GB1431944A - Process for preparing a crystalline aluminosilicate zeolite and process for the conversion of hydrocarbon oils - Google Patents
Process for preparing a crystalline aluminosilicate zeolite and process for the conversion of hydrocarbon oilsInfo
- Publication number
- GB1431944A GB1431944A GB2081873A GB2081873A GB1431944A GB 1431944 A GB1431944 A GB 1431944A GB 2081873 A GB2081873 A GB 2081873A GB 2081873 A GB2081873 A GB 2081873A GB 1431944 A GB1431944 A GB 1431944A
- Authority
- GB
- United Kingdom
- Prior art keywords
- zeolite
- sio
- solution
- exchanged
- heating
- 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
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
- C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
- C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
- C10G47/12—Inorganic carriers
- C10G47/16—Crystalline alumino-silicate carriers
- C10G47/20—Crystalline alumino-silicate carriers the catalyst containing other metals or 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
- B01J20/186—Chemical treatments in view of modifying the properties of the sieve, e.g. increasing the stability or the activity, also decreasing the activity
-
- 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
-
- 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
- C01B33/2876—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 from a reacting mixture containing an amine or an organic cation, e.g. a quaternary onium cation-ammonium, phosphonium, stibonium
-
- 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
-
- 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
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
- C10G45/60—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used
- C10G45/64—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used containing crystalline alumino-silicates, e.g. molecular sieves
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Crystallography & Structural Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Inorganic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Materials Engineering (AREA)
- Analytical Chemistry (AREA)
- Catalysts (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
1431944 Aluminosilicate zeolites SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ BV 2 May 1973 [4 May 1972 (2)] 20818/73 Heading C1A [Also in Divisions B1 and C4-C5] A high-silica faujasite zeolite (529) having SiO 2 /Al 2 O 3 ratio 5À5 to 8À0, unit cell 24À35- 24À60 Š and a benzene sorption at 20‹ C. of 17-24 wt. per cent is made by: (1) heating to 40-70‹ C. a faujasite precursor solution having Na 2 O/SiO 2 =1 to 3/1, SiO 2 /Al 2 O 3 =4 to 20/1, H 2 O/Na 2 O = 10 to 30/1 (molar ratios); (2) combining the solution with Na silicate solution to increase the SiO 2 /Al 2 O 3 molar ratio to 50- 135/1; (3) mixing the combined solution with AlCl 3 solution to form a gel slurry; (4) heating the slurry at 20-150‹ C. and separating an amorphous gel therefrom; (5) mixing the gel with H 2 O to reduce the solids content by 10- 80%; (6) crystallizing the zeolite by heating the mixture at 20-150‹ C. The zeolite may be exchanged with ammonium or metal ions, or converted to hydrogen form by calcining at 500-800‹ C. The NH 4 <SP>+</SP>- exchanged zeolite may be calcined, further NH 4 <SP>+</SP>-exchanged and re-calcined at a lower temperature to provide a catalyst useful in hydrocarbon cracking. The zeolite may also be composited with hydrogenation metal components (see Division B1).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US25039472A | 1972-05-04 | 1972-05-04 | |
US25022072A | 1972-05-04 | 1972-05-04 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1431944A true GB1431944A (en) | 1976-04-14 |
Family
ID=26940697
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2081873A Expired GB1431944A (en) | 1972-05-04 | 1973-05-02 | Process for preparing a crystalline aluminosilicate zeolite and process for the conversion of hydrocarbon oils |
Country Status (7)
Country | Link |
---|---|
JP (1) | JPS56366B2 (en) |
AU (1) | AU468048B2 (en) |
CA (1) | CA1006865A (en) |
DE (1) | DE2322099C2 (en) |
FR (1) | FR2183156B1 (en) |
GB (1) | GB1431944A (en) |
