CA2862039C - Procede d'hydrotraitement d'une huile hydrocarbonee - Google Patents
Procede d'hydrotraitement d'une huile hydrocarbonee Download PDFInfo
- Publication number
- CA2862039C CA2862039C CA2862039A CA2862039A CA2862039C CA 2862039 C CA2862039 C CA 2862039C CA 2862039 A CA2862039 A CA 2862039A CA 2862039 A CA2862039 A CA 2862039A CA 2862039 C CA2862039 C CA 2862039C
- Authority
- CA
- Canada
- Prior art keywords
- hydrogen
- containing gas
- stream
- reactor
- hydrocarbon oil
- 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.)
- Active
Links
- 229930195733 hydrocarbon Natural products 0.000 title claims abstract description 92
- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 92
- 239000004215 Carbon black (E152) Substances 0.000 title claims abstract description 89
- 238000000034 method Methods 0.000 title claims abstract description 78
- 230000008569 process Effects 0.000 title claims abstract description 76
- 239000007789 gas Substances 0.000 claims abstract description 182
- 239000001257 hydrogen Substances 0.000 claims abstract description 152
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 152
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 150
- 239000003054 catalyst Substances 0.000 claims abstract description 54
- 238000010438 heat treatment Methods 0.000 claims abstract description 19
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 9
- 229910052751 metal Inorganic materials 0.000 claims description 16
- 239000002184 metal Substances 0.000 claims description 16
- 239000007788 liquid Substances 0.000 claims description 10
- 150000002739 metals Chemical class 0.000 claims description 10
- 230000000737 periodic effect Effects 0.000 claims description 7
- 239000007787 solid Substances 0.000 claims description 7
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims description 6
- 229910000510 noble metal Inorganic materials 0.000 claims description 5
- 238000004140 cleaning Methods 0.000 claims description 4
- 238000009835 boiling Methods 0.000 claims description 2
- 239000003921 oil Substances 0.000 description 78
- 150000002431 hydrogen Chemical class 0.000 description 17
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 12
- 150000001412 amines Chemical class 0.000 description 11
- 239000010457 zeolite Substances 0.000 description 10
- -1 i.e. Chemical class 0.000 description 9
- 238000000926 separation method Methods 0.000 description 7
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 239000005864 Sulphur Substances 0.000 description 6
- 229910021536 Zeolite Inorganic materials 0.000 description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 5
- 230000008901 benefit Effects 0.000 description 5
- 150000001875 compounds Chemical class 0.000 description 5
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 4
- 125000004432 carbon atom Chemical group C* 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000000356 contaminant Substances 0.000 description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- 125000000217 alkyl group Chemical group 0.000 description 3
- 239000011230 binding agent Substances 0.000 description 3
- 125000002768 hydroxyalkyl group Chemical group 0.000 description 3
- 239000010687 lubricating oil Substances 0.000 description 3
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 2
- GLUUGHFHXGJENI-UHFFFAOYSA-N Piperazine Chemical compound C1CNCCN1 GLUUGHFHXGJENI-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 238000004517 catalytic hydrocracking Methods 0.000 description 2
- 229910017052 cobalt Inorganic materials 0.000 description 2
- 239000010941 cobalt Substances 0.000 description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- 229940083124 ganglion-blocking antiadrenergic secondary and tertiary amines Drugs 0.000 description 2
- 239000007792 gaseous phase Substances 0.000 description 2
- YBMRDBCBODYGJE-UHFFFAOYSA-N germanium dioxide Chemical compound O=[Ge]=O YBMRDBCBODYGJE-UHFFFAOYSA-N 0.000 description 2
- 238000005984 hydrogenation reaction Methods 0.000 description 2
- 230000010354 integration Effects 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910052750 molybdenum Inorganic materials 0.000 description 2
- 239000011733 molybdenum Substances 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 229910052763 palladium Inorganic materials 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 2
- 229910052721 tungsten Inorganic materials 0.000 description 2
