NO316647B1 - Fremgangsmate for fremstilling av mellomdestillater ved hydrokrakking av tung destillatolje - Google Patents
Fremgangsmate for fremstilling av mellomdestillater ved hydrokrakking av tung destillatolje Download PDFInfo
- Publication number
- NO316647B1 NO316647B1 NO19986095A NO986095A NO316647B1 NO 316647 B1 NO316647 B1 NO 316647B1 NO 19986095 A NO19986095 A NO 19986095A NO 986095 A NO986095 A NO 986095A NO 316647 B1 NO316647 B1 NO 316647B1
- Authority
- NO
- Norway
- Prior art keywords
- alumina
- weight
- catalyst
- zeolite
- hydrocracking
- Prior art date
Links
- 238000004517 catalytic hydrocracking Methods 0.000 title claims description 60
- 238000004519 manufacturing process Methods 0.000 title claims description 11
- 239000003054 catalyst Substances 0.000 claims description 112
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 105
- 238000000034 method Methods 0.000 claims description 82
- 239000010457 zeolite Substances 0.000 claims description 43
- 229910021536 Zeolite Inorganic materials 0.000 claims description 42
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 41
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 39
- 239000011148 porous material Substances 0.000 claims description 35
- 229910052731 fluorine Inorganic materials 0.000 claims description 30
- 239000011737 fluorine Substances 0.000 claims description 28
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 26
- 229910052739 hydrogen Inorganic materials 0.000 claims description 26
- 239000001257 hydrogen Substances 0.000 claims description 26
- 238000001354 calcination Methods 0.000 claims description 23
- 239000002131 composite material Substances 0.000 claims description 20
- 229910052757 nitrogen Inorganic materials 0.000 claims description 20
- 238000009826 distribution Methods 0.000 claims description 14
- 239000007789 gas Substances 0.000 claims description 14
- 239000002253 acid Substances 0.000 claims description 13
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 11
- 229910052708 sodium Inorganic materials 0.000 claims description 11
- 239000011734 sodium Substances 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 10
- 229910000480 nickel oxide Inorganic materials 0.000 claims description 10
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 claims description 10
- 229910001593 boehmite Inorganic materials 0.000 claims description 9
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 claims description 9
- QGLKJKCYBOYXKC-UHFFFAOYSA-N nonaoxidotritungsten Chemical compound O=[W]1(=O)O[W](=O)(=O)O[W](=O)(=O)O1 QGLKJKCYBOYXKC-UHFFFAOYSA-N 0.000 claims description 9
- 229910001930 tungsten oxide Inorganic materials 0.000 claims description 9
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 8
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 8
- 229910052680 mordenite Inorganic materials 0.000 claims description 7
- 229910052717 sulfur Inorganic materials 0.000 claims description 7
- 239000011593 sulfur Substances 0.000 claims description 7
- 239000001569 carbon dioxide Substances 0.000 claims description 6
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 6
- 238000001179 sorption measurement Methods 0.000 claims description 6
- 238000009835 boiling Methods 0.000 claims description 5
- 230000007062 hydrolysis Effects 0.000 claims description 5
- 238000006460 hydrolysis reaction Methods 0.000 claims description 5
- 238000004438 BET method Methods 0.000 claims description 4
- 150000002910 rare earth metals Chemical group 0.000 claims description 4
- 230000003197 catalytic effect Effects 0.000 claims description 3
- 125000005234 alkyl aluminium group Chemical group 0.000 claims description 2
- 238000004939 coking Methods 0.000 claims description 2
- 239000012013 faujasite Substances 0.000 claims description 2
- 238000000926 separation method Methods 0.000 claims description 2
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 claims 3
- 229910000329 aluminium sulfate Inorganic materials 0.000 claims 1
- 239000003921 oil Substances 0.000 description 28
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 25
- 239000007864 aqueous solution Substances 0.000 description 23
- 238000006243 chemical reaction Methods 0.000 description 19
