GB1119239A - Hydrocarbon cracking catalyst with zeolite - Google Patents
Hydrocarbon cracking catalyst with zeoliteInfo
- Publication number
- GB1119239A GB1119239A GB3299765A GB3299765A GB1119239A GB 1119239 A GB1119239 A GB 1119239A GB 3299765 A GB3299765 A GB 3299765A GB 3299765 A GB3299765 A GB 3299765A GB 1119239 A GB1119239 A GB 1119239A
- Authority
- GB
- United Kingdom
- Prior art keywords
- zeolite
- alumina
- silica
- alkali
- cracking catalyst
- 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
- B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
- B01J29/084—Y-type faujasite
Landscapes
- Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
A composite mixture of siliceous cracking catalyst and a zeolite is formed in water and then is washed with an aqueous solution of an ammonium salt to reduce the alkali-metal content of the zeolite before drying. Various filterings, washings slurryings and spray dryings may be performed on the composite before the ammonium treatment. The zeolite has the general formula xR2O: ym2/n O:Al2O3 : 3.5-7SiO2 : O-9H2O where x is 0.1-1; y is O to (1-x) m is a cation other than alkali-metal of valency n and R is an alkali metal cation. The siliceous catalyst may be silicon/magnesia, silicon/zirconia, silica/alumina, silica/alumina/zirconia or silica/magnesia/alumina or an acidified clay. Unit cell sizes surface areas and pore sizes are mentioned.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US38718664A | 1964-08-03 | 1964-08-03 | |
US43116265A | 1965-02-08 | 1965-02-08 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1119239A true GB1119239A (en) | 1968-07-10 |
Family
ID=27011779
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3299765A Expired GB1119239A (en) | 1964-08-03 | 1965-08-02 | Hydrocarbon cracking catalyst with zeolite |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE1542164C3 (en) |
GB (1) | GB1119239A (en) |
-
1965
- 1965-07-29 DE DE19651542164 patent/DE1542164C3/en not_active Expired
- 1965-08-02 GB GB3299765A patent/GB1119239A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
DE1542164B2 (en) | 1975-01-09 |
DE1542164C3 (en) | 1975-09-18 |
DE1542164A1 (en) | 1970-04-02 |
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