GB1343736A - Zeolite-promoted hydrocarbon conversion catalyst - Google Patents

Zeolite-promoted hydrocarbon conversion catalyst

Info

Publication number
GB1343736A
GB1343736A GB2542571A GB2542571A GB1343736A GB 1343736 A GB1343736 A GB 1343736A GB 2542571 A GB2542571 A GB 2542571A GB 2542571 A GB2542571 A GB 2542571A GB 1343736 A GB1343736 A GB 1343736A
Authority
GB
United Kingdom
Prior art keywords
weight per
per cent
faujasite
alumina
clay
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
GB2542571A
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.)
WR Grace and Co Conn
WR Grace and Co
Original Assignee
WR Grace and Co Conn
WR Grace and 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 WR Grace and Co Conn, WR Grace and Co filed Critical WR Grace and Co Conn
Publication of GB1343736A publication Critical patent/GB1343736A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G11/00Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/04Oxides
    • C10G11/05Crystalline alumino-silicates, e.g. molecular sieves
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y

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

1343736 Faujasite-promoted hydrocarbon cracking catalysts W R GRACE & CO 19 April 1971 [26 March 1970] 25425/71 Heading B1E A catalytic composition comprising faujasite, clay and silica-alumina is prepared by a process which comprises (a) providing a mixture which has been obtained in the synthesis of faujasite from alkali metal, silica and alumina values and which comprises faujasite having a SiO 2 :Al 2 O 3 molar ratio of from 3:1 to 6:1 and residual silicate-containing mother liquor, (b) separating the faujasite from the mother liquor, (c) adding clay to the mother liquor, (d) gelling silicate in the resulting reaction medium by addition thereto of carbon dioxide or mineral acid, for example sulphuric acid or hydrochloric acid, (e) ageing the gel-containing reaction medium, (f) adding an aluminium salt to the reaction medium, (g) precipitating alumina from the reaotion medium, for example by addition thereto of ammonia, and (h) recovering solids from the reaction medium, there being added to the reaction medium, at any time after silicate gellation and before solids recovery, faujasite. The clay, which may constitute 20-50 weight per cent of the composition, may be naturally occurring or thermally modified, for example calcined; specified clays, are kaolin, metakaolin, kaolinite, halloysite, montmorillonite, anauxite, dickite and nacrite. Additional silicate may be added either to the mother liquor prior to addition thereto of clay or to the reaction medium prior to silicate gellation; sodium aluminate may be added to the gel-containing reaction medium prior to ageing. The recovered solids may be spray-dried at a temperature of 250-350‹F to provide microspheres having an average diameter of 50-70 microns and/or may be subjected to ion exchange with rare earth metal chloride solution so that rare earth metal constitutes 2.0-4.0 weight per cent (expressed as oxide) of the composition which may contain 10-20 weight per cent faujasite and, correspondingly, 90-80 weight per cent amorphous matrix consisting of 25-50 weight per cent clay and, correspondingly 75-50 weight per cent silica-alumina having an alumina content of 25-40 weight per cent. According to a first example, a composition containing 3.27 weight per cent rare earth metal (expressed as oxide) and consisting of 15.7 weight per cent faujasite, 41.8 weight per cent clay and 42.5 weight per cent silicaalumina having an alumina content of 40 weight per cent is prepared by a procedure which comprises synthesising faujasite by a technique involving seeding, separating faujasite from the synthesis mixture by filtration, adding kaolin to the resulting mother liquor adding carbon dioxide thereby to gel silicate, adding sodium aluminate solution, ageing, adding aluminium sulhpate solution, adding aqueous ammonia thereby to precipitate alumina, adding faujasite separated from the synthesis mixture, filtering, slurrying the resulting filter cake, spray-drying the resulting slurry, subjecting the spray-dried product to ion exchange with ammonium sulphate solution, slurrying the ammonium-exchanged material, adding sulphuric acid, subjecting the resulting material to ion exchange with rare earth metal chloride solution and drying the rare earth metal-exchanged material. According to a second example, a composition containing 3.02 weight per cent rare earth metal (expressed as oxide) and consisting of 15.7 weight per cent faujasite, 24.3 weight per cent clay and 60.0 weight per cent silica-alumina having an alumina content of 25 weight per cent is prepared by a similar procedure modified in that sodium silicate solution is added to the mother liquor prior to addition of kaolin thereto, the addition of sodium aluminate prior to ageing is omitted and the rare earth metal-exchanged material is filtered and washed with water prior to drying.
GB2542571A 1970-03-26 1971-04-19 Zeolite-promoted hydrocarbon conversion catalyst Expired GB1343736A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US2301370A 1970-03-26 1970-03-26

Publications (1)

Publication Number Publication Date
GB1343736A true GB1343736A (en) 1974-01-16

Family

ID=21812627

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2542571A Expired GB1343736A (en) 1970-03-26 1971-04-19 Zeolite-promoted hydrocarbon conversion catalyst

Country Status (7)

Country Link
JP (1) JPS549149B1 (en)
AU (1) AU2699671A (en)
CA (1) CA983464A (en)
DE (1) DE2114355C3 (en)
FR (1) FR2083594B1 (en)
GB (1) GB1343736A (en)
NL (1) NL7104013A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2427843B1 (en) * 1978-06-07 1987-09-18 Exxon Research Engineering Co COMPOSITION FOR CATALYTIC CRACKING BASED ON ALUMINA, ULTRA STABLE Y ZEOLITE AND A POROUS OXIDE MATRIX
US5051164A (en) * 1987-09-04 1991-09-24 Mobil Oil Corporation Crystalline porous silicate composite and its use in catalytic cracking

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3410808A (en) * 1965-09-03 1968-11-12 Exxon Research Engineering Co Zeolitic materials
US3472792A (en) * 1967-03-13 1969-10-14 Universal Oil Prod Co Hydrocarbon conversion catalyst

Also Published As

Publication number Publication date
FR2083594B1 (en) 1975-01-17
CA983464A (en) 1976-02-10
NL7104013A (en) 1971-09-28
AU2699671A (en) 1972-09-28
DE2114355A1 (en) 1971-10-07
DE2114355B2 (en) 1979-09-20
JPS549149B1 (en) 1979-04-21
DE2114355C3 (en) 1980-08-14
FR2083594A1 (en) 1971-12-17

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Legal Events

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