- 239000002994 raw material Substances 0.000 description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 16
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 15
- 239000000047 product Substances 0.000 description 13
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 12
- 238000001125 extrusion Methods 0.000 description 9
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 8
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 8
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 description 8
- 239000002243 precursor Substances 0.000 description 8
- DDFHBQSCUXNBSA-UHFFFAOYSA-N 5-(5-carboxythiophen-2-yl)thiophene-2-carboxylic acid Chemical compound S1C(C(=O)O)=CC=C1C1=CC=C(C(O)=O)S1 DDFHBQSCUXNBSA-UHFFFAOYSA-N 0.000 description 7
- 238000001035 drying Methods 0.000 description 7
- 238000002360 preparation method Methods 0.000 description 7
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 7
- 238000005470 impregnation Methods 0.000 description 6
- 229910052759 nickel Inorganic materials 0.000 description 6
- MOWMLACGTDMJRV-UHFFFAOYSA-N nickel tungsten Chemical compound [Ni].[W] MOWMLACGTDMJRV-UHFFFAOYSA-N 0.000 description 6
- 229910052721 tungsten Inorganic materials 0.000 description 6
- 239000010937 tungsten Substances 0.000 description 6
- 229910052782 aluminium Inorganic materials 0.000 description 5
- 239000011230 binding agent Substances 0.000 description 5
- 239000013065 commercial product Substances 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 238000011068 loading method Methods 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 229910021529 ammonia Inorganic materials 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 3
- 125000003118 aryl group Chemical group 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 239000000295 fuel oil Substances 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 239000003208 petroleum Substances 0.000 description 3
- 239000012265 solid product Substances 0.000 description 3
- 238000010998 test method Methods 0.000 description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 2
- MQRWBMAEBQOWAF-UHFFFAOYSA-N acetic acid;nickel Chemical compound [Ni].CC(O)=O.CC(O)=O MQRWBMAEBQOWAF-UHFFFAOYSA-N 0.000 description 2
- SMZOGRDCAXLAAR-UHFFFAOYSA-N aluminium isopropoxide Chemical compound [Al+3].CC(C)[O-].CC(C)[O-].CC(C)[O-] SMZOGRDCAXLAAR-UHFFFAOYSA-N 0.000 description 2
- VXAUWWUXCIMFIM-UHFFFAOYSA-M aluminum;oxygen(2-);hydroxide Chemical compound [OH-].[O-2].[Al+3] VXAUWWUXCIMFIM-UHFFFAOYSA-M 0.000 description 2
- 229910001680 bayerite Inorganic materials 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 239000008367 deionised water Substances 0.000 description 2
- 229910021641 deionized water Inorganic materials 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 230000002431 foraging effect Effects 0.000 description 2
- 229910000040 hydrogen fluoride Inorganic materials 0.000 description 2
- 150000002484 inorganic compounds Chemical class 0.000 description 2
- 229910010272 inorganic material Inorganic materials 0.000 description 2
- 239000003350 kerosene Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000012263 liquid product Substances 0.000 description 2
- 238000000691 measurement method Methods 0.000 description 2
- 229940078494 nickel acetate Drugs 0.000 description 2
- 239000003223 protective agent Substances 0.000 description 2
- 229910001404 rare earth metal oxide Inorganic materials 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 1
- 229910018104 Ni-P Inorganic materials 0.000 description 1
- 229910018536 Ni—P Inorganic materials 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- LDDQLRUQCUTJBB-UHFFFAOYSA-N ammonium fluoride Chemical compound [NH4+].[F-] LDDQLRUQCUTJBB-UHFFFAOYSA-N 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- 238000004523 catalytic cracking Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000011874 heated mixture Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 238000006317 isomerization reaction Methods 0.000 description 1
- 125000001477 organic nitrogen group Chemical group 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 238000005504 petroleum refining Methods 0.000 description 1
