JP2003327972A - 低芳香族化合物含有量の高品質ガソリンの製造方法。 - Google Patents
低芳香族化合物含有量の高品質ガソリンの製造方法。Info
- Publication number
- JP2003327972A JP2003327972A JP2003114687A JP2003114687A JP2003327972A JP 2003327972 A JP2003327972 A JP 2003327972A JP 2003114687 A JP2003114687 A JP 2003114687A JP 2003114687 A JP2003114687 A JP 2003114687A JP 2003327972 A JP2003327972 A JP 2003327972A
- Authority
- JP
- Japan
- Prior art keywords
- isomerization
- catalyst
- branched
- stage
- isomers
- 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.)
- Pending
Links
- 238000000034 method Methods 0.000 title claims abstract description 42
- 230000008569 process Effects 0.000 title claims abstract description 20
- 150000001491 aromatic compounds Chemical class 0.000 title claims abstract description 11
- 239000003054 catalyst Substances 0.000 claims abstract description 54
- 238000006317 isomerization reaction Methods 0.000 claims abstract description 46
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 28
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 25
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 22
- 239000012188 paraffin wax Substances 0.000 claims abstract description 15
- 229910000510 noble metal Inorganic materials 0.000 claims abstract description 4
- 150000001336 alkenes Chemical class 0.000 claims abstract 2
- 125000000753 cycloalkyl group Chemical group 0.000 claims abstract 2
- 239000011973 solid acid Substances 0.000 claims abstract 2
- 239000007788 liquid Substances 0.000 claims description 24
- 238000000926 separation method Methods 0.000 claims description 22
- 239000000203 mixture Substances 0.000 claims description 18
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims description 16
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 14
- 239000001257 hydrogen Substances 0.000 claims description 14
- 229910052739 hydrogen Inorganic materials 0.000 claims description 14
- 239000002808 molecular sieve Substances 0.000 claims description 12
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 12
- 239000002253 acid Substances 0.000 claims description 9
- 230000002378 acidificating effect Effects 0.000 claims description 7
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims description 6
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 4
- 239000011148 porous material Substances 0.000 claims description 4
- 239000002608 ionic liquid Substances 0.000 claims description 3
- QGLKJKCYBOYXKC-UHFFFAOYSA-N nonaoxidotritungsten Chemical group O=[W]1(=O)O[W](=O)(=O)O[W](=O)(=O)O1 QGLKJKCYBOYXKC-UHFFFAOYSA-N 0.000 claims description 3
- 229910052763 palladium Inorganic materials 0.000 claims description 3
- 229910052697 platinum Inorganic materials 0.000 claims description 3
- 239000010970 precious metal Substances 0.000 claims description 3
- 229910001930 tungsten oxide Inorganic materials 0.000 claims description 3
- 241000588731 Hafnia Species 0.000 claims description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 2
- CJNBYAVZURUTKZ-UHFFFAOYSA-N hafnium(IV) oxide Inorganic materials O=[Hf]=O CJNBYAVZURUTKZ-UHFFFAOYSA-N 0.000 claims description 2
- 150000003839 salts Chemical class 0.000 claims description 2
- 239000007787 solid Substances 0.000 claims description 2
- 239000003930 superacid Substances 0.000 claims description 2
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims description 2
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims description 2
- 229910052721 tungsten Inorganic materials 0.000 claims description 2
- 239000010937 tungsten Substances 0.000 claims description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 claims 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims 2
- 229910003480 inorganic solid Inorganic materials 0.000 claims 1
- 229910001507 metal halide Inorganic materials 0.000 claims 1
- 150000005309 metal halides Chemical class 0.000 claims 1
- 150000003242 quaternary ammonium salts Chemical class 0.000 claims 1
- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical compound O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 claims 1
- 229910001887 tin oxide Inorganic materials 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 7
