RU2538210C2 - Улучшенный способ селективного уменьшения содержания бензола и легких ненасыщенных соединений в различных углеводородных фракциях - Google Patents
Улучшенный способ селективного уменьшения содержания бензола и легких ненасыщенных соединений в различных углеводородных фракциях Download PDFInfo
- Publication number
- RU2538210C2 RU2538210C2 RU2010130421/04A RU2010130421A RU2538210C2 RU 2538210 C2 RU2538210 C2 RU 2538210C2 RU 2010130421/04 A RU2010130421/04 A RU 2010130421/04A RU 2010130421 A RU2010130421 A RU 2010130421A RU 2538210 C2 RU2538210 C2 RU 2538210C2
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- Prior art keywords
- zone
- hydrogenation
- distillation
- benzene
- reaction zone
- Prior art date
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- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 title claims abstract description 273
- 238000000034 method Methods 0.000 title claims abstract description 94
- 150000001875 compounds Chemical class 0.000 title claims abstract description 45
- 229930195733 hydrocarbon Natural products 0.000 title claims abstract description 24
- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 21
- 239000004215 Carbon black (E152) Substances 0.000 title description 9
- 238000005984 hydrogenation reaction Methods 0.000 claims abstract description 166
- 238000004821 distillation Methods 0.000 claims abstract description 134
- 239000001257 hydrogen Substances 0.000 claims abstract description 54
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 54
- 239000003054 catalyst Substances 0.000 claims abstract description 45
- 230000003197 catalytic effect Effects 0.000 claims abstract description 42
- 238000006243 chemical reaction Methods 0.000 claims abstract description 39
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 36
- 239000007789 gas Substances 0.000 claims abstract description 23
- -1 benzene Chemical class 0.000 claims abstract description 6
- 238000000605 extraction Methods 0.000 claims abstract description 5
- 239000007788 liquid Substances 0.000 claims description 33
- 238000006317 isomerization reaction Methods 0.000 claims description 28
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 27
- 125000004432 carbon atom Chemical group C* 0.000 claims description 27
- 150000001336 alkenes Chemical class 0.000 claims description 25
- 238000005336 cracking Methods 0.000 claims description 21
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 20
- 150000002431 hydrogen Chemical class 0.000 claims description 18
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 18
- 239000012808 vapor phase Substances 0.000 claims description 16
- 238000004939 coking Methods 0.000 claims description 15
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 14
- 239000002994 raw material Substances 0.000 claims description 12
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 10
- 229910052757 nitrogen Inorganic materials 0.000 claims description 10
- 239000011593 sulfur Substances 0.000 claims description 10
- 229910052717 sulfur Inorganic materials 0.000 claims description 10
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 9
- 238000004523 catalytic cracking Methods 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 229910052697 platinum Inorganic materials 0.000 claims description 9
- 238000004517 catalytic hydrocracking Methods 0.000 claims description 8
- 229910052751 metal Inorganic materials 0.000 claims description 8
- 239000002184 metal Substances 0.000 claims description 8
- 229910052759 nickel Inorganic materials 0.000 claims description 7
- 238000000926 separation method Methods 0.000 claims description 7
- 239000007791 liquid phase Substances 0.000 claims description 6
- 238000010992 reflux Methods 0.000 claims description 5
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 4
- 239000000460 chlorine Substances 0.000 claims description 4
- 229910052801 chlorine Inorganic materials 0.000 claims description 4
- 238000009434 installation Methods 0.000 claims description 4
- 239000010457 zeolite Substances 0.000 claims description 4
- 229910021536 Zeolite Inorganic materials 0.000 claims description 3
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims description 3
- 229910052799 carbon Inorganic materials 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
- 229910052726 zirconium Inorganic materials 0.000 claims description 3
- 230000001174 ascending effect Effects 0.000 claims description 2
- 239000000126 substance Substances 0.000 abstract description 2