NL (1) | NL7306078A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4503023A (en) * | 1979-08-14 | 1985-03-05 | Union Carbide Corporation | Silicon substituted zeolite compositions and process for preparing same |
USH282H (en) | 1982-12-27 | 1987-06-02 | W. R. Grace & Co. | High silica/alumina ratio faujasite type NaY |
US4711770A (en) * | 1979-08-14 | 1987-12-08 | Union Carbide Corporation | Silicon substituted Y zeolite composition LZ-210 |
US4897178A (en) * | 1983-05-02 | 1990-01-30 | Uop | Hydrocracking catalyst and hydrocracking process |
WO2009126974A2 (en) * | 2008-04-10 | 2009-10-15 | Shell Oil Company | Diluents, method for preparing a diluted hydrocarbon composition, and diluted hydrocarbon compositions |
US8450538B2 (en) | 2008-04-10 | 2013-05-28 | Shell Oil Company | Hydrocarbon composition |
CN104743572A (en) * | 2013-12-27 | 2015-07-01 | 陕西煤化工技术工程中心有限公司 | Method for synthesis of high silica-alumina ratio ultrafine NaY molecular sieve |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3004060A1 (en) * | 1979-02-07 | 1980-08-21 | Toyo Soda Mfg Co Ltd | METHOD FOR PRODUCING Y ZEOLITE |
NL191266C (en) * | 1979-05-25 | 1995-04-18 | Shell Int Research | Process for the preparation of light hydrocarbon fractions. |
JPS6121911A (en) * | 1984-07-11 | 1986-01-30 | Toyo Soda Mfg Co Ltd | Preparation of faujasite type zeolite |
US4663025A (en) * | 1986-08-14 | 1987-05-05 | Phillips Petroleum Company | Catalytic cracking processes |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1058929B (en) * | 1954-04-20 | 1959-06-04 | Milprint Inc | Hose-like container made of flexible material |
US3492090A (en) * | 1966-04-07 | 1970-01-27 | Mobil Oil Corp | Process for producing faujasite |
-
1973
- 1973-03-07 CA CA165,417A patent/CA1006865A/en not_active Expired
- 1973-05-02 DE DE19732322099 patent/DE2322099C2/en not_active Expired
- 1973-05-02 NL NL7306078A patent/NL7306078A/xx active Search and Examination
- 1973-05-02 JP JP4859173A patent/JPS56366B2/ja not_active Expired
- 1973-05-02 FR FR7315713A patent/FR2183156B1/fr not_active Expired
- 1973-05-02 GB GB2081873A patent/GB1431944A/en not_active Expired
- 1973-05-02 AU AU55141/73A patent/AU468048B2/en not_active Expired
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4503023A (en) * | 1979-08-14 | 1985-03-05 | Union Carbide Corporation | Silicon substituted zeolite compositions and process for preparing same |
US4711770A (en) * | 1979-08-14 | 1987-12-08 | Union Carbide Corporation | Silicon substituted Y zeolite composition LZ-210 |
USH282H (en) | 1982-12-27 | 1987-06-02 | W. R. Grace & Co. | High silica/alumina ratio faujasite type NaY |
US4897178A (en) * | 1983-05-02 | 1990-01-30 | Uop | Hydrocracking catalyst and hydrocracking process |
WO2009126974A2 (en) * | 2008-04-10 | 2009-10-15 | Shell Oil Company | Diluents, method for preparing a diluted hydrocarbon composition, and diluted hydrocarbon compositions |
WO2009126974A3 (en) * | 2008-04-10 | 2010-03-18 | Shell Oil Company | Method for preparing a diluted hydrocarbon composition, and diluted hydrocarbon compositions |
US8450538B2 (en) | 2008-04-10 | 2013-05-28 | Shell Oil Company | Hydrocarbon composition |
US8734634B2 (en) | 2008-04-10 | 2014-05-27 | Shell Oil Company | Method for producing a crude product, method for preparing a diluted hydrocarbon composition, crude products, diluents and uses of such crude products and diluents |
CN104743572A (en) * | 2013-12-27 | 2015-07-01 | 陕西煤化工技术工程中心有限公司 | Method for synthesis of high silica-alumina ratio ultrafine NaY molecular sieve |
CN104743572B (en) * | 2013-12-27 | 2018-02-16 | 陕西煤化工技术工程中心有限公司 | A kind of method of the ultra-fine NaY molecular sieve of synthesizing high-silicon aluminum ratio |
Also Published As
Publication number | Publication date |
---|---|
FR2183156A1 (en) | 1973-12-14 |
AU5514173A (en) | 1974-11-07 |
DE2322099C2 (en) | 1982-08-26 |
DE2322099A1 (en) | 1973-11-22 |
JPS56366B2 (en) | 1981-01-07 |
JPS4961096A (en) | 1974-06-13 |
FR2183156B1 (en) | 1976-06-11 |
NL7306078A (en) | 1973-11-06 |
AU468048B2 (en) | 1975-12-18 |
CA1006865A (en) | 1977-03-15 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PCNP | Patent ceased through non-payment of renewal fee |
Effective date: 19920502 |