- -1 12C hydrocarbon Chemical class 0.000 abstract description 5
- 230000002708 enhancing effect Effects 0.000 abstract 1
- 238000009738 saturating Methods 0.000 abstract 1
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical class CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 33
- 238000006243 chemical reaction Methods 0.000 description 31
- 238000005336 cracking Methods 0.000 description 21
- 239000003463 adsorbent Substances 0.000 description 10
- 239000011949 solid catalyst Substances 0.000 description 9
- 239000010457 zeolite Substances 0.000 description 9
- 229910021536 Zeolite Inorganic materials 0.000 description 7
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 7
- 239000012528 membrane Substances 0.000 description 5
- 230000004913 activation Effects 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 150000001924 cycloalkanes Chemical class 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000000543 intermediate Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910018287 SbF 5 Inorganic materials 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000007210 heterogeneous catalysis Methods 0.000 description 2
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 2
- UAEPNZWRGJTJPN-UHFFFAOYSA-N methylcyclohexane Chemical compound CC1CCCCC1 UAEPNZWRGJTJPN-UHFFFAOYSA-N 0.000 description 2
- 238000007142 ring opening reaction Methods 0.000 description 2
- 102200118166 rs16951438 Human genes 0.000 description 2
- SZYJELPVAFJOGJ-UHFFFAOYSA-N trimethylamine hydrochloride Chemical compound Cl.CN(C)C SZYJELPVAFJOGJ-UHFFFAOYSA-N 0.000 description 2
- WGECXQBGLLYSFP-UHFFFAOYSA-N (+-)-2,3-dimethyl-pentane Natural products CCC(C)C(C)C WGECXQBGLLYSFP-UHFFFAOYSA-N 0.000 description 1
- CXOWYJMDMMMMJO-UHFFFAOYSA-N 2,2,4-trimethyl-butane Natural products CCCC(C)(C)C CXOWYJMDMMMMJO-UHFFFAOYSA-N 0.000 description 1
- BZHMBWZPUJHVEE-UHFFFAOYSA-N 2,3-dimethylpentane Natural products CC(C)CC(C)C BZHMBWZPUJHVEE-UHFFFAOYSA-N 0.000 description 1
- KUFFULVDNCHOFZ-UHFFFAOYSA-N 2,4-xylenol Chemical compound CC1=CC=C(O)C(C)=C1 KUFFULVDNCHOFZ-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- 229910021591 Copper(I) chloride Inorganic materials 0.000 description 1
- AEXMKKGTQYQZCS-UHFFFAOYSA-N Dimethyl-diaethyl-methan Natural products CCC(C)(C)CC AEXMKKGTQYQZCS-UHFFFAOYSA-N 0.000 description 1
- 238000005727 Friedel-Crafts reaction Methods 0.000 description 1
- 239000002841 Lewis acid Substances 0.000 description 1
- 239000004820 Pressure-sensitive adhesive Substances 0.000 description 1
- 229910006404 SnO 2 Inorganic materials 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 150000001412 amines Chemical group 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 150000001721 carbon Chemical group 0.000 description 1
- 238000004523 catalytic cracking Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000001833 catalytic reforming Methods 0.000 description 1
- 238000005341 cation exchange Methods 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 239000007806 chemical reaction intermediate Substances 0.000 description 1
- 238000013375 chromatographic separation Methods 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- OXBLHERUFWYNTN-UHFFFAOYSA-M copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 150000001923 cyclic compounds Chemical class 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- QWBBPBRQALCEIZ-UHFFFAOYSA-N di-methylphenol Natural products CC1=CC=CC(O)=C1C QWBBPBRQALCEIZ-UHFFFAOYSA-N 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 229910001657 ferrierite group Inorganic materials 0.000 description 1
- 229910021480 group 4 element Inorganic materials 0.000 description 1
- 229910021476 group 6 element Inorganic materials 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 150000002500 ions Chemical group 0.000 description 1
- 239000001282 iso-butane Substances 0.000 description 1
- 150000007517 lewis acids Chemical class 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- GYNNXHKOJHMOHS-UHFFFAOYSA-N methyl-cycloheptane Natural products CC1CCCCCC1 GYNNXHKOJHMOHS-UHFFFAOYSA-N 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- UJVRJBAUJYZFIX-UHFFFAOYSA-N nitric acid;oxozirconium Chemical compound [Zr]=O.O[N+]([O-])=O.O[N+]([O-])=O UJVRJBAUJYZFIX-UHFFFAOYSA-N 0.000 description 1
