GB1342977A - Process for preparing attrition resistant zeolitc particles - Google Patents
Process for preparing attrition resistant zeolitc particlesInfo
- Publication number
- GB1342977A GB1342977A GB4472571A GB4472571A GB1342977A GB 1342977 A GB1342977 A GB 1342977A GB 4472571 A GB4472571 A GB 4472571A GB 4472571 A GB4472571 A GB 4472571A GB 1342977 A GB1342977 A GB 1342977A
- Authority
- GB
- United Kingdom
- Prior art keywords
- sio
- particles
- attrition resistant
- zeolite
- zeolitc
- 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
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/20—Silicates
- C01B33/26—Aluminium-containing silicates, i.e. silico-aluminates
- C01B33/28—Base exchange silicates, e.g. zeolites
- C01B33/2807—Zeolitic silicoaluminates with a tridimensional crystalline structure possessing molecular sieve properties; Isomorphous compounds wherein a part of the aluminium ore of the silicon present may be replaced by other elements such as gallium, germanium, phosphorus; Preparation of zeolitic molecular sieves from molecular sieves of another type or from preformed reacting mixtures
- C01B33/2815—Zeolitic silicoaluminates with a tridimensional crystalline structure possessing molecular sieve properties; Isomorphous compounds wherein a part of the aluminium ore of the silicon present may be replaced by other elements such as gallium, germanium, phosphorus; Preparation of zeolitic molecular sieves from molecular sieves of another type or from preformed reacting mixtures of type A (UNION CARBIDE trade name; corresponds to GRACE's types Z-12 or Z-12L)
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/20—Silicates
- C01B33/26—Aluminium-containing silicates, i.e. silico-aluminates
- C01B33/28—Base exchange silicates, e.g. zeolites
- C01B33/2807—Zeolitic silicoaluminates with a tridimensional crystalline structure possessing molecular sieve properties; Isomorphous compounds wherein a part of the aluminium ore of the silicon present may be replaced by other elements such as gallium, germanium, phosphorus; Preparation of zeolitic molecular sieves from molecular sieves of another type or from preformed reacting mixtures
- C01B33/2838—Zeolitic silicoaluminates with a tridimensional crystalline structure possessing molecular sieve properties; Isomorphous compounds wherein a part of the aluminium ore of the silicon present may be replaced by other elements such as gallium, germanium, phosphorus; Preparation of zeolitic molecular sieves from molecular sieves of another type or from preformed reacting mixtures of faujasite type, or type X or Y (UNION CARBIDE trade names; correspond to GRACE's types Z-14 and Z-14HS, respectively)
- C01B33/2853—Zeolitic silicoaluminates with a tridimensional crystalline structure possessing molecular sieve properties; Isomorphous compounds wherein a part of the aluminium ore of the silicon present may be replaced by other elements such as gallium, germanium, phosphorus; Preparation of zeolitic molecular sieves from molecular sieves of another type or from preformed reacting mixtures of faujasite type, or type X or Y (UNION CARBIDE trade names; correspond to GRACE's types Z-14 and Z-14HS, respectively) of type Y
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Catalysts (AREA)
Abstract
1342977 Attrition resistant zeolites W R GRACE & CO 24 Sept 1971 [24 Sept 1970] 44725/71 Heading C1A Attrition resistant zeolites having particle size in the range 50-200 Á are prepared by, (a) subdividing and dehydrating, e.g. spraydrying, a slurry of SiO 2 and Al 2 O 3 to solids of size 50-200 Á, (b) mixing the particles with a solution of sodium hydroxide or silicate, with or subsequently, as nucleation centres, particles of a zeolite which are amorphous to X-rays and have an average size below 0À1 Á, e.g. down to 0À05 Á, and then (c) hydrothermally crystallizing the reaction mixture at a temperature of 80-120‹ C. A slurry of clay, SiO 2 - Al 2 O 3 gel, or a cracking catalyst containing 10-40% by wt. Al 2 O 3 may be used. The zeolite may be a faujasite having a SiO 2 /Al 2 O 3 mol. ratio > 3, and a surface area of 230-929 m<SP>2</SP>/g, a pore size of 5-15Š and an attrition index < 40. The nucleation centre may have a SiO 2 /Al 2 O 3 ratio of 2À3-2À7. The zeolite product may be R.E. exchanged to 3% Na.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US7526370A | 1970-09-24 | 1970-09-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1342977A true GB1342977A (en) | 1974-01-10 |
Family
ID=22124566
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4472571A Expired GB1342977A (en) | 1970-09-24 | 1971-09-24 | Process for preparing attrition resistant zeolitc particles |
Country Status (6)
Country | Link |
---|---|
JP (1) | JPS5536603B1 (en) |
CA (1) | CA990708A (en) |
DE (1) | DE2147067A1 (en) |
FR (1) | FR2108479A5 (en) |
GB (1) | GB1342977A (en) |
