POROUS, ABRASION-RESISTANT BEAD-LIKE CATALYST SUPPORTS FOR REACTIONS IN FLUIDISED BEDS CONTAINING IN A MATRIX OF A SILICON DIOXIDE GELMIXED WITH 0.1 TO 3% BY WEIGHT OF MAGNESIUM OXIDE A SILICON DIOXIDE FILLER WITH A SPECIFIC SURFACE AREA OF 20 TO 200 M.2/G. ACCORDING TO BET IN QUANTITIES OF FROM 20 TO 60% BY WEIGHT AND AN ARGILLACEOUS MINERAL FROM THE GROUP COMPRISING KAOLINITE, MONTMORILLONITE AND ATTAPULGITE IN QUANTITIES OF FROM 5 TO 30% BY WEIGHT, BOTH QUANTITIES BEING RELATED TO THE DRY GRANULATED MATERIAL. THE CATALYST SUPPORTS ARE OBTAINED BY SUSPENDING THE SILICON DIOXIDE FILLER AND THE ARGILLACEOUS MINERAL IN THE AFORESAID QUANTITIES IN AN AQUEOS, STABLE SILICON DIOXIDE SOL WITH A SPECIFIC SURFACE AREA OF 150 TO 400 M.2/G. ACCORDING TO BET AND GELLING THE LIQUID SUSPENSION BY THE ADDITION OF HYDRATED FINALLY DIVIDED MAGNESIUM OXIDE IN QUANTITIES OF 0.1 TO 3% BY WEIGHT AND FEEDING THIS GELLABLE MIXTURE IN DROPLET FORM INTO A LIQUID WHICH IS IMMISCIBLE WITH WATER AND FINALLY SEPARATING THE SULPHATED GRANULATED MATERIAL FROM THE LIQUID AND DRIVING AND HARDENING THE BEAD-LIKE GRANULATED MATERIAL FOR AT LEAST 10 MINUTES AT A TEMPERATURE OF FROM 500 TO 1000*C.

    Catalyst and method of preparation
    16.
    发明授权
    Catalyst and method of preparation 失效
    催化剂及其制备方法

    公开(公告)号:US3637525A

    公开(公告)日:1972-01-25

    申请号:US3637525D

    申请日:1969-11-21

    Inventor: O'HARA MARK J

    Abstract: A method of manufacturing an extruded catalyst composite of a Group VIII metal, a Group VIB metal and a refractory inorganic oxide-boron phosphate carrier material. A refractory inorganic oxide hydrogel is prepared and formed into a slurry with an aqueous solution of boric and phosphoric acids. The liquid level of the slurry is adjusted to form an extrudable mass comprising from about 15 to about 45 weight percent solids. The material is then extruded, impregnated with a metal of Group VIII and a metal of Group VIB, dried and calcined in an oxidizing atmosphere.

    Abstract translation: 一种制备第VIII族金属,第VIB族金属和耐火无机氧化物 - 硼磷酸盐载体材料的挤出催化剂复合材料的方法。 制备耐火无机氧化物水凝胶,并用硼酸和磷酸的水溶液形成浆料。 调节浆液的液面以形成包含约15至约45重量%固体的可挤出物料。 然后将材料挤出,用VIII族金属和VIB族金属浸渍,干燥并在氧化气氛中煅烧。

    Iron-modified bismuth phosphomolybdate catalyst
    17.
    发明授权
    Iron-modified bismuth phosphomolybdate catalyst 失效
    铁改性双相磷光体催化剂

    公开(公告)号:US3629148A

    公开(公告)日:1971-12-21

    申请号:US3629148D

    申请日:1969-09-24

    CPC classification number: B01J27/192

    Abstract: THE INSTANT PRODUCT IS A REMANUFACTURED CATALYST. USED OR SPENT BISMUTH PHOSPHOMOLYBDATE CATALYST IS REFORMULATED WITH THE ADDITION OF IRON BY COMMUNUTING SAID CATALYST WITH SUFFICIENT WATER TO FORM A PASTE, ADDING AQUEOUS AMMONIUM HEPTAMOLYBDATE SOLUTION TO SAID PASTE TO FORM A SLURRY, ADDING SAID SLURRY TO A SILICA DISPERSION IN WATER ACIDIFIED WITH PHOSPHORIC ACID, ADDING AN IRON SALT IN ACIDIC SOLUTION TO SAID SLURRY AND HOMOGENEOUSLY DISPERSING IT THEREIN TO FORM A SMOOTH MIXTURE, SPRAY-DRYING SAID MIXTURE AND CALCINING THE SPRAY-DRIED PRODUCT.

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