NO311501B1 - Katalysator basert på edelmetall og silisiumdioksyd/aluminiumoksyd, samt fremgangsmåte forhydroisomerisering av tunge utgangsmaterialer - Google Patents
Katalysator basert på edelmetall og silisiumdioksyd/aluminiumoksyd, samt fremgangsmåte forhydroisomerisering av tunge utgangsmaterialer Download PDFInfo
- Publication number
- NO311501B1 NO311501B1 NO19954876A NO954876A NO311501B1 NO 311501 B1 NO311501 B1 NO 311501B1 NO 19954876 A NO19954876 A NO 19954876A NO 954876 A NO954876 A NO 954876A NO 311501 B1 NO311501 B1 NO 311501B1
- Authority
- NO
- Norway
- Prior art keywords
- catalyst according
- pore volume
- catalyst
- weight
- mean diameter
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title claims description 60
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 title claims description 28
- 239000007858 starting material Substances 0.000 title claims description 24
- 239000000377 silicon dioxide Substances 0.000 title claims description 14
- 238000000034 method Methods 0.000 title claims description 12
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 title claims description 11
- 239000010970 precious metal Substances 0.000 title claims description 6
- 239000011148 porous material Substances 0.000 claims description 48
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 29
- 229910052751 metal Inorganic materials 0.000 claims description 21
- 239000002184 metal Substances 0.000 claims description 21
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 13
- 238000009826 distribution Methods 0.000 claims description 13
- 229910052739 hydrogen Inorganic materials 0.000 claims description 13
- 239000001257 hydrogen Substances 0.000 claims description 13
- 235000012239 silicon dioxide Nutrition 0.000 claims description 13
- 229910052697 platinum Inorganic materials 0.000 claims description 12
- 229910000510 noble metal Inorganic materials 0.000 claims description 11
- 239000006185 dispersion Substances 0.000 claims description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- 239000010457 zeolite Substances 0.000 claims description 4
- 229910021536 Zeolite Inorganic materials 0.000 claims description 3
- 238000009835 boiling Methods 0.000 claims description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 3
- 229910021417 amorphous silicon Inorganic materials 0.000 claims description 2
- 229910052736 halogen Inorganic materials 0.000 claims description 2
- 150000002367 halogens Chemical class 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 239000003208 petroleum Substances 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 description 11
- 239000003921 oil Substances 0.000 description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 7
- 239000001301 oxygen Substances 0.000 description 7
- 239000002253 acid Substances 0.000 description 6
- 239000010687 lubricating oil Substances 0.000 description 6
- 238000005984 hydrogenation reaction Methods 0.000 description 5
- 238000006317 isomerization reaction Methods 0.000 description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- 238000004517 catalytic hydrocracking Methods 0.000 description 4
- 125000004432 carbon atom Chemical group C* 0.000 description 3
- 238000005470 impregnation Methods 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 3
- 230000000737 periodic effect Effects 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012634 fragment Substances 0.000 description 2
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 2
- 229910052753 mercury Inorganic materials 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000011959 amorphous silica alumina Substances 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000001588 bifunctional effect Effects 0.000 description 1
