GB1232393A - - Google Patents
Info
- Publication number
- GB1232393A GB1232393A GB3177167A GB1232393DA GB1232393A GB 1232393 A GB1232393 A GB 1232393A GB 3177167 A GB3177167 A GB 3177167A GB 1232393D A GB1232393D A GB 1232393DA GB 1232393 A GB1232393 A GB 1232393A
- Authority
- GB
- United Kingdom
- Prior art keywords
- sulphur
- nickel
- fraction
- hydrogen
- 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
-
- 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
- C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
- C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
- C10G45/06—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
-
- 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
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
- C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
1,232,393. Catalytic hydrodesulphurization. BRITISH PETROLEUM CO. Ltd. 2 July, 1968 [11 July, 1967], No. 31771/67. Heading C5E. A process for the desulphurization of an aromatic-containing hydrocarbon fraction containing up to 50 p.p.m. by weight sulphur in which not more than 10 mole per cent hydrogenation of the aromatic hydrocarbons occurs comprises passing the fraction in the liquid phase and in the presence of hydrogen upwardly or downwardly through a bed of supported nickel catalyst at an elevated temperature and pressure such that sulphur combines with the nickel but substantially no hydrogen sulphide is produced, the amount of hydrogen present being not more than the maximum amount that would dissolve in the liquid fraction at the process temperature and pressure. The preferred catalyst for the process comprises nickel on sepiolite. High-sulphur-containing feedstocks may be subjected to a preliminary desulphurization over a conventional catalyst such as cobalt oxide and molybdenum oxide on alumina.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB3177167 | 1967-07-11 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1232393A true GB1232393A (en) | 1971-05-19 |
Family
ID=10328163
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB3177167A Expired GB1232393A (en) | 1967-07-11 | 1967-07-11 |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US3714030A (en) |
| JP (1) | JPS4927170B1 (en) |
| AT (1) | AT286476B (en) |
| BE (1) | BE717937A (en) |
| FR (1) | FR1573584A (en) |
| GB (1) | GB1232393A (en) |
| NL (1) | NL6809780A (en) |
| NO (1) | NO122197B (en) |
| SE (1) | SE350981B (en) |
Families Citing this family (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3884797A (en) * | 1971-09-27 | 1975-05-20 | Union Oil Co | Hydrofining-reforming process |
| US4152250A (en) * | 1975-12-09 | 1979-05-01 | Chiyoda Chemical Engineering & Construction | Demetallation of hydrocarbons with catalysts supported on sepiolite |
| GB2031011B (en) * | 1978-10-05 | 1983-01-06 | Chiyoda Chem Eng Construct Co | Processing heavy hydrocarbon oils |
| JPS59120640A (en) * | 1982-12-27 | 1984-07-12 | Takeda Chem Ind Ltd | Sampi complex |
| WO1996017039A1 (en) * | 1994-12-01 | 1996-06-06 | Mobil Oil Corporation | Integrated process for the production of reformate having reduced benzene content |
| JP3553258B2 (en) * | 1995-02-14 | 2004-08-11 | 新日本石油株式会社 | Method for hydrogenating aromatic hydrocarbons in hydrocarbon oil and catalyst used therefor |
| US6495029B1 (en) | 1997-08-22 | 2002-12-17 | Exxon Research And Engineering Company | Countercurrent desulfurization process for refractory organosulfur heterocycles |
| CA2243267C (en) | 1997-09-26 | 2003-12-30 | Exxon Research And Engineering Company | Countercurrent reactor with interstage stripping of nh3 and h2s in gas/liquid contacting zones |