- 238000001637 plasma atomic emission spectroscopy Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000002076 thermal analysis method Methods 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
- 238000004846 x-ray emission Methods 0.000 description 1
- -1 zeolite X Chemical compound 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
- 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
- C10G65/12—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including cracking steps and other hydrotreatment steps
-
- 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
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/888—Tungsten
-
- 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
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/06—Halogens; Compounds thereof
- B01J27/132—Halogens; Compounds thereof with chromium, molybdenum, tungsten or polonium
-
- 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
- C10G45/08—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 in combination with chromium, molybdenum, or tungsten metals, 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
- 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
- C10G47/16—Crystalline alumino-silicate carriers
- C10G47/18—Crystalline alumino-silicate carriers the catalyst containing platinum group metals or compounds thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Crystallography & Structural Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96106724 | 1996-06-28 | ||
| CN96106587 | 1996-06-28 | ||
| CN96109007 | 1996-07-22 | ||
| PCT/CN1997/000064 WO1998000384A1 (fr) | 1996-06-28 | 1997-06-27 | Procede d'hydrocraquage d'une huile de distillat lourde a des pressions moyennes |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| NO986095D0 NO986095D0 (no) | 1998-12-23 |
| NO986095L NO986095L (no) | 1999-02-26 |
| NO316647B1 true NO316647B1 (no) | 2004-03-22 |
Family
ID=27179089
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NO19986095A NO316647B1 (no) | 1996-06-28 | 1998-12-23 | Fremgangsmate for fremstilling av mellomdestillater ved hydrokrakking av tung destillatolje |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US5954944A (id) |
| EP (1) | EP0947575B1 (id) |
| JP (1) | JP2001503451A (id) |
| AU (1) | AU3252797A (id) |
| HR (1) | HRP970357B1 (id) |
| ID (1) | ID17947A (id) |
| NO (1) | NO316647B1 (id) |
| WO (1) | WO1998000384A1 (id) |
Families Citing this family (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6129904A (en) * | 1996-09-19 | 2000-10-10 | Sud-Chemie A.G. | Aluminum oxide masses with very narrow pore radius distribution |
| CN1096296C (zh) | 1998-11-13 | 2002-12-18 | 中国石油化工集团公司 | 一种生产中间馏分油的加氢裂化催化剂及其制备 |
| FR2815041B1 (fr) * | 2000-10-05 | 2018-07-06 | IFP Energies Nouvelles | Procede de production de diesel par hydrocraquage a pression moderee |
| EP1342774A1 (en) | 2002-03-06 | 2003-09-10 | ExxonMobil Chemical Patents Inc. | A process for the production of hydrocarbon fluids |
| US20040040890A1 (en) * | 2002-08-30 | 2004-03-04 | Morton Robert W. | Desulfurization and novel compositions for same |
| CN1296135C (zh) * | 2003-09-28 | 2007-01-24 | 中国石油化工股份有限公司 | 一种大孔氧化铝载体及其制备方法 |
| CN100412172C (zh) * | 2004-09-07 | 2008-08-20 | 白跃华 | 一种柴油加氢改质的新工艺 |
| US8883669B2 (en) * | 2005-04-29 | 2014-11-11 | China Petroleum & Chemical Corporation | Hydrocracking catalyst, a process for producing the same, and the use of the same |
| US8980081B2 (en) * | 2007-10-22 | 2015-03-17 | Chevron U.S.A. Inc. | Method of making high energy distillate fuels |
| US9127217B2 (en) * | 2007-12-21 | 2015-09-08 | Chevron U.S.A. Inc. | Method of making high energy distillate fuels |
| CN103480410B (zh) * | 2012-06-12 | 2016-08-24 | 中国石油化工股份有限公司 | 具有加氢催化作用的催化剂及其制备方法和应用以及加氢处理方法 |
| JP6038708B2 (ja) * | 2013-03-29 | 2016-12-07 | Ｊｘエネルギー株式会社 | 石油製品の製造方法 |
| US10208261B2 (en) | 2014-02-12 | 2019-02-19 | Lummus Technology Inc. | Processing vacuum residuum and vacuum gas oil in ebullated bed reactor systems |
| US10213772B2 (en) | 2015-04-10 | 2019-02-26 | Chevron U.S.A. Inc. | Middle distillate hydrocracking catalyst containing zeolite USY with enhanced acid sites |
| US10040058B2 (en) | 2015-08-11 | 2018-08-07 | Chevron U.S.A. Inc. | Middle distillate hydrocracking catalyst containing zeolite USY, and zeolite beta with low acidity and large domain size |
