AU3285901A - Single stage multi-zone hydroisomerization process - Google Patents
Single stage multi-zone hydroisomerization process Download PDFInfo
- Publication number
- AU3285901A AU3285901A AU32859/01A AU3285901A AU3285901A AU 3285901 A AU3285901 A AU 3285901A AU 32859/01 A AU32859/01 A AU 32859/01A AU 3285901 A AU3285901 A AU 3285901A AU 3285901 A AU3285901 A AU 3285901A
- Authority
- AU
- Australia
- Prior art keywords
- zone
- hydrogen
- fraction
- hydroisomerization
- process according
- 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.)
- Abandoned
Links
- 238000000034 method Methods 0.000 title claims description 58
- 229930195733 hydrocarbon Natural products 0.000 claims description 168
- 150000002430 hydrocarbons Chemical class 0.000 claims description 165
- 239000004215 Carbon black (E152) Substances 0.000 claims description 71
- 238000009835 boiling Methods 0.000 claims description 63
- 239000003054 catalyst Substances 0.000 claims description 61
- 229910052739 hydrogen Inorganic materials 0.000 claims description 57
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 56
- 239000001257 hydrogen Substances 0.000 claims description 56
- 239000007789 gas Substances 0.000 claims description 50
- 238000003786 synthesis reaction Methods 0.000 claims description 48
- 230000015572 biosynthetic process Effects 0.000 claims description 42
- 239000000446 fuel Substances 0.000 claims description 31
- 238000006243 chemical reaction Methods 0.000 claims description 27
- 239000000203 mixture Substances 0.000 claims description 14
- 102100028701 General vesicular transport factor p115 Human genes 0.000 claims description 7
- 101000767151 Homo sapiens General vesicular transport factor p115 Proteins 0.000 claims description 7
- 239000003350 kerosene Substances 0.000 claims description 4
- 239000000047 product Substances 0.000 description 39
- 239000002002 slurry Substances 0.000 description 29
- 239000007788 liquid Substances 0.000 description 27
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- 229910017052 cobalt Inorganic materials 0.000 description 11
- 239000010941 cobalt Substances 0.000 description 11
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 11
- 239000000377 silicon dioxide Substances 0.000 description 11
- 238000005336 cracking Methods 0.000 description 10
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 6
- 230000003197 catalytic effect Effects 0.000 description 6
- 238000000926 separation method Methods 0.000 description 6
- 239000000314 lubricant Substances 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 229910052750 molybdenum Inorganic materials 0.000 description 5
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 4
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 239000011733 molybdenum Substances 0.000 description 4
- 229910000510 noble metal Inorganic materials 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 230000009849 deactivation Effects 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 238000005194 fractionation Methods 0.000 description 3
- 238000007327 hydrogenolysis reaction Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 238000011144 upstream manufacturing Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- -1 C 4 hydrocarbons Chemical class 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 238000004517 catalytic hydrocracking Methods 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005984 hydrogenation reaction Methods 0.000 description 2
- 239000012263 liquid product Substances 0.000 description 2
- 229910017464 nitrogen compound Inorganic materials 0.000 description 2
- 150000002830 nitrogen compounds Chemical class 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 239000011959 amorphous silica alumina Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000010730 cutting oil Substances 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910000476 molybdenum oxide Inorganic materials 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- PQQKPALAQIIWST-UHFFFAOYSA-N oxomolybdenum Chemical class [Mo]=O PQQKPALAQIIWST-UHFFFAOYSA-N 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 229910052702 rhenium Inorganic materials 0.000 description 1
- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 description 1
- 239000010454 slate Substances 0.000 description 1
- 239000011949 solid catalyst Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 229910052721 tungsten 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
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US49743800A | 2000-02-03 | 2000-02-03 | |
| US09497438 | 2000-02-03 | ||
| PCT/US2001/001765 WO2001057160A1 (en) | 2000-02-03 | 2001-01-18 | Single stage multi-zone hydroisomerization process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AU3285901A true AU3285901A (en) | 2001-08-14 |
Family
ID=23976869
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU32859/01A Abandoned AU3285901A (en) | 2000-02-03 | 2001-01-18 | Single stage multi-zone hydroisomerization process |
Country Status (8)
| Country | Link |
|---|---|
| EP (1) | EP1254199A1 (es) |
| JP (1) | JP2003522252A (es) |
| AR (1) | AR027321A1 (es) |
| AU (1) | AU3285901A (es) |
| BR (1) | BR0108019A (es) |
| CA (1) | CA2399070A1 (es) |
| NO (1) | NO20023682L (es) |
| WO (1) | WO2001057160A1 (es) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7198710B2 (en) * | 2003-03-10 | 2007-04-03 | Chevron U.S.A. Inc. | Isomerization/dehazing process for base oils from Fischer-Tropsch wax |
| JP5137399B2 (ja) * | 2003-04-11 | 2013-02-06 | セイソル テクノロジー （プロプライエタリー） リミテッド | 低硫黄ディーゼル燃料及び航空機タービン燃料 |
| AU2005305799B2 (en) * | 2004-11-18 | 2009-07-09 | Shell Internationale Research Maatschappij B.V. | Process to prepare a gas oil |
| BRPI0517785A (pt) | 2004-11-18 | 2008-10-21 | Shell Int Research | processo para otimizar o rendimento de óleos de base a partir de uma alimentação derivada de fischer-tropsch |
| JP4791167B2 (ja) | 2005-12-09 | 2011-10-12 | Ｊｘ日鉱日石エネルギー株式会社 | 水素化精製方法 |
| KR101211376B1 (ko) * | 2010-09-30 | 2012-12-13 | 한국에너지기술연구원 | 복합 반응이 가능한 ｆ-ｔ 기포탑 반응기 |
| CN104673384B (zh) * | 2015-03-02 | 2016-09-14 | 武汉凯迪工程技术研究总院有限公司 | 一种低温费托全馏分油多产中间馏分油的加氢精制方法 |
| FR3084082B1 (fr) | 2018-07-18 | 2020-08-07 | Ifp Energies Now | Utilisation d'un catalyseur bifonctionnel a base de zeolithe izm-2 pour l'hydroisomerisation de charges paraffiniques legeres issues de la synthese fischer-tropsch |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4919786A (en) * | 1987-12-18 | 1990-04-24 | Exxon Research And Engineering Company | Process for the hydroisomerization of was to produce middle distillate products (OP-3403) |
| US5378348A (en) * | 1993-07-22 | 1995-01-03 | Exxon Research And Engineering Company | Distillate fuel production from Fischer-Tropsch wax |
| US5660714A (en) * | 1995-07-14 | 1997-08-26 | Exxon Research And Engineering Company | Hydroconversion process utilizing a supported Ni-Cu hydroconversion catalyst |
-
2001
- 2001-01-18 EP EP01904928A patent/EP1254199A1/en not_active Withdrawn
- 2001-01-18 CA CA002399070A patent/CA2399070A1/en not_active Abandoned
- 2001-01-18 AU AU32859/01A patent/AU3285901A/en not_active Abandoned
- 2001-01-18 BR BR0108019-9A patent/BR0108019A/pt not_active Application Discontinuation
- 2001-01-18 JP JP2001557980A patent/JP2003522252A/ja active Pending
- 2001-01-18 WO PCT/US2001/001765 patent/WO2001057160A1/en not_active Application Discontinuation
- 2001-01-29 AR ARP010100400A patent/AR027321A1/es unknown
-
2002
- 2002-08-02 NO NO20023682A patent/NO20023682L/no not_active Application Discontinuation
Also Published As
| Publication number | Publication date |
|---|---|
| CA2399070A1 (en) | 2001-08-09 |
| AR027321A1 (es) | 2003-03-19 |
| JP2003522252A (ja) | 2003-07-22 |
| NO20023682L (no) | 2002-09-25 |
| BR0108019A (pt) | 2002-10-29 |
| WO2001057160A1 (en) | 2001-08-09 |
| EP1254199A1 (en) | 2002-11-06 |
| NO20023682D0 (no) | 2002-08-02 |
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