利索-全球专利检索

  1. 登录
  2. 注册

搜索结果

353 条记录 (耗时 0.016 秒)

    Hydrocarbon conversion with an acidic multimetallic catalytic composite
    112.
    发明授权
    Hydrocarbon conversion with an acidic multimetallic catalytic composite 失效
    用酸性多金属催化复合材料进行烃转化

    公开(公告)号：US4024052A

    公开(公告)日：1977-05-17

    申请号：US633890

    申请日：1975-11-20

    申请人： George J. Antos

    发明人： George J. Antos

    IPC分类号： B01J23/76 ,  B01J23/89 ,  C10G35/09 ,  C10G35/06

    CPC分类号： C10G35/09 ,  B01J23/76 ,  B01J23/89 ,  B01J23/894

    摘要： Hydrocarbons are converted by contacting them at hydrocarbon conversion conditions with an acidic multimetallic catalytic composite comprising a combination of catalytically effective amounts of a platinum group component, a lanthanide series component, a cobalt component, and a halogen component with a porous carrier material. The platinum group component, lanthanide series component, cobalt component, and halogen component are present in the multimetallic catalyst in amounts respectively, calculated on an elemental basis, corresponding to about 0.01 to about 2 wt. % platinum group metal, about 0.01 to about 5 wt. % lanthanide series component, about 0.05 to about 5 wt. % cobalt, and about 0.1 to about 3.5 wt. % halogen. Moreover, these metallic components are uniformly dispersed throughout the porous carrier material in carefully controlled oxidation states such that substantially all of the platinum group metal is present therein in the elemental metallic state, substantially all of the catalytically available cobalt component is present in the elemental metallic state or in a state which is reducible to the elemental metallic state under hydrocarbon conversion conditions, or in a mixture of these states, while substantially all of the lanthanide series component is present therein in an oxidation state above that of the elemental metal. A specific example of the type of hydrocarbon conversion process disclosed is a process for the catalytic reforming of a low-octane gasoline fraction wherein the gasoline fraction and a hydrogen stream are contacted with the acidic multimetallic catalyst disclosed herein at reforming conditions.

    摘要翻译： 通过在碳氢化合物转化条件下与含有催化有效量的铂族组分，镧系元素组分，钴组分和卤素组分与多孔载体材料的组合的酸性多金属催化复合物接触来转化碳氢化合物。 铂族组分，镧系元素组分，钴组分和卤素组分分别以基于元素计算的量存在于多金属催化剂中，相当于约0.01至约2重量％ ％铂族金属，约0.01至约5wt。 ％镧系元素组分，约0.05至约5wt。 ％钴，和约0.1至约3.5wt。 ％卤素。 此外，这些金属组分在仔细控制的氧化状态下均匀地分散在整个多孔载体材料中，使得基本上所有的铂族金属存在于元素金属状态中，基本上所有的催化可用的钴组分存在于元素金属 状态或在烃转化条件下还原成元素金属状态的状态下，或以这些状态的混合状态，而基本上所有的镧系元素组分都存在于比元素金属高的氧化态。 所公开的烃转化方法的具体实例是一种低辛烷值汽油馏分的催化重整方法，其中汽油馏分和氢气流在重整条件下与本文公开的酸性多金属催化剂接触。

    Process for the preparation of ammonia synthesis catalyst
    114.
    发明授权
    Process for the preparation of ammonia synthesis catalyst 失效
    氨合成催化剂的制备工艺

    公开(公告)号：US3951862A

    公开(公告)日：1976-04-20

    申请号：US519481

    申请日：1974-10-30

    申请人： Morgan C. Sze

    发明人： Morgan C. Sze

    IPC分类号： B01J23/76 ,  C01C1/04 ,  B01J21/18 ,  B01J23/10

    CPC分类号： C01C1/0411 ,  B01J23/76 ,  Y02P20/52

    摘要： A process for the preparation of an ammonia synthesis catalyst, in which an iron oxide, together with traces of aluminum, calcium, potassium, magnesium and silicon oxides, is fused in the presence of a small quantity of graphite and reduced and the reduced catalyst is thereafter treated with an aqueous solution of a water soluble cerium salt.The use of the so prepared catalyst in the synthesis of ammonia makes it possible to operate at significantly reduced temperatures and/or pressure, and thereby obtain very considerable capital and operational savings.

