FR2385790A1 - - Google Patents
Info
- Publication number
- FR2385790A1 FR2385790A1 FR7809158A FR7809158A FR2385790A1 FR 2385790 A1 FR2385790 A1 FR 2385790A1 FR 7809158 A FR7809158 A FR 7809158A FR 7809158 A FR7809158 A FR 7809158A FR 2385790 A1 FR2385790 A1 FR 2385790A1
- Authority
- FR
- France
- Prior art keywords
- hydrogen
- white oil
- investment
- viii
- halogen
- 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.)
- Granted
Links
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 3
- 229910052739 hydrogen Inorganic materials 0.000 abstract 3
- 239000001257 hydrogen Substances 0.000 abstract 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract 1
- 239000004215 Carbon black (E152) Substances 0.000 abstract 1
- 125000003118 aryl group Chemical group 0.000 abstract 1
- 229910052799 carbon Inorganic materials 0.000 abstract 1
- 239000003054 catalyst Substances 0.000 abstract 1
- 150000001875 compounds Chemical class 0.000 abstract 1
- 229910052736 halogen Inorganic materials 0.000 abstract 1
- 150000002367 halogens Chemical class 0.000 abstract 1
- 229930195733 hydrocarbon Natural products 0.000 abstract 1
- 150000002430 hydrocarbons Chemical class 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 229910052751 metal Inorganic materials 0.000 abstract 1
- 239000002184 metal Substances 0.000 abstract 1
- 150000002739 metals Chemical class 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 230000000737 periodic effect Effects 0.000 abstract 1
- 239000000377 silicon dioxide Substances 0.000 abstract 1
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
- C10G45/44—Hydrogenation of the aromatic hydrocarbons
-
- 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/14—White oil, eating oil
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)
- Catalysts (AREA)
Abstract
Fabrication d'huile blanche. On met en contact une charge d'hydrocarbure contenant moins de 7 % de carbone aromatique (selon la norme ASTM D 2140) de préférence en une unique étape, avec un catalyseur constitué par des métaux (ou leurs composés) des groupes VI B et VIII du tableau périodique des élements, sur un support exempt de silice et d'halogène, en présence d'hydrogene à température de 260 à 330 degrés C, sous une pression partielle d'hydrogène de 20 à 60 bars, un rapport entre l'hydrogène et la charge de 50 à 500 lites normaux de H2 par litre et de préférence avec une vitesse spatiale de 0,1 à 5,0 v/heure/v, et on recueille l'huile blanche à partir des produits formés lors de cette étape. Les frais d'investissement en équipement et de fonctionnement sont plus faibles qu'avec les procédés classiques.Manufacture of white oil. A hydrocarbon feed containing less than 7% of aromatic carbon (according to standard ASTM D 2140) is brought into contact, preferably in a single step, with a catalyst consisting of metals (or their compounds) of groups VI B and VIII. of the Periodic Table of the Elements, on a support free of silica and halogen, in the presence of hydrogen at a temperature of 260 to 330 degrees C, under a partial pressure of hydrogen of 20 to 60 bars, a ratio of hydrogen and charging 50 to 500 normal liters of H2 per liter and preferably with a space velocity of 0.1 to 5.0 v / hour / v, and the white oil is collected from the products formed in this step . The investment in equipment and operating costs are lower than with conventional processes.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB13388/77A GB1597165A (en) | 1977-03-30 | 1977-03-30 | White oils and method of making same |
Publications (2)
Publication Number | Publication Date |
---|---|
FR2385790A1 true FR2385790A1 (en) | 1978-10-27 |
FR2385790B1 FR2385790B1 (en) | 1983-08-12 |
Family
ID=10022062
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FR7809158A Expired FR2385790B1 (en) | 1977-03-30 | 1978-03-29 |
