GB1343736A - Zeolite-promoted hydrocarbon conversion catalyst - Google Patents
Zeolite-promoted hydrocarbon conversion catalystInfo
- 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
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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
- C10G11/04—Oxides
- C10G11/05—Crystalline alumino-silicates, e.g. molecular sieves
-
- 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
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.
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)
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)
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 |
-
1970
- 1970-12-11 CA CA100,404A patent/CA983464A/en not_active Expired
-
1971
- 1971-03-24 DE DE19712114355 patent/DE2114355C3/en not_active Expired
- 1971-03-24 FR FR7110462A patent/FR2083594B1/fr not_active Expired
- 1971-03-25 AU AU26996/71A patent/AU2699671A/en not_active Expired
- 1971-03-25 JP JP1691671A patent/JPS549149B1/ja active Pending
- 1971-03-25 NL NL7104013A patent/NL7104013A/xx unknown
- 1971-04-19 GB GB2542571A patent/GB1343736A/en not_active Expired
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 |