- 230000002902 bimodal effect Effects 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000009795 derivation Methods 0.000 description 1
- 238000011066 ex-situ storage Methods 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910052741 iridium Inorganic materials 0.000 description 1
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 229910052762 osmium Inorganic materials 0.000 description 1
- SYQBFIAQOQZEGI-UHFFFAOYSA-N osmium atom Chemical compound [Os] SYQBFIAQOQZEGI-UHFFFAOYSA-N 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 150000003057 platinum Chemical class 0.000 description 1
- 229910052703 rhodium Inorganic materials 0.000 description 1
- 239000010948 rhodium Substances 0.000 description 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 238000004448 titration Methods 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000004876 x-ray fluorescence Methods 0.000 description 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
- C10G45/58—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
- C10G45/62—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 platinum group 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/615—100-500 m2/g
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/63—Pore volume
- B01J35/635—0.5-1.0 ml/g
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
- B01J35/647—2-50 nm
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/66—Pore distribution
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/66—Pore distribution
- B01J35/67—Pore distribution monomodal
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/66—Pore distribution
- B01J35/69—Pore distribution bimodal
-
- 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/12—Silica and alumina
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Crystallography & Structural Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR9403866A FR2718060B1 (fr) | 1994-04-01 | 1994-04-01 | Catalyseur pour la conversion de charges hydrocarbonées, à base de métal noble et silice-alumine. |
FR9403867A FR2718144B1 (fr) | 1994-04-01 | 1994-04-01 | Procédé de traitement avec hydroisomérisation de charges lourdes. |
PCT/FR1995/000352 WO1995026819A1 (fr) | 1994-04-01 | 1995-03-22 | Catalyseur a base de metal noble et silice-alumine et procede de traitement avec hydroisomerisation de charges lourdes |
Publications (3)
Publication Number | Publication Date |
---|---|
NO954876L NO954876L (no) | 1995-11-30 |
NO954876D0 NO954876D0 (no) | 1995-11-30 |
NO311501B1 true NO311501B1 (no) | 2001-12-03 |
Family
ID=26231063
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO19954876A NO311501B1 (no) | 1994-04-01 | 1995-11-30 | Katalysator basert på edelmetall og silisiumdioksyd/aluminiumoksyd, samt fremgangsmåte forhydroisomerisering av tunge utgangsmaterialer |
Country Status (10)
Country | Link |
---|---|
US (1) | US5879539A (ja) |
EP (1) | EP0701480B1 (ja) |
JP (1) | JP3843345B2 (ja) |
KR (1) | KR100336723B1 (ja) |
CN (1) | CN1071134C (ja) |
DE (1) | DE69511974T2 (ja) |
ES (1) | ES2138730T3 (ja) |
NO (1) | NO311501B1 (ja) |
RU (1) | RU2141380C1 (ja) |
WO (1) | WO1995026819A1 (ja) |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1123383C (zh) * | 1997-09-10 | 2003-10-08 | 中国石油化工集团公司 | 一种无定形硅铝及其制备方法 |
NL1015035C2 (nl) * | 1999-04-29 | 2001-02-12 | Inst Francais Du Petrole | Flexibel proces voor de productie van basisoliÙn en destillatieproducten door een omzetting-hydroisomerisatie op een weinig gedispergeerde katalysator, gevolgd door een katalytische ontparaffinering. |