    摘要翻译： 一种制备氨合成催化剂的方法，其中氧化铁与微量的铝，钙，钾，镁和氧化硅一起在少量石墨的存在下熔合并且还原的催化剂是 然后用水溶性铈盐水溶液处理。

    Amorphous hydrocarbon conversion catalysts and process for preparing same
    117.
    发明授权
    Amorphous hydrocarbon conversion catalysts and process for preparing same 失效
    无定形烃转化催化剂及其制备方法

    公开(公告)号：US3867305A

    公开(公告)日：1975-02-18

    申请号：US38215173

    申请日：1973-07-24

    申请人： UNION CARBIDE CORP

    发明人： FLANIGEN EDITH MARIE ,  GROSE ROBERT WILLIAM

    IPC分类号： B01J23/76 ,  B01J27/18 ,  C07C5/333 ,  C10G11/04 ,  C10G35/06 ,  C10G49/02 ,  C10G49/08 ,  B01J11/82

    CPC分类号： C10G49/08 ,  B01J23/76 ,  B01J27/18 ,  C07C5/3332 ,  C10G11/04 ,  C10G35/06 ,  C10G49/02 ,  Y10S585/901 ,  Y10S585/906 ,  C07C15/46

    摘要： Novel amorphous compositions possessing catalytic properties may be prepared by controlled calcination of synthetic crystalline precursor material structurally related to the mineral jarosite, said precursor material being prepared and crystallized from an aqueous reaction mixture having a composition expressed in terms of mole ratios of oxides as

    摘要翻译： 具有催化性质的新型无定形组合物可以通过对结构上与矿物黄钾铁矾相关的合成结晶前体材料的可控煅烧来制备，所述前体材料由具有以氧化物摩尔比表示的组成的水性反应混合物制成并结晶，如G 2 O 。 f Fe2O3。 g L2O3。 我XO4 j H 2 O，其中G表示NH 4 +，H +，Ag +或碱金属离子或其任何混合物，其中L 2 O 3代表选自Al 2 O 3，Cr 2 O 3，V 2 O 3，La 2 O 3和 Ce2O3; XO4表示选自PO4，MoO4，VO4，SiO4和T104中的至少一种氧化物; q具有0.5至6.0的值：f具有1.5至4.0的值; g的值为0到1.0; h的值为8.0〜10.0; 我具有从零到2.0的值：j具有从100到1,000的值：f + g的和具有不超过4.0的值。

    Nickel-uranium catalyst
    118.
    发明授权
    Nickel-uranium catalyst 失效
    镍 - 铀催化剂

    公开(公告)号：US3847836A

    公开(公告)日：1974-11-12

    申请号：US27085072

    申请日：1972-07-11

    申请人： FARRINGTON F ,  NICKLIN T

    发明人： NICKLIN T ,  FARRINGTON F

    IPC分类号： B01J23/76 ,  B01J23/78 ,  B01J23/83 ,  B01J37/02 ,  C01B3/40 ,  B01J11/06 ,  B01J11/22

    CPC分类号： B01J23/83 ,  B01J23/76 ,  B01J23/78 ,  B01J37/0201 ,  C01B3/40 ,  C01B2203/1052 ,  Y02P20/52

    摘要： 1. A CATALYST COMPOSITION SUITABLE FOR USE IN THE REFORMING OF HYDROCARBONS WITH STEAM AT AN ELEVATED TEMPERATURE WHICH CATALYST COMPOSITION COMPRISES: (1) AT LEAST ONE MEMBER SELECTED FROM THE GROUP CONSISTING OF NICKEL AND NICKEL OXIDE, (2) AT LEAST ONE MEMBER SELECTED FROM THE GROUP CONSISTING OF URANOSO-URANIC OXIDE (U3O8) AND URANIUM TRIOXIDE (UO3), AND (3) A CARRIER, THE COMPOSITION CONTAINING URANIUM, CALCULATED AS URANOSO-URANIC OXIDE OR URANIUM TRIOXIDE, IN AN AMOUNT OF FROM 5 TO 30 PERCENT BASED ON THE TOTAL WEIGHT OF THE CATALYST COMPOSITION, THE RATIO OF URANIUM TO NICKEL PRESENT IN THE CATALYST COMPOSITION, IN THE REDUCED FORM, BEING FROM ABOUT 0.45 TO ABOUT 0.76:1, SAID CATALYST COMPOSITION HAVING BEEN PRODUCED IN ITS OXIDIZED FORM BY IMPREGNATING THE CARRIER WITH A SOLUTION OF URANIUM AND NICKEL SALTS AND CALCINING SAID SALTS TO THE OXIDES.