GB1091424A - Process for hydrocracking a petroleum distillate and a catalytic composition - Google Patents
Process for hydrocracking a petroleum distillate and a catalytic compositionInfo
- Publication number
- GB1091424A GB1091424A GB35340/65A GB3534065A GB1091424A GB 1091424 A GB1091424 A GB 1091424A GB 35340/65 A GB35340/65 A GB 35340/65A GB 3534065 A GB3534065 A GB 3534065A GB 1091424 A GB1091424 A GB 1091424A
- Authority
- GB
- United Kingdom
- Prior art keywords
- prepared
- carrier
- ion
- distillate
- metal
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Abstract
A petroleum distillate 90% of which boils above 204 DEG C. is catalytically hydrocracked with hydrogen at a partial pressure between 35 and 700 kgs/sq. cm. and a feed rate of 35.6 to 534 standard cubic metres/100 litres of distillate with liquid hourly space velocity between 0.5 and 10 volume, as liquid, of said distillate per volume of catalytic composition per hour. The temperature is between 288 DEG and 510 DEG C. The nitrogen content of the feed may be reduced before cracking. The catalytic component is prepared by compositing a Group VI or VIII metal with the calcined carrier prepared from a gelled mixture of a freshly prepared, metallicion free silica sol obtained by ion-exchange of water glass and an aqueous solution yielding aluminium cations.ALSO:A calcined carrier is prepared from a gelled mixture of freshly-prepared, metal-ion-free, silica sol obtained by ion-exchange of water-glass and an aqueous solution containing aluminium cations. Preferably the carrier is composited with metals, metal oxides or sulphides of Group VI or VIII of the Periodic Table. Physical characteristics of the carrier, viz pore and particle size, are given.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US391014A US3306843A (en) | 1964-08-20 | 1964-08-20 | Process and composition for the hydrocracking of hydrocarbon oils |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1091424A true GB1091424A (en) | 1967-11-15 |
Family
ID=23544862
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB35340/65A Expired GB1091424A (en) | 1964-08-20 | 1965-08-18 | Process for hydrocracking a petroleum distillate and a catalytic composition |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US3306843A (en) |
| BE (1) | BE668573A (en) |
| DE (1) | DE1251891B (en) |
| ES (1) | ES316647A1 (en) |
| GB (1) | GB1091424A (en) |
| NL (1) | NL6510949A (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4062809A (en) * | 1976-03-18 | 1977-12-13 | Union Oil Company Of California | Catalyst for production of middle distillate oils |
| US4872895A (en) * | 1986-12-11 | 1989-10-10 | American Telephone And Telegraph Company, At&T Bell Laboratories | Method for fabricating articles which include high silica glass bodies |
| US20020145780A1 (en) * | 2000-09-05 | 2002-10-10 | Frigo Nicholas J. | Simultaneous delivery of 1280 video channels over a WDM passive optical network |
| US6887822B2 (en) * | 2001-09-25 | 2005-05-03 | Pq Corporation | Method for making silica supported, crush-resistant catalysts |
| US8448473B2 (en) * | 2007-10-17 | 2013-05-28 | Compania Vidriera, S.A. De C.V. | Glass melting furnace built entirely with refractory concrete |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3041140A (en) * | 1956-12-31 | 1962-06-26 | Du Pont | Pulverulent silica products |
| US3182012A (en) * | 1958-09-12 | 1965-05-04 | Socony Mobil Oil Co Inc | Catalytic hydrocracking |
| US3078221A (en) * | 1959-07-24 | 1963-02-19 | Gulf Research Development Co | Hydrogenation process for preparation of lubricating oils |
| US3169106A (en) * | 1959-08-20 | 1965-02-09 | Pullman Inc | Hydrogenation catalyst and process |
-
0
- DE DENDAT1251891D patent/DE1251891B/de active Pending
-
1964
- 1964-08-20 US US391014A patent/US3306843A/en not_active Expired - Lifetime
-
1965
- 1965-08-18 GB GB35340/65A patent/GB1091424A/en not_active Expired
- 1965-08-19 ES ES0316647A patent/ES316647A1/en not_active Expired
- 1965-08-20 BE BE668573D patent/BE668573A/xx unknown
- 1965-08-20 NL NL6510949A patent/NL6510949A/xx unknown
Also Published As
| Publication number | Publication date |
|---|---|
| ES316647A1 (en) | 1966-03-16 |
| NL6510949A (en) | 1966-02-21 |
| BE668573A (en) | 1965-12-16 |
| DE1251891B (en) | |
| US3306843A (en) | 1967-02-28 |
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