FR2792851B1 (fr) * | 1999-04-29 | 2002-04-05 | Inst Francais Du Petrole | Catalyseur a base de metal noble faiblement disperse et son utilisation pour la conversion de charges hydrocarbonees |
CN1102077C (zh) * | 1999-06-25 | 2003-02-26 | 李海 | 一种支撑、复盖催化剂的保护剂及其制造方法 |
FR2846574B1 (fr) * | 2002-10-30 | 2006-05-26 | Inst Francais Du Petrole | Catalyseur et procede d'hydrocraquage de charges hydrocarbonees |
US7030053B2 (en) * | 2002-11-06 | 2006-04-18 | Conocophillips Company | Catalyst composition comprising ruthenium and a treated silica support component and processes therefor and therewith for preparing high molecular weight hydrocarbons such as polymethylene |
US6995112B2 (en) * | 2002-11-08 | 2006-02-07 | Chevron U.S.A. Inc. | Highly homogeneous amorphous silica-alumina catalyst composition |
US6902664B2 (en) * | 2002-11-08 | 2005-06-07 | Chevron U.S.A. Inc. | Extremely low acidity USY and homogeneous, amorphous silica-alumina hydrocracking catalyst and process |
FR2851569B1 (fr) * | 2003-02-21 | 2007-04-20 | Inst Francais Du Petrole | Procede d'hydrocraquage en deux etapes utilisant un catalyseur amorphe a base de platine et de palladium |
US7943547B2 (en) * | 2005-09-14 | 2011-05-17 | Hamilton Sundstrand Space Systems International, Inc. | Selective catalytic oxidation of ammonia to water and nitrogen |
US8114806B2 (en) * | 2008-04-10 | 2012-02-14 | Shell Oil Company | Catalysts having selected pore size distributions, method of making such catalysts, methods of producing a crude product, products obtained from such methods, and uses of products obtained |
US9187702B2 (en) * | 2009-07-01 | 2015-11-17 | Chevron U.S.A. Inc. | Hydroprocessing catalyst and method of making the same |
US9084983B2 (en) * | 2009-12-15 | 2015-07-21 | Basf Se | Catalyst and process for hydrogenating aromatics |
US11559789B2 (en) * | 2021-03-11 | 2023-01-24 | Chevron U.S.A. Inc. | Base oil hydrotreating catalyst and process of use |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6021802A (ja) * | 1983-07-15 | 1985-02-04 | Daido Sanso Kk | 均一な細孔を有する金属酸化物、その製造方法およびその金属酸化物からなる触媒用担体 |
DD223077B1 (de) * | 1984-04-23 | 1989-04-12 | Leuna Werke Veb | Verfahren zur herstellung eines katalysators fuer die kohlenwasserstoffreformierung |
FR2563120A1 (fr) * | 1984-04-23 | 1985-10-25 | Leuna Werke Veb | Catalyseur pour le reformage d'hydrocarbures, et procede pour sa fabrication |
JPS6115739A (ja) * | 1984-04-25 | 1986-01-23 | Toa Nenryo Kogyo Kk | 水素化処理用触媒 |
FR2565504B1 (fr) * | 1984-06-07 | 1986-08-29 | Inst Francais Du Petrole | Procede de fabrication d'un catalyseur d'hydrocraquage de fractions petrolieres lourdes |
US5157187A (en) * | 1991-01-02 | 1992-10-20 | Mobil Oil Corp. | Hydroisomerization process for pour point reduction of long chain alkyl aromatic compounds |
US5187138A (en) * | 1991-09-16 | 1993-02-16 | Exxon Research And Engineering Company | Silica modified hydroisomerization catalyst |
-
1995
- 1995-03-22 US US08/556,943 patent/US5879539A/en not_active Expired - Lifetime
- 1995-03-22 DE DE69511974T patent/DE69511974T2/de not_active Expired - Lifetime
- 1995-03-22 JP JP52544095A patent/JP3843345B2/ja not_active Expired - Lifetime
- 1995-03-22 ES ES95914399T patent/ES2138730T3/es not_active Expired - Lifetime
- 1995-03-22 WO PCT/FR1995/000352 patent/WO1995026819A1/fr active IP Right Grant
- 1995-03-22 KR KR1019950705395A patent/KR100336723B1/ko not_active IP Right Cessation
- 1995-03-22 CN CN95190229A patent/CN1071134C/zh not_active Expired - Lifetime
- 1995-03-22 EP EP95914399A patent/EP0701480B1/fr not_active Expired - Lifetime
