ES332400A1 - A procedure for the desulfuration of an aromatic hydrocarbon. (Machine-translation by Google Translate, not legally binding) - Google Patents
A procedure for the desulfuration of an aromatic hydrocarbon. (Machine-translation by Google Translate, not legally binding)Info
- Publication number
- ES332400A1 ES332400A1 ES0332400A ES332400A ES332400A1 ES 332400 A1 ES332400 A1 ES 332400A1 ES 0332400 A ES0332400 A ES 0332400A ES 332400 A ES332400 A ES 332400A ES 332400 A1 ES332400 A1 ES 332400A1
- Authority
- ES
- Spain
- Prior art keywords
- translation
- machine
- legally binding
- google translate
- aromatic hydrocarbon
- 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
Abstract
A process for the desulfurization of an aromatic hydrocarbon, containing fractions containing from 1 to 50 parts per thousand by weight of sulfur without appreciable hydrogenation of the aromatic hydrocarbons, characterized in that it comprises the passage of the fraction in liquid phase or vapor , and in the presence of hydrogen, on a nickel supported at an elevated temperature and pressure such that the sulfur combines with the nickel but without producing a substantial amount of hydrogen sulfide, the equilibrium of the hydrogen partial pressure being greater than the minimum necessary to prevent deactivation of the catalyst but less than that in which 10 mol per hundred hydrogenation of the aromatic hydrocarbons is produced. (Machine-translation by Google Translate, not legally binding)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB41940/65A GB1141809A (en) | 1965-10-04 | 1965-10-04 | Improvements relating to the desulphurisation and hydrogenation of aromatic hydrocarbons |
Publications (1)
Publication Number | Publication Date |
---|---|
ES332400A1 true ES332400A1 (en) | 1967-08-01 |
Family
ID=10422076
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES0332400A Expired ES332400A1 (en) | 1965-10-04 | 1966-10-04 | A procedure for the desulfuration of an aromatic hydrocarbon. (Machine-translation by Google Translate, not legally binding) |
Country Status (12)
Country | Link |
---|---|
US (1) | US3484496A (en) |
AT (1) | AT267026B (en) |
BE (1) | BE687782A (en) |
CH (1) | CH508563A (en) |
DE (1) | DE1568189C3 (en) |
ES (1) | ES332400A1 (en) |
FR (1) | FR1498696A (en) |
GB (1) | GB1141809A (en) |
IL (1) | IL26615A (en) |
NL (1) | NL6613968A (en) |
NO (1) | NO120151B (en) |
SE (1) | SE346556B (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3767562A (en) * | 1971-09-02 | 1973-10-23 | Lummus Co | Production of jet fuel |
US4036734A (en) * | 1973-11-02 | 1977-07-19 | Exxon Research And Engineering Company | Process for manufacturing naphthenic solvents and low aromatics mineral spirits |
US3996304A (en) * | 1974-06-19 | 1976-12-07 | Universal Oil Products Company | Hydroprocessing of hydrocarbons |
US3992464A (en) * | 1974-11-08 | 1976-11-16 | Uop Inc. | Hydroprocessing aromatics to make cycloparaffins |
JP3424053B2 (en) * | 1994-09-02 | 2003-07-07 | 新日本石油株式会社 | Method for producing low sulfur low aromatic gas oil |
CA2206309A1 (en) * | 1994-12-01 | 1996-06-06 | Stuart Shansen Shih | Integrated process for the production of reformate having reduced benzene content |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1974057A (en) * | 1931-12-11 | 1934-09-18 | Tide Water Oil Company | Two stage method of hydrogenation |
US2303075A (en) * | 1938-11-12 | 1942-11-24 | Phillips Proroleum Company | Catalytic hydrogenation process |
US2300877A (en) * | 1940-08-12 | 1942-11-03 | Phillips Petroleum Co | Process for treating hydrocarbons |
US2426929A (en) * | 1944-07-17 | 1947-09-02 | Shell Dev | Hydrogenation of liquid carbonaceous materials |
US2459465A (en) * | 1945-05-11 | 1949-01-18 | Standard Oil Dev Co | Two-stage hydrogenation treatment for hydrocarbon oils |
US2464539A (en) * | 1945-09-19 | 1949-03-15 | Standard Oil Dev Co | Two-stage destructive hydrogenation of petroleum oil |
US2755317A (en) * | 1952-11-10 | 1956-07-17 | Universal Oil Prod Co | Hydrogenation of benzene to cyclohexane |
GB1002394A (en) * | 1961-08-08 | 1965-08-25 | British Petroleum Co | Isomerisation of olefines |
FR1419557A (en) * | 1961-09-13 | 1965-12-03 | Inst Francais Du Petrole | New process for the catalytic hydrogenation of aromatic hydrocarbons |
GB979257A (en) * | 1962-03-10 | 1965-01-01 | British Petroleum Co | Multi-stage hydrogenation process |
US3147210A (en) * | 1962-03-19 | 1964-09-01 | Union Oil Co | Two stage hydrogenation process |
US3222274A (en) * | 1963-01-02 | 1965-12-07 | Socony Mobil Oil Co Inc | Process for producing high energy jet fuels |
US3341613A (en) * | 1964-10-30 | 1967-09-12 | Phillips Petroleum Co | Method for production of cyclohexane by the hydrogenation of benzene |
US3254134A (en) * | 1965-04-05 | 1966-05-31 | Texaco Inc | Plural stage hydrogenation of aromatics |
-
1965
- 1965-10-04 GB GB41940/65A patent/GB1141809A/en not_active Expired
-
1966
- 1966-09-30 NO NO164953A patent/NO120151B/no unknown
- 1966-10-01 DE DE1568189A patent/DE1568189C3/en not_active Expired
- 1966-10-02 IL IL26615A patent/IL26615A/en unknown
- 1966-10-03 FR FR78571A patent/FR1498696A/en not_active Expired
- 1966-10-03 US US583740A patent/US3484496A/en not_active Expired - Lifetime
- 1966-10-04 BE BE687782D patent/BE687782A/xx unknown
- 1966-10-04 ES ES0332400A patent/ES332400A1/en not_active Expired
- 1966-10-04 AT AT927966A patent/AT267026B/en active
- 1966-10-04 SE SE13364/66A patent/SE346556B/xx unknown
- 1966-10-04 NL NL6613968A patent/NL6613968A/xx unknown
- 1966-10-04 CH CH1429266A patent/CH508563A/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
DE1568189A1 (en) | 1970-02-05 |
SE346556B (en) | 1972-07-10 |
GB1141809A (en) | 1969-02-05 |
DE1568189B2 (en) | 1974-05-22 |
BE687782A (en) | 1967-04-04 |
CH508563A (en) | 1971-06-15 |
FR1498696A (en) | 1967-10-20 |
DE1568189C3 (en) | 1975-01-02 |
NO120151B (en) | 1970-09-07 |
US3484496A (en) | 1969-12-16 |
AT267026B (en) | 1968-12-10 |
NL6613968A (en) | 1967-04-05 |
IL26615A (en) | 1970-07-19 |
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