| US6497810B1 (en) | 1998-12-07 | 2002-12-24 | Larry L. Laccino | Countercurrent hydroprocessing with feedstream quench to control temperature |
| US6569314B1 (en) | 1998-12-07 | 2003-05-27 | Exxonmobil Research And Engineering Company | Countercurrent hydroprocessing with trickle bed processing of vapor product stream |
| US6579443B1 (en) | 1998-12-07 | 2003-06-17 | Exxonmobil Research And Engineering Company | Countercurrent hydroprocessing with treatment of feedstream to remove particulates and foulant precursors |
| US6623621B1 (en) | 1998-12-07 | 2003-09-23 | Exxonmobil Research And Engineering Company | Control of flooding in a countercurrent flow reactor by use of temperature of liquid product stream |
| US6835301B1 (en) | 1998-12-08 | 2004-12-28 | Exxon Research And Engineering Company | Production of low sulfur/low aromatics distillates |
| US7374667B2 (en) * | 2001-03-12 | 2008-05-20 | Bp Corporation North America, Inc. | Process for the production of gasoline with a low sulfur content comprising a stage for transformation of sulfur-containing compounds, an acid-catalyst treatment and a desulfurization |
| US6884531B2 (en) * | 2001-05-21 | 2005-04-26 | Saudi Arabian Oil Company | Liquid hydrocarbon based fuels for fuel cell on-board reformers |
| US7081555B2 (en) * | 2002-08-07 | 2006-07-25 | Shell Oil Company | Process for hydrogenation of aromatics in hydrocarbon feedstocks containing thiopheneic compounds |
| DE60313201T2 (en) * | 2002-09-23 | 2008-01-31 | Shell Internationale Research Maatschappij B.V. | CATALYST PARTICLES AND THEIR USE IN DEHYDRATION |
| CN101448919A (en) * | 2006-04-21 | 2009-06-03 | 国际壳牌研究有限公司 | A process for the hydrogenation of aromatics in a hydrocarbon feedstock that contains a thiopheneic compound |
| KR101111006B1 (en) * | 2008-08-14 | 2012-02-15 | 에스케이에너지 주식회사 | Method and apparatus for recovering hydrogen from petroleum desulfurization |
| AU2010303805A1 (en) * | 2009-10-05 | 2012-05-10 | Exxonmobil Research And Engineering Company | Stacking of low activity or regenerated catalyst above higher activity catalyst |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE571792A (en) * | ||||
| US3274275A (en) * | 1963-11-26 | 1966-09-20 | Phillips Petroleum Co | Method for production of cyclohexane |
| US3318965A (en) * | 1964-09-04 | 1967-05-09 | Phillips Petroleum Co | Hydrogenation of benzene to cyclohexane |
| US3254134A (en) * | 1965-04-05 | 1966-05-31 | Texaco Inc | Plural stage hydrogenation of aromatics |
| GB1098698A (en) * | 1965-10-04 | 1968-01-10 | British Petroleum Co | Improvements relating to the desulphurisation of petroleum fractions |
-
1967
- 1967-07-11 GB GB3177167A patent/GB1232393A/en not_active Expired
-
1968
- 1968-07-04 NO NO2675/68A patent/NO122197B/no unknown
- 1968-07-09 SE SE09428/68A patent/SE350981B/xx unknown
- 1968-07-10 FR FR1573584D patent/FR1573584A/fr not_active Expired
- 1968-07-10 NL NL6809780A patent/NL6809780A/xx unknown
- 1968-07-11 BE BE717937D patent/BE717937A/xx unknown
- 1968-07-11 JP JP43048767A patent/JPS4927170B1/ja active Pending
- 1968-07-11 AT AT669568A patent/AT286476B/en not_active IP Right Cessation
-
1970
- 1970-11-13 US US00089445A patent/US3714030A/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| BE717937A (en) | 1969-01-13 |
| FR1573584A (en) | 1969-07-04 |
| JPS4927170B1 (en) | 1974-07-16 |
| US3714030A (en) | 1973-01-30 |
| SE350981B (en) | 1972-11-13 |
| NO122197B (en) | 1971-06-01 |
| AT286476B (en) | 1970-12-10 |
| NL6809780A (en) | 1969-01-14 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PS | Patent sealed [section 19, patents act 1949] | ||
| PCNP | Patent ceased through non-payment of renewal fee |