- 239000010937 tungsten Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- GGYVTHJIUNGKFZ-UHFFFAOYSA-N 1-methylpiperidin-2-one Chemical compound CN1CCCCC1=O GGYVTHJIUNGKFZ-UHFFFAOYSA-N 0.000 description 1
- AVFZOVWCLRSYKC-UHFFFAOYSA-N 1-methylpyrrolidine Chemical compound CN1CCCC1 AVFZOVWCLRSYKC-UHFFFAOYSA-N 0.000 description 1
- GIAFURWZWWWBQT-UHFFFAOYSA-N 2-(2-aminoethoxy)ethanol Chemical compound NCCOCCO GIAFURWZWWWBQT-UHFFFAOYSA-N 0.000 description 1
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 1
- BFSVOASYOCHEOV-UHFFFAOYSA-N 2-diethylaminoethanol Chemical compound CCN(CC)CCO BFSVOASYOCHEOV-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- KWYHDKDOAIKMQN-UHFFFAOYSA-N N,N,N',N'-tetramethylethylenediamine Chemical compound CN(C)CCN(C)C KWYHDKDOAIKMQN-UHFFFAOYSA-N 0.000 description 1
- AHVYPIQETPWLSZ-UHFFFAOYSA-N N-methyl-pyrrolidine Natural products CN1CC=CC1 AHVYPIQETPWLSZ-UHFFFAOYSA-N 0.000 description 1
- OPKOKAMJFNKNAS-UHFFFAOYSA-N N-methylethanolamine Chemical compound CNCCO OPKOKAMJFNKNAS-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 1
- IJCVBMSXIPFVLH-UHFFFAOYSA-N [C].S=O Chemical compound [C].S=O IJCVBMSXIPFVLH-UHFFFAOYSA-N 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 150000007933 aliphatic carboxylic acids Chemical class 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- IYYZUPMFVPLQIF-ALWQSETLSA-N dibenzothiophene Chemical class C1=CC=CC=2[34S]C3=C(C=21)C=CC=C3 IYYZUPMFVPLQIF-ALWQSETLSA-N 0.000 description 1
- ZBCBWPMODOFKDW-UHFFFAOYSA-N diethanolamine Chemical compound OCCNCCO ZBCBWPMODOFKDW-UHFFFAOYSA-N 0.000 description 1
- LVTYICIALWPMFW-UHFFFAOYSA-N diisopropanolamine Chemical compound CC(O)CNCC(C)O LVTYICIALWPMFW-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 238000011066 ex-situ storage Methods 0.000 description 1
- 239000012013 faujasite Substances 0.000 description 1
- 229910001657 ferrierite group Inorganic materials 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 238000005342 ion exchange Methods 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
- 239000003350 kerosene Substances 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- CRVGTESFCCXCTH-UHFFFAOYSA-N methyl diethanolamine Chemical compound OCCN(C)CCO CRVGTESFCCXCTH-UHFFFAOYSA-N 0.000 description 1
- 229910052680 mordenite Inorganic materials 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 150000003141 primary amines Chemical class 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000005201 scrubbing Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000000629 steam reforming Methods 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- YTWOHSWDLJUCRK-UHFFFAOYSA-N thiolane 1,1-dioxide Chemical compound O=S1(=O)CCCC1.O=S1(=O)CCCC1 YTWOHSWDLJUCRK-UHFFFAOYSA-N 0.000 description 1
- 229930195735 unsaturated hydrocarbon Natural products 0.000 description 1
- 229910052727 yttrium Inorganic materials 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
- C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
- C10G65/043—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps at least one step being a change in the structural skeleton
-
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4031—Start up or shut down operations
-
- 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
-
- 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)
- Catalysts (AREA)
Abstract
L'invention concerne l'hydrotraitement d'une huile hydrocarbonée dans un procédé employant au moins une première et une seconde cuve de réacteur, ledit procédé comprenant : (i) la préparation d'un premier courant de gaz contenant de l'hydrogène ; (ii) l'hydrotraitement de l'huile hydrocarbonée dans le premier réacteur avec un premier catalyseur d'hydrotraitement en présence du premier courant de gaz contenant de l'hydrogène tel que préparé à l'étape (i) pour obtenir un premier effluent ; (iii) la séparation du premier effluent tel qu'obtenu à l'étape (ii) en une huile hydrocarbonée hydrotraitée et un gaz contenant de l'hydrogène usagé en utilisant une colonne d'extraction employant un gaz contenant de l'hydrogène en tant que gaz d'extraction ; (iv) la préparation d'un second courant de gaz contenant de l'hydrogène qui est chauffé dans une section d'un dispositif de chauffage qui est agencé en amont du premier réacteur pour obtenir un courant de gaz contenant de l'hydrogène chauffé ; et (v) la mise en contact dans le second réacteur d'au moins une partie du courant de gaz contenant de l'hydrogène chauffé tel qu'obtenu à l'étape (iv), éventuellement en présence d'au moins une partie de l'huile hydrocarbonée hydrotraitée telle qu'obtenue à l'étape (iii), avec un second catalyseur d'hydrotraitement pour obtenir un courant de gaz contenant de l'hydrogène usagé et un second effluent qui comprend une huile hydrocarbonée hydrotraitée supplémentaire lorsque l'huile hydrocarbonée hydrotraitée telle qu'obtenue à l'étape (iii) est également présente.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP11195994 | 2011-12-29 | ||
