GB998262A - Catalytic cracking - Google Patents
Catalytic crackingInfo
- Publication number
- GB998262A GB998262A GB124362A GB124362A GB998262A GB 998262 A GB998262 A GB 998262A GB 124362 A GB124362 A GB 124362A GB 124362 A GB124362 A GB 124362A GB 998262 A GB998262 A GB 998262A
- Authority
- GB
- United Kingdom
- Prior art keywords
- matrix
- catalyst
- aluminosilicate
- ions
- aluminium
- 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
-
- 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
-
- 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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/16—Alumino-silicates
- B01J20/18—Synthetic zeolitic 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/30—Ion-exchange
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Crystallography & Structural Chemistry (AREA)
- Materials Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
A method for the catalytic cracking of hydrocarbons employs as a catalyst composition a crystalline aluminosilicate with a total hydrogen in content of at least 0.5 equivalents per grain atom of aluminium and a total alkali metal content of less than 0.25 equivalents per grain atom of aluminium, such aluminosilicate being intimately mixed with a matrix. The crystalline aluminosilicates used in this invention are obtained by heating any natural or synthetic crystalline aluminosilicate either before or after its incorporation in the matrix with a fluid medium, preferably water, containing hydrogen ions or ions capable of conversion to hydrogen ions, e.g. ammonium ions until the desired concentration is reached. Long lists of suitable zeolites and clays is supplied. The matrix may be an inert or catalytically active material, and is preferably a siliceous gel matrix. The matrix and the aluminosilicate may be combined in a variety of ways. The siliceous gel matrix may also consist of a plural gel comprising a predominant amount of silica with one or more metals or oxides thereof selected from Groups II, III, IV, V, VI, VII and VIII of the Periodic Table. The cracking activity of the catalyst is illustrated by its ability to catalyze the conversion of a Mid-Continent Gas Oil having a boiling range of 450-950 DEG F. to gasoline having an end point of 410 DEG F. Vapours of the gas oil are passed through the catalyst at temperatures of 875 DEG or 900 DEG F. substantially at atmospheric pressure and a feed rate of 1.3 to 16.0 volumes of liquid oil per volume of catalyst per hour for ten minutes.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US16123961A | 1961-12-21 | 1961-12-21 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB998262A true GB998262A (en) | 1965-07-14 |
Family
ID=22580407
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB124362A Expired GB998262A (en) | 1961-12-21 | 1962-01-12 | Catalytic cracking |
Country Status (8)
Country | Link |
---|---|
JP (1) | JPS5138321B1 (en) |
AT (1) | AT256296B (en) |
BE (1) | BE612552A (en) |
DE (1) | DE1442833A1 (en) |
ES (1) | ES273559A1 (en) |
GB (1) | GB998262A (en) |
NL (1) | NL273444A (en) |
NO (1) | NO115180B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0003752A1 (en) * | 1978-02-10 | 1979-09-05 | Kali-Chemie Aktiengesellschaft | Process for preparing molecular-sieve-containing grains having good mechanical solidity, the grains manufactured by this process and their use |
GB2159168A (en) * | 1984-05-25 | 1985-11-27 | Gulf Research Development Co | Process for cracking high metals content feedstocks using a cracking catalyst mixture containing antimony and/or tin |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52143825U (en) * | 1976-04-27 | 1977-10-31 | ||
JPS56135013U (en) * | 1981-02-16 | 1981-10-13 | ||
US11261097B2 (en) * | 2018-05-14 | 2022-03-01 | Umicore Ag & Co. Kg | Stable small-pore zeolites |
-
0
- NL NL273444D patent/NL273444A/xx unknown
- BE BE612552D patent/BE612552A/xx unknown
-
1962
- 1962-01-08 NO NO14278462A patent/NO115180B/no unknown
- 1962-01-11 JP JP82662A patent/JPS5138321B1/ja active Pending
- 1962-01-11 DE DE19621442833 patent/DE1442833A1/en active Pending
- 1962-01-11 ES ES0273559A patent/ES273559A1/en not_active Expired
- 1962-01-11 AT AT20162A patent/AT256296B/en active
- 1962-01-12 GB GB124362A patent/GB998262A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0003752A1 (en) * | 1978-02-10 | 1979-09-05 | Kali-Chemie Aktiengesellschaft | Process for preparing molecular-sieve-containing grains having good mechanical solidity, the grains manufactured by this process and their use |
GB2159168A (en) * | 1984-05-25 | 1985-11-27 | Gulf Research Development Co | Process for cracking high metals content feedstocks using a cracking catalyst mixture containing antimony and/or tin |
GB2159168B (en) * | 1984-05-25 | 1989-05-10 | Gulf Research Development Co | Process for cracking high metals content feedstocks using a cracking catalyst mixture containing antimony and/or tin |
Also Published As
Publication number | Publication date |
---|---|
NO115180B (en) | 1968-08-19 |
BE612552A (en) | |
ES273559A1 (en) | 1962-07-01 |
AT256296B (en) | 1967-08-10 |
JPS5138321B1 (en) | 1976-10-21 |
NL273444A (en) | |
DE1442833A1 (en) | 1969-05-14 |
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