Country Status (6)
Country | Link |
---|---|
JP (1) | JPS53121805A (en) |
DE (1) | DE2813571A1 (en) |
FR (1) | FR2385790B1 (en) |
GB (1) | GB1597165A (en) |
IT (1) | IT1156182B (en) |
NL (1) | NL7803416A (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3143869A1 (en) * | 1981-11-05 | 1983-05-11 | Basf Ag, 6700 Ludwigshafen | METHOD FOR PRODUCING TECHNICAL WHITE OILS BY HYDRATION |
JPS58109592A (en) * | 1981-12-22 | 1983-06-29 | アトランテイツク・リツチフイ−ルド・カンパニ− | Manufacture of white mineral oil from mineral hydrocarbon oil having lubricant oil viscosity |
US5019662A (en) * | 1988-05-19 | 1991-05-28 | Uop | Process for the production of white oil from heavy aromatic alkylate |
US5057206A (en) * | 1988-08-25 | 1991-10-15 | Uop | Process for the production of white oils |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1256037A (en) * | 1960-02-02 | 1961-03-17 | Exxon Research Engineering Co | Refining process to obtain a high yield of white oil |
FR2080537A1 (en) * | 1970-02-16 | 1971-11-19 | Exxon Research Engineering Co | |
DE2240600A1 (en) * | 1971-08-20 | 1973-03-08 | British Petroleum Co | CATALYTIC TREATMENT OF NPARAFFINES |
US3959122A (en) * | 1972-02-24 | 1976-05-25 | Sun Oil Company Of Pennsylvania | Making a white oil by hydrogenation with a sulfided nickel and molybdenum catalyst |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3393148A (en) * | 1965-11-30 | 1968-07-16 | Standard Oil Co | Hydrofining catalyst and process using same |
US3459656A (en) * | 1966-08-16 | 1969-08-05 | Sinclair Research Inc | Making a white oil by two stages of catalytic hydrogenation |
US3553107A (en) * | 1968-06-05 | 1971-01-05 | Gulf Research Development Co | Production of white oils from hydrotreated and acid contacted oil stocks |
GB1345972A (en) * | 1971-06-23 | 1974-02-06 | British Petroleum Co | Production of white oils |
NL172756C (en) * | 1972-11-09 | 1983-10-17 | Shell Int Research | PROCESS FOR PREPARING A TECHNICAL WHITE OIL. |
DE2300038C2 (en) * | 1973-01-02 | 1987-05-07 | Basf Ag, 6700 Ludwigshafen | Use of a sulfurized catalyst for the production of technical white oils |
GB1476426A (en) * | 1973-07-03 | 1977-06-16 | Shell Int Research | Process for preparing white oils |
GB1476428A (en) * | 1973-07-03 | 1977-06-16 | Shell Int Research | Process for preparing white oils |
CA1069452A (en) * | 1974-04-11 | 1980-01-08 | Atlantic Richfield Company | Production of white oils by two stages of hydrogenation |
-
1977
- 1977-03-30 GB GB13388/77A patent/GB1597165A/en not_active Expired
-
1978
- 1978-03-24 JP JP3397878A patent/JPS53121805A/en active Pending
- 1978-03-28 IT IT7848627A patent/IT1156182B/en active
- 1978-03-29 DE DE19782813571 patent/DE2813571A1/en not_active Ceased
- 1978-03-29 FR FR7809158A patent/FR2385790B1/fr not_active Expired
- 1978-03-30 NL NL7803416A patent/NL7803416A/en not_active Application Discontinuation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1256037A (en) * | 1960-02-02 | 1961-03-17 | Exxon Research Engineering Co | Refining process to obtain a high yield of white oil |
FR2080537A1 (en) * | 1970-02-16 | 1971-11-19 | Exxon Research Engineering Co | |
DE2240600A1 (en) * | 1971-08-20 | 1973-03-08 | British Petroleum Co | CATALYTIC TREATMENT OF NPARAFFINES |
US3959122A (en) * | 1972-02-24 | 1976-05-25 | Sun Oil Company Of Pennsylvania | Making a white oil by hydrogenation with a sulfided nickel and molybdenum catalyst |
Also Published As
Publication number | Publication date |
---|---|
JPS53121805A (en) | 1978-10-24 |
DE2813571A1 (en) | 1978-10-05 |
GB1597165A (en) | 1981-09-03 |
IT1156182B (en) | 1987-01-28 |
NL7803416A (en) | 1978-10-03 |
IT7848627A0 (en) | 1978-03-28 |
FR2385790B1 (en) | 1983-08-12 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
ST | Notification of lapse |