GB1161071A - Catalyst Composition - Google Patents

Catalyst Composition

Info

Publication number
GB1161071A
GB1161071A GB3178366A GB3178366A GB1161071A GB 1161071 A GB1161071 A GB 1161071A GB 3178366 A GB3178366 A GB 3178366A GB 3178366 A GB3178366 A GB 3178366A GB 1161071 A GB1161071 A GB 1161071A
Authority
GB
United Kingdom
Prior art keywords
zeolite
molecular sieve
oxide
agent
july
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB3178366A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Union Carbide Corp
Original Assignee
Union Carbide Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Union Carbide Corp filed Critical Union Carbide Corp
Publication of GB1161071A publication Critical patent/GB1161071A/en
Expired legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/10—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y containing iron group metals, noble metals or copper
    • B01J29/12—Noble metals
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G35/00—Reforming naphtha
    • C10G35/04—Catalytic reforming
    • C10G35/06—Catalytic reforming characterised by the catalyst used
    • C10G35/095—Catalytic reforming characterised by the catalyst used containing crystalline alumino-silicates, e.g. molecular sieves

Landscapes

  • Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

1,161,071. Reforming catalyst UNION CARBIDE CORP. 15 July, 1966 [16 July, 1965], No. 31783/66. Heading B1E. [Also in Division C5] A reforming catalyst composition comprises a crystalline zeolitic molecular sieve having a pore size sufficient to accept benzene and general formula where Q is alkali metal, M is calcium and/or manganese, M<SP>1</SP> is thorium and/or a rare earth element of atomic number 57 to 71 inclusive, (x+y+z) is 0.92 to 1, y is at least 0.7, b is 2.3 to 4, z has a positive value of up to 0.20 when 6 is greater than 3 and z is 0.04 to 0.20 when b is not greater than 3, p is zero to 9 and n is the valency of M<SP>1</SP>, the molecular sieve containing a hydrogenation agent. The molecular sieve may be zeolite Y or zeolite X, and preferably contains 0.05 to 2 weight % of Group VIII metal. The zeolite may be mixed with 25% to 75% by weight of total composite of an inorganic oxide diluent which may have hydrogenation activity or may carry a hydrogenation agent. The diluent may be an oxide of Cr, Mo or W; or an oxide of Al or Si, a co-gel of SiO 2 and oxides of Al, Zr, Ti, Th or mixtures thereof, or a clay such as kaolin, attapulgite, sepiolite, polygarskite, bentonite, montinorillonite, carrying as hydro= genating agent 0.05% to 20% Group VIII noble metals or Cr, Ni, Mo, W, Co, Ag, Cu, Re, Sn or Pb.
GB3178366A 1965-07-16 1966-07-15 Catalyst Composition Expired GB1161071A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US47265365A 1965-07-16 1965-07-16

Publications (1)

Publication Number Publication Date
GB1161071A true GB1161071A (en) 1969-08-13

Family

ID=23876397

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3178366A Expired GB1161071A (en) 1965-07-16 1966-07-15 Catalyst Composition

Country Status (3)

Country Link
GB (1) GB1161071A (en)
NL (1) NL6610025A (en)
SE (2) SE329998B (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3303121A1 (en) * 1982-02-01 1983-08-04 Chevron Research Co., 94105 San Francisco, Calif. METHOD FOR REFORMING HYDROCARBONS
US4631123A (en) * 1982-02-01 1986-12-23 Chevron Research Company Method of dehydrocyclizing alkanes
US4634518A (en) * 1982-02-01 1987-01-06 Chevron Research Company Platinum-barium-type L zeolite
US4636298A (en) * 1982-02-01 1987-01-13 Chevron Research Company Reforming process
US4645588A (en) * 1982-02-01 1987-02-24 Chevron Research Company Reforming with a platinum-barium-zeolite of L family
US4721694A (en) * 1982-08-06 1988-01-26 Chevron Research Company Platinum-barium-type L zeolite
US4721695A (en) * 1982-06-28 1988-01-26 Chevron Research Company Platinum-barium-zeolite of L family
CN111054328A (en) * 2018-10-16 2020-04-24 中国石油化工股份有限公司 Selective hydrogenation catalyst for alkylation raw material and preparation method thereof
CN113213506A (en) * 2021-06-01 2021-08-06 江西师范大学 Preparation method and application of metal modified SAPO-34 molecular sieve

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3303121A1 (en) * 1982-02-01 1983-08-04 Chevron Research Co., 94105 San Francisco, Calif. METHOD FOR REFORMING HYDROCARBONS
US4631123A (en) * 1982-02-01 1986-12-23 Chevron Research Company Method of dehydrocyclizing alkanes
US4634518A (en) * 1982-02-01 1987-01-06 Chevron Research Company Platinum-barium-type L zeolite
US4636298A (en) * 1982-02-01 1987-01-13 Chevron Research Company Reforming process
US4645588A (en) * 1982-02-01 1987-02-24 Chevron Research Company Reforming with a platinum-barium-zeolite of L family
US4721695A (en) * 1982-06-28 1988-01-26 Chevron Research Company Platinum-barium-zeolite of L family
US4721694A (en) * 1982-08-06 1988-01-26 Chevron Research Company Platinum-barium-type L zeolite
CN111054328A (en) * 2018-10-16 2020-04-24 中国石油化工股份有限公司 Selective hydrogenation catalyst for alkylation raw material and preparation method thereof
CN111054328B (en) * 2018-10-16 2023-04-11 中国石油化工股份有限公司 Selective hydrogenation catalyst for alkylation raw material and preparation method thereof
CN113213506A (en) * 2021-06-01 2021-08-06 江西师范大学 Preparation method and application of metal modified SAPO-34 molecular sieve

Also Published As

Publication number Publication date
SE329998B (en) 1970-11-02
SE344207B (en) 1972-04-04
DE1542533B2 (en) 1973-01-18
DE1542533A1 (en) 1970-04-16
NL6610025A (en) 1967-01-17

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Legal Events

Date Code Title Description
PS Patent sealed
PCNP Patent ceased through non-payment of renewal fee