| US10183286B2 (en) | 2015-08-11 | 2019-01-22 | Chevron U.S.A. Inc. | Noble metal zeolite catalyst for second-stage hydrocracking to make middle distillate |
| US10046317B2 (en) | 2015-08-11 | 2018-08-14 | Chevron U.S.A. Inc. | Middle distillate hydrocracking catalyst containing zeolite beta with low OD acidity and large domain size |
| US9919293B1 (en) * | 2017-07-17 | 2018-03-20 | Kuwait Institute For Scientific Research | Catalyst for mild-hydrocracking of residual oil |
| CN109722290B (zh) * | 2017-10-27 | 2021-04-06 | 中国石油化工股份有限公司 | 降低高干点航煤冰点的方法 |
| MY207871A (en) * | 2017-12-29 | 2025-03-25 | Lummus Technology Inc | Conversion of heavy fuel oil to chemicals |
| KR20200086983A (ko) * | 2019-01-10 | 2020-07-20 | 코아텍주식회사 | 대용량 과불화화합물 제거를 위한 금속산화물 촉매 및 그 제조 방법 |
Family Cites Families (49)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2847358A (en) * | 1954-09-24 | 1958-08-12 | California Research Corp | Conversion of wax into oil |
| US3132089A (en) * | 1960-12-23 | 1964-05-05 | Union Oil Co | Hydrocracking process with pre-hydrogenation |
| US3159568A (en) * | 1961-10-02 | 1964-12-01 | Union Oil Co | Low pressure hydrocracking process with hydrofining of feed |
| US3779903A (en) * | 1967-12-11 | 1973-12-18 | Shell Oil Co | Hydroconversion process with a catalyst having a hydrogenation component composited with a high density alumina |
| US3554898A (en) * | 1968-08-29 | 1971-01-12 | Union Oil Co | Recycle hydrocracking process for converting heavy oils to middle distillates |
| US3592757A (en) * | 1969-03-17 | 1971-07-13 | Union Oil Co | Combination hydrocracking-hydrogenation process |
| US3673112A (en) * | 1970-05-13 | 1972-06-27 | Shell Oil Co | Hydroconversion catalyst preparation |
| CA967986A (en) * | 1971-03-26 | 1975-05-20 | Grace (W. R.) And Co. | Preparation of macroporous alumina extrudates |
| GB1399379A (en) * | 1971-07-14 | 1975-07-02 | Nippon Oil Co Ltd | Process for the preparation of a hydrocarbon conversion catalyst |
| US3923638A (en) * | 1971-12-10 | 1975-12-02 | Standard Oil Co | Two-catalyst hydrocracking process |
| US4175033A (en) * | 1976-05-06 | 1979-11-20 | Uop Inc. | Hydroprocessing of hydrocarbons over nickel, moly, platinum catalyst |
| US4138326A (en) * | 1977-08-12 | 1979-02-06 | Gulf Research & Development | Hydrotreating process and catalyst |
| US4225421A (en) * | 1979-03-13 | 1980-09-30 | Standard Oil Company (Indiana) | Process for hydrotreating heavy hydrocarbons |
| US4618594A (en) * | 1979-03-19 | 1986-10-21 | Standard Oil Company (Indiana) | Catalyst and process for the hydrodenitrogenation and hydrocracking of high-nitrogen feeds |
| NL191266C (nl) * | 1979-05-25 | 1995-04-18 | Shell Int Research | Werkwijze voor de bereiding van lichte koolwaterstoffracties. |
| CA1143712A (en) * | 1979-06-05 | 1983-03-29 | Gerard T. Pott | Process for the preparation of a sulphided fluorine-containing nickel-tungsten catalyst and a process for the conversion of hydrocarbons, and the resulting hydrocarbons |
| US4419271A (en) * | 1979-10-15 | 1983-12-06 | Union Oil Company Of California | Hydrocarbon conversion catalyst |
| US4672048A (en) * | 1979-10-15 | 1987-06-09 | Union Oil Company Of California | Hydrocracking catalyst |
| US4517073A (en) * | 1982-08-09 | 1985-05-14 | Union Oil Company Of California | Hydrocracking process and catalyst therefor |
| US4576711A (en) * | 1979-10-15 | 1986-03-18 | Union Oil Company Of California | Hydrocracking process and catalyst therefor |
| US4401556A (en) * | 1979-11-13 | 1983-08-30 | Union Carbide Corporation | Midbarrel hydrocracking |
| JPS595011B2 (ja) * | 1979-11-27 | 1984-02-02 | 千代田化工建設株式会社 | 重質炭化水素油の水素化処理用触媒ならびにその製法 |
| US4301037A (en) * | 1980-04-01 | 1981-11-17 | W. R. Grace & Co. | Extruded alumina catalyst support having controlled distribution of pore sizes |
| US4435278A (en) * | 1980-06-09 | 1984-03-06 | Chezon Research Co. | Hydroprocessing with a catalyst having bimodal pore distribution |
| US4456701A (en) * | 1980-06-09 | 1984-06-26 | Chevron Research Company | Hydroprocessing catalyst having bimodal pore distribution and process for preparing the catalyst |
| JPS57204231A (en) * | 1981-06-11 | 1982-12-14 | Res Assoc Residual Oil Process<Rarop> | Catalyst for hydrocracking heavy oil |