| EP11195994.6 | 2011-12-29 | ||
| PCT/EP2012/076966 WO2013098336A1 (fr) | 2011-12-29 | 2012-12-27 | Procédé d'hydrotraitement d'une huile hydrocarbonée |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2862039A1 CA2862039A1 (fr) | 2013-07-04 |
| CA2862039C true CA2862039C (fr) | 2021-02-02 |
Family
ID=47470014
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA2862039A Active CA2862039C (fr) | 2011-12-29 | 2012-12-27 | Procede d'hydrotraitement d'une huile hydrocarbonee |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US20150175909A1 (fr) |
| EP (1) | EP2798044B1 (fr) |
| KR (1) | KR102041762B1 (fr) |
| CN (1) | CN104114678B (fr) |
| CA (1) | CA2862039C (fr) |
| RU (1) | RU2630219C2 (fr) |
| WO (1) | WO2013098336A1 (fr) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108884396A (zh) * | 2016-02-29 | 2018-11-23 | 沙特基础工业全球技术公司 | 使用芳烃饱和生产烯烃的方法 |
Family Cites Families (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2337358A (en) * | 1939-10-20 | 1943-12-21 | Albert C Travis | Treatment of hydrocarbons |
| US3928178A (en) * | 1974-06-12 | 1975-12-23 | Standard Oil Co | Method of controlling catalyst deposits in hydrodesulfurization |
| US4913797A (en) * | 1985-11-21 | 1990-04-03 | Mobil Oil Corporation | Catalyst hydrotreating and dewaxing process |
| US4994170A (en) * | 1988-12-08 | 1991-02-19 | Coastal Eagle Point Oil Company | Multi-stage wax hydrocrackinig |
| JPH06299168A (ja) | 1993-02-15 | 1994-10-25 | Shell Internatl Res Maatschappij Bv | 水素化処理法 |
| DE4305176A1 (de) | 1993-02-19 | 1994-08-25 | Winkhaus Fa August | Schlüsselprofile und daraus hergestellte Schlüsselgruppen |
| US5958218A (en) * | 1996-01-22 | 1999-09-28 | The M. W. Kellogg Company | Two-stage hydroprocessing reaction scheme with series recycle gas flow |
| US5976354A (en) * | 1997-08-19 | 1999-11-02 | Shell Oil Company | Integrated lube oil hydrorefining process |
| US6635170B2 (en) * | 2000-12-14 | 2003-10-21 | Exxonmobil Research And Engineering Company | Hydroprocessing process with integrated interstage stripping |
| JP3860973B2 (ja) * | 2001-02-06 | 2006-12-20 | 新日本石油精製株式会社 | 水素化処理プラントの冷却方法および冷却装置 |
| EP1451268A1 (fr) * | 2001-11-22 | 2004-09-01 | Institut Francais Du Petrole | Procede d'hydrotraitement d'une charge hydrocarbonee en deux etapes comprenant un fractionnement intermediaire par stripage avec rectification |
| US6797154B2 (en) * | 2001-12-17 | 2004-09-28 | Chevron U.S.A. Inc. | Hydrocracking process for the production of high quality distillates from heavy gas oils |
| US20040159582A1 (en) * | 2003-02-18 | 2004-08-19 | Simmons Christopher A. | Process for producing premium fischer-tropsch diesel and lube base oils |
| US7282138B2 (en) * | 2003-11-05 | 2007-10-16 | Exxonmobil Research And Engineering Company | Multistage removal of heteroatoms and wax from distillate fuel |
| WO2009073436A2 (fr) * | 2007-11-28 | 2009-06-11 | Saudi Arabian Oil Company | Processus d'hydrotraitement catalytique des pétroles bruts sulfureux |
| CN102482594B (zh) * | 2009-07-15 | 2015-08-12 | 国际壳牌研究有限公司 | 加氢处理烃油的方法 |
| CN101831317A (zh) * | 2010-05-08 | 2010-09-15 | 何巨堂 | 一种高芳高氮烃的氢化方法 |
-
2012
- 2012-12-27 CA CA2862039A patent/CA2862039C/fr active Active
- 2012-12-27 RU RU2014131225A patent/RU2630219C2/ru active
- 2012-12-27 KR KR1020147020807A patent/KR102041762B1/ko active Active
- 2012-12-27 EP EP12808840.8A patent/EP2798044B1/fr active Active
- 2012-12-27 CN CN201280069030.7A patent/CN104114678B/zh active Active
- 2012-12-27 US US14/369,432 patent/US20150175909A1/en not_active Abandoned
- 2012-12-27 WO PCT/EP2012/076966 patent/WO2013098336A1/fr not_active Ceased
Also Published As
| Publication number | Publication date |
|---|---|
| CA2862039A1 (fr) | 2013-07-04 |
| CN104114678A (zh) | 2014-10-22 |
| CN104114678B (zh) | 2017-11-24 |
| KR102041762B1 (ko) | 2019-11-07 |
| US20150175909A1 (en) | 2015-06-25 |
| RU2014131225A (ru) | 2016-02-20 |
| EP2798044A1 (fr) | 2014-11-05 |
| KR20140119046A (ko) | 2014-10-08 |
| RU2630219C2 (ru) | 2017-09-06 |
| WO2013098336A1 (fr) | 2013-07-04 |
| EP2798044B1 (fr) | 2020-01-22 |
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