- 1995-03-31 RU RU95104891A patent/RU2141380C1/ru active
- 1995-11-30 NO NO19954876A patent/NO311501B1/no not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
CN1125912A (zh) | 1996-07-03 |
JP3843345B2 (ja) | 2006-11-08 |
RU95104891A (ru) | 1996-12-27 |
NO954876L (no) | 1995-11-30 |
NO954876D0 (no) | 1995-11-30 |
KR960702770A (ko) | 1996-05-23 |
EP0701480B1 (fr) | 1999-09-08 |
CN1071134C (zh) | 2001-09-19 |
RU2141380C1 (ru) | 1999-11-20 |
KR100336723B1 (ko) | 2002-11-18 |
DE69511974T2 (de) | 2000-05-31 |
US5879539A (en) | 1999-03-09 |
JPH08511199A (ja) | 1996-11-26 |
WO1995026819A1 (fr) | 1995-10-12 |
ES2138730T3 (es) | 2000-01-16 |
DE69511974D1 (de) | 1999-10-14 |
EP0701480A1 (fr) | 1996-03-20 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
NO315123B1 (no) | Fremgangsmåte for hydroisomerisering av utgangsmaterialer som stammer fra Fischer-Tropsch-syntesen | |
Calemma et al. | Upgrading of LCO by partial hydrogenation of aromatics and ring opening of naphthenes over bi-functional catalysts | |
JP4224637B2 (ja) | 転化/水素化異性化とそれに続く接触脱パラフィンにより基油および中間溜出物を製造するための改良された融通性のある方法 | |
NO311501B1 (no) | Katalysator basert på edelmetall og silisiumdioksyd/aluminiumoksyd, samt fremgangsmåte forhydroisomerisering av tunge utgangsmaterialer | |
CA2109228C (en) | High porosity, high surface area isomerization catalyst and its use | |
Camblor et al. | Mild hydrocracking of vacuum gasoil over NiMo-Beta zeolite catalysts: the role of the location of the NiMo phases and the crystallite size of the zeolite | |
JP3581198B2 (ja) | ロウ性原料の水素異性化方法 | |
EP3356035B1 (en) | Process for producing aromatics from a heavy hydrocarbon feed | |
NO335873B1 (no) | Fremgangsmåte for fremstilling av mellomdestillater fra lineære parafiner. | |
NO171318B (no) | Fremgangsmaate for hydroisomerisering og hydrokrakking av fischer-tropsch-voks for aa fremstille synkrud og forbedrede hydrokarbonprodukter | |
RU2291184C2 (ru) | Способ получения средних дистиллятов гидроизомеризацией и гидрокрекингом в две стадии сырья, полученного синтезом фишера-тропша, и установка для его осуществления | |
KR20010049307A (ko) | 분산도가 낮은 귀금속계 촉매 및 탄화수소 공급원료의전환 반응에서의 이의 용도 | |
NO116209B (ja) | ||
NO335524B1 (no) | Fremgangsmåte for å fremstille mellomdestillater fra en parafintilførsel fremstilt av Fischer-Tropsch prosessen | |
KR20000071874A (ko) | 전환-수소화 이성화 반응후 접촉 탈왁스화 처리에 의한베이스 오일 및 중간 증류물의 융통적인 제조 방법 | |
RU2345123C2 (ru) | Способ получения средних дистиллятов и основ для смазки, исходя из синтетического углеводородного сырья | |
NO335525B1 (no) | Fremgangsmåte for fremstilling av mellomdestillater fra en parafinfødestrøm fremstilt av Fischer-Tropsch prosessen | |
NO335523B1 (no) | Fremgangsmåte og apparat for fremstilling av mellomdestillater fra en parafintilførsel fremstilt av Fischer-Tropsch prosessen. | |
RU97103141A (ru) | Способ получения смазочного масла с использованием катализатора с высокой селективностью индекса | |
EP0070125B1 (en) | Crystalline silica zeolite-containing catalyst and hydrocarbon hydroprocess utilizing the catalyst | |
EP1404783B1 (en) | Process for the production of paraffinic middle distillates | |
Jahangiri et al. | Preparation of Pt/Al2O3-Cl catalyst and investigation of operating variables effects on isomerization reaction | |
US4959337A (en) | Wax isomerization catalyst and method for its production | |
NO311178B1 (no) | Fremgangsmåte for å undertrykke CH4-utbyttet ved hydroisomerisering av en C5+-parafininnmatning | |
Golubev et al. | Development of protective-layer catalysts for removal of chlorine compounds from diesel fractions |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
MK1K | Patent expired |