| US4549957A (en) * | 1981-06-17 | 1985-10-29 | Amoco Corporation | Hydrotreating catalyst and process |
| US4454026A (en) * | 1981-06-17 | 1984-06-12 | Standard Oil Company (Indiana) | Hydrotreating catalyst and process |
| US4435275A (en) * | 1982-05-05 | 1984-03-06 | Mobil Oil Corporation | Hydrocracking process for aromatics production |
| US4563434A (en) * | 1982-08-09 | 1986-01-07 | Union Oil Company Of California | Hydrocracking catalyst |
| US4483942A (en) * | 1982-10-15 | 1984-11-20 | Nippon Oil Co., Ltd. | Process of preparing hydrogenation catalysts |
| US4572778A (en) * | 1984-01-19 | 1986-02-25 | Union Oil Company Of California | Hydroprocessing with a large pore catalyst |
| US4844792A (en) * | 1984-08-07 | 1989-07-04 | Union Oil Company Of California | Hydroprocessing with a specific pore sized catalyst containing non-hydrolyzable halogen |
| CN85100218B (zh) * | 1985-04-01 | 1987-03-11 | 中国石油化工总公司石油化工科学研究院 | 低碳烷氧基铝水解制备氧化铝方法 |
| FR2581896B1 (fr) * | 1985-05-14 | 1987-07-24 | Inst Francais Du Petrole | Catalyseur d'hydroraffinage d'huile ou d'hydrocraquage doux de charges petrolieres lourdes pour produire des distillats moyens |
| CN85104438B (zh) * | 1985-06-13 | 1986-08-06 | 中国石油化工总公司石油化工科学研究院 | 一种馏分油加氢精制催化剂 |
| US4891127A (en) * | 1985-12-31 | 1990-01-02 | Exxon Research And Engineering Company | Preparation and use of catalysts comprising a mixture of tungsten oxide and silica supported on a boehmite-like surface |
| JPS62199687A (ja) * | 1986-04-28 | 1987-09-03 | ユニオン・オイル・コンパニ−・オブ・カリフオルニア | 細孔の大きい触媒を用いる水素化法 |
| US4908344A (en) * | 1986-05-02 | 1990-03-13 | W. R. Grace & Co.-Conn. | Hydroprocessing catalyst and support having bidisperse pore structure |
| US4791090A (en) * | 1986-05-02 | 1988-12-13 | W. R. Grace & Co.-Conn. | Hydroprocessing catalyst and support having bidisperse pore structure |
| US4859312A (en) * | 1987-01-12 | 1989-08-22 | Chevron Research Company | Process for making middle distillates using a silicoaluminophosphate molecular sieve |
| US4894142A (en) * | 1987-03-24 | 1990-01-16 | Uop | Hydrocracking process employing low acidity Y zeolite |
| US4816538A (en) * | 1987-07-16 | 1989-03-28 | Union Oil Company Of California | Nickel-containing hydrocracking catalyst |
| US4957895A (en) * | 1988-05-23 | 1990-09-18 | The Harshaw Chemical Company | Hydrotreating catalyst and process |
| US4976848A (en) * | 1988-10-04 | 1990-12-11 | Chevron Research Company | Hydrodemetalation and hydrodesulfurization using a catalyst of specified macroporosity |
| US5089463A (en) * | 1988-10-04 | 1992-02-18 | Chevron Research And Technology Company | Hydrodemetalation and hydrodesulfurization catalyst of specified macroporosity |
| US5266300A (en) * | 1989-08-02 | 1993-11-30 | Texaco Inc. | Method of making porous alumina |
| JP2908959B2 (ja) * | 1993-04-07 | 1999-06-23 | 出光興産株式会社 | 新規触媒組成物 |
| US5378671A (en) * | 1993-06-03 | 1995-01-03 | Mobil Oil Corp. | Method for preparing catalysts comprising zeolites |
-
1997
- 1997-06-27 JP JP50370098A patent/JP2001503451A/ja active Pending
- 1997-06-27 EP EP97928101A patent/EP0947575B1/en not_active Expired - Lifetime
- 1997-06-27 WO PCT/CN1997/000064 patent/WO1998000384A1/zh not_active Ceased
- 1997-06-27 HR HR970357A patent/HRP970357B1/xx not_active IP Right Cessation
- 1997-06-27 AU AU32527/97A patent/AU3252797A/en not_active Abandoned
- 1997-06-30 ID IDP972258A patent/ID17947A/id unknown
- 1997-06-30 US US08/884,813 patent/US5954944A/en not_active Expired - Lifetime
-
1998
- 1998-12-23 NO NO19986095A patent/NO316647B1/no not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| US5954944A (en) | 1999-09-21 |
| EP0947575A4 (en) | 2000-03-22 |
| ID17947A (id) | 1998-02-12 |
| NO986095L (no) | 1999-02-26 |
| AU3252797A (en) | 1998-01-21 |
| EP0947575A1 (en) | 1999-10-06 |
| EP0947575B1 (en) | 2001-04-11 |
| JP2001503451A (ja) | 2001-03-13 |
| HRP970357B1 (en) | 2001-12-31 |
| NO986095D0 (no) | 1998-12-23 |
| WO1998000384A1 (fr) | 1998-01-08 |
| HRP970357A2 (en) | 1998-04-30 |
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Legal Events
| Date | Code | Title | Description |
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| MK1K | Patent expired |