- 230000000694 effects Effects 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 19
- 238000005070 sampling Methods 0.000 description 14
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 9
- 238000009835 boiling Methods 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 9
- 238000004231 fluid catalytic cracking Methods 0.000 description 8
- GDOPTJXRTPNYNR-UHFFFAOYSA-N methylcyclopentane Chemical compound CC1CCCC1 GDOPTJXRTPNYNR-UHFFFAOYSA-N 0.000 description 8
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 8
- 238000002407 reforming Methods 0.000 description 8
- 239000000446 fuel Substances 0.000 description 6
- 150000001491 aromatic compounds Chemical class 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 4
- 239000005977 Ethylene Substances 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 238000001833 catalytic reforming Methods 0.000 description 4
- 239000003153 chemical reaction reagent Substances 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 239000003377 acid catalyst Substances 0.000 description 3
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 3
- 239000000571 coke Substances 0.000 description 3
- 230000003111 delayed effect Effects 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 3
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 3
- 238000000197 pyrolysis Methods 0.000 description 3
- 238000007670 refining Methods 0.000 description 3
- MHNNAWXXUZQSNM-UHFFFAOYSA-N 2-methylbut-1-ene Chemical compound CCC(C)=C MHNNAWXXUZQSNM-UHFFFAOYSA-N 0.000 description 2
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- 230000000711 cancerogenic effect Effects 0.000 description 2
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 210000000540 fraction c Anatomy 0.000 description 2
- 230000009931 harmful effect Effects 0.000 description 2
- QWTDNUCVQCZILF-UHFFFAOYSA-N isopentane Chemical compound CCC(C)C QWTDNUCVQCZILF-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000012188 paraffin wax Substances 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 206010067484 Adverse reaction Diseases 0.000 description 1
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 description 1
- 206010038687 Respiratory distress Diseases 0.000 description 1
- 230000006838 adverse reaction Effects 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 229910000287 alkaline earth metal oxide Inorganic materials 0.000 description 1
- 230000029936 alkylation Effects 0.000 description 1
- 238000005804 alkylation reaction Methods 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000000895 extractive distillation Methods 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 125000005842 heteroatom Chemical group 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 238000006552 photochemical reaction Methods 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 229910001404 rare earth metal oxide Inorganic materials 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 150000003738 xylenes Chemical class 0.000 description 1
Images
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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
-
- 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
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/305—Octane number, e.g. motor octane number [MON], research octane number [RON]
-
- 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
- C10G2300/4087—Catalytic distillation
-
- 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
- C10G2400/02—Gasoline
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 (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12/765,962 US8808533B2 (en) | 2010-04-23 | 2010-04-23 | Process for selective reduction of the contents of benzene and light unsaturated compounds of different hydrocarbon fractions |
| US12/765,962 | 2010-04-23 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| RU2010130421A RU2010130421A (ru) | 2012-01-27 |
| RU2538210C2 true RU2538210C2 (ru) | 2015-01-10 |
Family
ID=44814888
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| RU2010130421/04A RU2538210C2 (ru) | 2010-04-23 | 2010-07-20 | Улучшенный способ селективного уменьшения содержания бензола и легких ненасыщенных соединений в различных углеводородных фракциях |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US8808533B2 (enExample) |
| JP (1) | JP5964552B2 (enExample) |
| CA (1) | CA2738541C (enExample) |
| MX (1) | MX2011003916A (enExample) |
| RU (1) | RU2538210C2 (enExample) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103540343B (zh) * | 2012-07-12 | 2016-01-13 | 中国石油化工股份有限公司 | 提高汽油辛烷值的方法 |