NL (1) | NL7113157A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3028785A1 (en) * | 1980-07-29 | 1982-02-25 | Engelhard Minerals & Chemicals Corp., Edison, N.J. | Prodn. of shaped zeolite aluminosilicate bodies - from a mixt. of calcined clay precursor bodies and aq. alkali soln. contg. aluminosilicate seed |
EP0117545A2 (en) * | 1983-02-25 | 1984-09-05 | Engelhard Corporation | A fluid catalytic cracking catalyst comprising microspheres containing more than about 40% by weight Y-faujasite and methods for making and using it |
WO2002024329A2 (en) * | 2000-09-22 | 2002-03-28 | Engelhard Corporation | Structurally enhanced cracking catalysts |
US6656347B2 (en) | 2000-09-22 | 2003-12-02 | Engelhard Corporation | Structurally enhanced cracking catalysts |
US6673235B2 (en) | 2000-09-22 | 2004-01-06 | Engelhard Corporation | FCC catalysts for feeds containing nickel and vanadium |
US6942783B2 (en) | 2003-05-19 | 2005-09-13 | Engelhard Corporation | Enhanced FCC catalysts for gas oil and resid applications |
US7101473B2 (en) | 2002-05-31 | 2006-09-05 | Engelhard Corporation | Method of enhancing the activity of FCC catalysts |
US11014821B2 (en) * | 2018-07-09 | 2021-05-25 | Zeolyfe, LLC | Methods for preparation of CHA Zeolite at ambient pressure |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3402842A1 (en) * | 1984-01-27 | 1985-08-08 | Süd-Chemie AG, 8000 München | METHOD FOR PRODUCING CRYSTALLINE ZEOLITHIC ALUMOSILICATES |
FR2565847B1 (en) * | 1984-06-18 | 1986-08-29 | Inst Francais Du Petrole | SYNTHESIS AND USE OF PREFORMED ZEOLITHS |
GB8517997D0 (en) * | 1985-07-17 | 1985-08-21 | English Clays Lovering Pochin | Synthesing faujasites |
JPH0674129B2 (en) * | 1985-12-13 | 1994-09-21 | 東ソー株式会社 | Method for producing synthetic phosphite molding |
DE4021118A1 (en) * | 1990-07-03 | 1992-01-09 | Vaw Ver Aluminium Werke Ag | METHOD FOR THE PREPARATION OF CRYSTALLINE ZEOTITHANALOGEN GALLOSILICATES AND THEIR USE FOR THE PRODUCTION OF CATALYSTS AND ADSORBENTS |
JPH04114225U (en) * | 1991-03-26 | 1992-10-07 | ミツミ電機株式会社 | surface acoustic wave device |
-
1971
- 1971-06-25 CA CA116,672A patent/CA990708A/en not_active Expired
- 1971-09-21 DE DE19712147067 patent/DE2147067A1/en not_active Withdrawn
- 1971-09-23 FR FR7134305A patent/FR2108479A5/fr not_active Expired
- 1971-09-24 NL NL7113157A patent/NL7113157A/xx not_active Application Discontinuation
- 1971-09-24 GB GB4472571A patent/GB1342977A/en not_active Expired
- 1971-09-25 JP JP7496671A patent/JPS5536603B1/ja active Pending
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3028785A1 (en) * | 1980-07-29 | 1982-02-25 | Engelhard Minerals & Chemicals Corp., Edison, N.J. | Prodn. of shaped zeolite aluminosilicate bodies - from a mixt. of calcined clay precursor bodies and aq. alkali soln. contg. aluminosilicate seed |
EP0117545A2 (en) * | 1983-02-25 | 1984-09-05 | Engelhard Corporation | A fluid catalytic cracking catalyst comprising microspheres containing more than about 40% by weight Y-faujasite and methods for making and using it |
US4493902A (en) * | 1983-02-25 | 1985-01-15 | Engelhard Corporation | Fluid catalytic cracking catalyst comprising microspheres containing more than about 40 percent by weight Y-faujasite and methods for making |
EP0117545A3 (en) * | 1983-02-25 | 1986-09-10 | Engelhard Corporation | A fluid catalytic cracking catalyst comprising microspheres containing more than about 40% by weight y-faujasite and methods for making and using it |
AU577521B2 (en) * | 1983-02-25 | 1988-09-29 | Engelhard Corporation | Y-faujasite catalytic cracking catalyst microspheres |
EP0308989A1 (en) * | 1983-02-25 | 1989-03-29 | Engelhard Corporation | A fluid catalytic cracking catalyst comprising microspheres containing more than about 40% by weight Y-faujasite and methods for making and using it |
WO2002024329A2 (en) * | 2000-09-22 | 2002-03-28 | Engelhard Corporation | Structurally enhanced cracking catalysts |
WO2002024329A3 (en) * | 2000-09-22 | 2003-02-06 | Engelhard Corp | Structurally enhanced cracking catalysts |
US6656347B2 (en) | 2000-09-22 | 2003-12-02 | Engelhard Corporation | Structurally enhanced cracking catalysts |
US6673235B2 (en) | 2000-09-22 | 2004-01-06 | Engelhard Corporation | FCC catalysts for feeds containing nickel and vanadium |
EP1502648A1 (en) * | 2000-09-22 | 2005-02-02 | Engelhard Corporation | Structurally enhanced cracking catalysts |
US7101473B2 (en) | 2002-05-31 | 2006-09-05 | Engelhard Corporation | Method of enhancing the activity of FCC catalysts |
US6942783B2 (en) | 2003-05-19 | 2005-09-13 | Engelhard Corporation | Enhanced FCC catalysts for gas oil and resid applications |
US11014821B2 (en) * | 2018-07-09 | 2021-05-25 | Zeolyfe, LLC | Methods for preparation of CHA Zeolite at ambient pressure |
Also Published As
Publication number | Publication date |
---|---|
DE2147067A1 (en) | 1972-03-30 |
CA990708A (en) | 1976-06-08 |
FR2108479A5 (en) | 1972-05-19 |
NL7113157A (en) | 1972-03-28 |
JPS5536603B1 (en) | 1980-09-22 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PCNP | Patent ceased through non-payment of renewal fee |