GB1281265A - A catalytic composition for the conversion of petroleum hydrocarbons - Google Patents

A catalytic composition for the conversion of petroleum hydrocarbons

Info

Publication number
GB1281265A
GB1281265A GB1661270A GB1661270A GB1281265A GB 1281265 A GB1281265 A GB 1281265A GB 1661270 A GB1661270 A GB 1661270A GB 1661270 A GB1661270 A GB 1661270A GB 1281265 A GB1281265 A GB 1281265A
Authority
GB
United Kingdom
Prior art keywords
pore
aluminosilicate
catalyst
april
catalytic composition
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
GB1661270A
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.)
Standard Oil Co
Original Assignee
Standard Oil Co
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 Standard Oil Co filed Critical Standard Oil Co
Publication of GB1281265A publication Critical patent/GB1281265A/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • C10G47/12—Inorganic carriers
    • C10G47/16—Crystalline alumino-silicate carriers
    • C10G47/20—Crystalline alumino-silicate carriers the catalyst containing other metals or compounds thereof
    • 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
    • B01J29/16—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J29/166—Y-type faujasite
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/12—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing crystalline alumino-silicates, e.g. molecular sieves

Landscapes

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

Abstract

1281265 Cracking catalyst STANDARD OIL CO 8 April 1970 [8 April 1969] 16612/70 Heading B1E [Also in Division C5] A catalytic composition comprises (i) elemental nickel and elemental tungsten, their oxides, their sulphides or mixtures thereof, and (ii) a support comprising a large-pore crystalline aluminosilicate material and a refractory inorganic oxide. By large-pore it is meant that the pores are of a sufficient size to permit the passage thereinto of benzene molecules, e.g. 9 to 10Š or above. Suitably, the large-pore aluminosilicate is an ultrastable, large-pore crystalline aluminosilicate of max. cubic unit cell dimension of 24-55Š, hydroxyl IR bands near 3700 cm<SP>-1</SP> and near 3625cm<SP>-1</SP> and an alkali metal content of less than 1 per cent. The specified refractory oxide is silica-alumina, preferably in the form of a matrix for the aluminosilicate. The quantity of nickel and tungsten present are 0.03 to 0.20 gm-mole of NiO and WO 3 per 100 gms of catalyst with a W/Ni ratio of 0.6 to 12.0. The catalyst may be pretreated before use with a stream of hydrogen optionally containing a little hydrogen sulphide.
GB1661270A 1969-04-08 1970-04-08 A catalytic composition for the conversion of petroleum hydrocarbons Expired GB1281265A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US81435669A 1969-04-08 1969-04-08

Publications (1)

Publication Number Publication Date
GB1281265A true GB1281265A (en) 1972-07-12

Family

ID=25214819

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1661270A Expired GB1281265A (en) 1969-04-08 1970-04-08 A catalytic composition for the conversion of petroleum hydrocarbons

Country Status (6)

Country Link
BE (1) BE748685A (en)
CA (1) CA970346A (en)
DE (1) DE2016774A1 (en)
FR (1) FR2043108A5 (en)
GB (1) GB1281265A (en)
NL (1) NL7005010A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0038140A1 (en) * 1980-04-14 1981-10-21 Mobil Oil Corporation Catalytic hydrocracking
EP0044631A1 (en) * 1980-07-18 1982-01-27 Mobil Oil Corporation Hydrocarbon cracking process
WO2011091203A3 (en) * 2010-01-21 2012-08-09 Shell Oil Company Hydrocarbon composition
US8562818B2 (en) 2010-01-21 2013-10-22 Shell Oil Company Hydrocarbon composition
US8597498B2 (en) 2010-01-21 2013-12-03 Shell Oil Company Process for treating a hydrocarbon-containing feed
US8597499B2 (en) 2010-01-21 2013-12-03 Shell Oil Company Process for treating a hydrocarbon-containing feed
US8679319B2 (en) 2010-01-21 2014-03-25 Shell Oil Company Hydrocarbon composition
CN104588081A (en) * 2013-11-03 2015-05-06 中国石油化工股份有限公司 Preparation method of hydrocracking catalyst containing rare earth
RU2600448C1 (en) * 2015-10-20 2016-10-20 Федеральное государственное бюджетное учреждение науки Институт химии нефти Сибирского отделения Российской академии наук (ИХН СО РАН) Method of processing natural bitumen
CN104588119B (en) * 2013-11-03 2017-01-25 中国石油化工股份有限公司 Preparation method for hydrocracking catalyst containing heteropoly acid

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0038140A1 (en) * 1980-04-14 1981-10-21 Mobil Oil Corporation Catalytic hydrocracking
EP0044631A1 (en) * 1980-07-18 1982-01-27 Mobil Oil Corporation Hydrocarbon cracking process
WO2011091203A3 (en) * 2010-01-21 2012-08-09 Shell Oil Company Hydrocarbon composition
US8562818B2 (en) 2010-01-21 2013-10-22 Shell Oil Company Hydrocarbon composition
US8597498B2 (en) 2010-01-21 2013-12-03 Shell Oil Company Process for treating a hydrocarbon-containing feed
US8597499B2 (en) 2010-01-21 2013-12-03 Shell Oil Company Process for treating a hydrocarbon-containing feed
US8679319B2 (en) 2010-01-21 2014-03-25 Shell Oil Company Hydrocarbon composition
CN104588081A (en) * 2013-11-03 2015-05-06 中国石油化工股份有限公司 Preparation method of hydrocracking catalyst containing rare earth
CN104588081B (en) * 2013-11-03 2016-11-23 中国石油化工股份有限公司 The preparation method of the hydrocracking catalyst containing rare earth
CN104588119B (en) * 2013-11-03 2017-01-25 中国石油化工股份有限公司 Preparation method for hydrocracking catalyst containing heteropoly acid
RU2600448C1 (en) * 2015-10-20 2016-10-20 Федеральное государственное бюджетное учреждение науки Институт химии нефти Сибирского отделения Российской академии наук (ИХН СО РАН) Method of processing natural bitumen

Also Published As

Publication number Publication date
DE2016774A1 (en) 1970-10-15
FR2043108A5 (en) 1971-02-12
NL7005010A (en) 1970-10-12
BE748685A (en) 1970-09-06
CA970346A (en) 1975-07-01

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Legal Events

Date Code Title Description
414F Notice of opposition given (sect. 14/1949)
414A Case decided by the comptroller ** specification amended (sect. 14/1949)
PS Patent sealed
PCNP Patent ceased through non-payment of renewal fee