| CN104629797B (zh) * | 2015-02-05 | 2016-06-29 | 中石化上海工程有限公司 | 裂解汽油加氢装置二段反应器出口物料余热回收的方法 |
| AU2017216346B2 (en) | 2016-02-05 | 2021-03-11 | Anellotech, Inc. | Chemicals and fuel blendstocks by a catalytic fast pyrolysis process |
| US10710942B2 (en) | 2016-05-23 | 2020-07-14 | Sabic Global Technologies B.V. | Method of co-processing fluidized catalytic cracking naphtha and pyrolysis gasoline |
| CN107779225B (zh) * | 2016-08-31 | 2019-07-12 | 中国石油化工股份有限公司 | 一种加氢转化系统及方法 |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2091441C1 (ru) * | 1992-01-15 | 1997-09-27 | Энститю Франсэ Дю Петроль | Способ снижения содержания бензола в бензиновых фракциях |
| US5817227A (en) * | 1995-12-27 | 1998-10-06 | Institut Francais Du Petrole | Process for the selective reduction to the content of benzene and light unsaturated compounds in a hydrocarbon cut |
| RU2130962C1 (ru) * | 1993-12-29 | 1999-05-27 | Энститю Франсэ Дю Петроль | Способ снижения содержания бензола в бензиновых фракциях |
| US6048450A (en) * | 1995-12-27 | 2000-04-11 | Institut Francais Du Petrole | Process for the selective reduction to the content of benzene and light unsaturated compounds in a hydrocarbon cut |
| US20080286172A1 (en) * | 2007-05-18 | 2008-11-20 | David J Shecterle | Isomerization of Benzene-Containing Feedstocks |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3759819A (en) * | 1971-06-30 | 1973-09-18 | Union Oil Co | Integral hydrogenation isomerization process |
| US5770047A (en) * | 1994-05-23 | 1998-06-23 | Intevep, S.A. | Process for producing reformulated gasoline by reducing sulfur, nitrogen and olefin |
| FR2743079B1 (fr) * | 1995-12-27 | 1998-02-06 | Inst Francais Du Petrole | Procede et dispositif d'hydrogenation selective par distillation catalytique comportant une zone reactionnelle a co-courant ascendant liquide-gaz |
| US5830345A (en) * | 1996-02-28 | 1998-11-03 | Chinese Petroleum Corporation | Process of producing a debenzenated and isomerized gasoline blending stock by using a dual functional catalyst |
| US5856602A (en) * | 1996-09-09 | 1999-01-05 | Catalytic Distillation Technologies | Selective hydrogenation of aromatics contained in hydrocarbon streams |
| FR2777013B1 (fr) * | 1998-04-06 | 2000-05-05 | Inst Francais Du Petrole | Procede de conversion d'hydrocarbures par traitement dans une zone de distillation comprenant un reflux circulant, associee a une zone reactionnelle et son utilisation en hydrogenation du benzene |
| FR2818637B1 (fr) * | 2000-12-21 | 2003-02-07 | Inst Francais Du Petrole | Procede de traitement d'hydrocarbures c4 comportant du butadiene et des composes acetylenique comprenant des etapes de distillation et d'hydrogenation selective |
| CA2705036C (en) * | 2007-11-09 | 2017-07-04 | Ranfeng Ding | A system and a process for recombining catalytic hydrocarbon to produce high quality gasoline |
| US9315741B2 (en) * | 2008-09-08 | 2016-04-19 | Catalytic Distillation Technologies | Process for ultra low benzene reformate using catalytic distillation |
-
2010
- 2010-04-23 US US12/765,962 patent/US8808533B2/en active Active
- 2010-07-20 RU RU2010130421/04A patent/RU2538210C2/ru active
-
2011
- 2011-04-12 MX MX2011003916A patent/MX2011003916A/es active IP Right Grant
- 2011-04-19 CA CA2738541A patent/CA2738541C/fr active Active
- 2011-04-22 JP JP2011095563A patent/JP5964552B2/ja active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2091441C1 (ru) * | 1992-01-15 | 1997-09-27 | Энститю Франсэ Дю Петроль | Способ снижения содержания бензола в бензиновых фракциях |
| RU2130962C1 (ru) * | 1993-12-29 | 1999-05-27 | Энститю Франсэ Дю Петроль | Способ снижения содержания бензола в бензиновых фракциях |
| US5817227A (en) * | 1995-12-27 | 1998-10-06 | Institut Francais Du Petrole | Process for the selective reduction to the content of benzene and light unsaturated compounds in a hydrocarbon cut |
| US6048450A (en) * | 1995-12-27 | 2000-04-11 | Institut Francais Du Petrole | Process for the selective reduction to the content of benzene and light unsaturated compounds in a hydrocarbon cut |
| US20080286172A1 (en) * | 2007-05-18 | 2008-11-20 | David J Shecterle | Isomerization of Benzene-Containing Feedstocks |
Also Published As
| Publication number | Publication date |
|---|---|
| MX2011003916A (es) | 2011-10-27 |
| JP2011231322A (ja) | 2011-11-17 |
| CA2738541A1 (fr) | 2011-10-23 |
| CA2738541C (fr) | 2018-07-31 |
| JP5964552B2 (ja) | 2016-08-03 |
| US8808533B2 (en) | 2014-08-19 |
| US20110259792A1 (en) | 2011-10-27 |
| RU2010130421A (ru) | 2012-01-27 |
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