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 description 1
- IYDGMDWEHDFVQI-UHFFFAOYSA-N phosphoric acid;trioxotungsten Chemical compound O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.OP(O)(O)=O IYDGMDWEHDFVQI-UHFFFAOYSA-N 0.000 description 1
- 238000000066 reactive distillation Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- CGFYHILWFSGVJS-UHFFFAOYSA-N silicic acid;trioxotungsten Chemical compound O[Si](O)(O)O.O=[W]1(=O)O[W](=O)(=O)O[W](=O)(=O)O1.O=[W]1(=O)O[W](=O)(=O)O[W](=O)(=O)O1.O=[W]1(=O)O[W](=O)(=O)O[W](=O)(=O)O1.O=[W]1(=O)O[W](=O)(=O)O[W](=O)(=O)O1 CGFYHILWFSGVJS-UHFFFAOYSA-N 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- ITMCEJHCFYSIIV-UHFFFAOYSA-N triflic acid Chemical compound OS(=O)(=O)C(F)(F)F ITMCEJHCFYSIIV-UHFFFAOYSA-N 0.000 description 1
- 229910001928 zirconium oxide 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
- C10G59/00—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha
- C10G59/02—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha 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
- 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)
- Catalysts (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DKPA200200576 | 2002-04-18 | ||
DK200200576 | 2002-04-18 |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2003327972A true JP2003327972A (ja) | 2003-11-19 |
JP2003327972A5 JP2003327972A5 (fr) | 2006-04-27 |
Family
ID=28685789
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2003114687A Pending JP2003327972A (ja) | 2002-04-18 | 2003-04-18 | 低芳香族化合物含有量の高品質ガソリンの製造方法。 |
Country Status (3)
Country | Link |
---|---|
US (1) | US20030196931A1 (fr) |
EP (1) | EP1357167A1 (fr) |
JP (1) | JP2003327972A (fr) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007217591A (ja) * | 2006-02-17 | 2007-08-30 | Japan Energy Corp | ガソリン基材の製造方法及びガソリン組成物 |
JP2007217589A (ja) * | 2006-02-17 | 2007-08-30 | Japan Energy Corp | ガソリン基材の製造方法及びガソリン組成物 |
JP2007217590A (ja) * | 2006-02-17 | 2007-08-30 | Japan Energy Corp | ガソリン基材の製造方法及びガソリン組成物 |
JP2010510351A (ja) * | 2006-11-20 | 2010-04-02 | ラマス テクノロジ インコーポレイテッド | 非還流型反応器ストリッパー |
JP2011241406A (ja) * | 2011-09-06 | 2011-12-01 | Jx Nippon Oil & Energy Corp | 環境対応型ガソリン組成物及びその製造方法 |
Families Citing this family (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7435865B2 (en) * | 2003-08-18 | 2008-10-14 | Vrije Universiteit Brussel | Method for separating hydrocarbons and use of a zeolite therefor |
CN100425674C (zh) * | 2003-10-31 | 2008-10-15 | 中国石油化工股份有限公司 | 一种提高汽油辛烷值的催化转化方法 |
MX2007011163A (es) * | 2005-03-11 | 2007-11-13 | Uop Llc | Membranas de tamiz de microporo de alto flujo y separadores que contienen tales membranas y procesos que usan dichos antecedentes de las membranas del invento. |
US7846322B2 (en) * | 2005-03-11 | 2010-12-07 | Uop Llc | Integrated refinery with enhanced olefin and reformate production |
US7638674B2 (en) * | 2007-09-07 | 2009-12-29 | Uop Llc | Processes for the isomerization of paraffins of 5 and 6 carbon atoms with methylcyclopentane recovery |
US7638675B2 (en) * | 2007-09-07 | 2009-12-29 | Uop Llc | Processes for the isomerization of normal butane to isobutane |
US7638676B2 (en) * | 2007-09-07 | 2009-12-29 | Uop Llc | Processes for the isomerization of feedstocks comprising paraffins of 5 to 7 carbon atoms |
US7812207B2 (en) * | 2007-09-07 | 2010-10-12 | Uop Llc | Membrane separation processes and systems for enhanced permeant recovery |
US9102577B2 (en) | 2013-06-28 | 2015-08-11 | Uop Llc | Catalytic disproportionation of paraffins using ionic liquids |
US9126881B2 (en) | 2013-06-28 | 2015-09-08 | Uop Llc | Catalytic isomerization of pentane using ionic liquids |
US9096481B2 (en) | 2013-06-28 | 2015-08-04 | Uop Llc | Catalytic disproportionation of pentane using ionic liquids |
US9096480B2 (en) | 2013-06-28 | 2015-08-04 | Uop Llc | Catalytic disproportionation of heptane using ionic liquids |
US9096482B2 (en) | 2013-06-28 | 2015-08-04 | Uop Llc | Catalytic reverse disproportionation of paraffins using ionic liquids |
US9096483B2 (en) | 2013-06-28 | 2015-08-04 | Uop Llc | Catalytic isomerization of hexanes using ionic liquids |
US9102578B2 (en) | 2013-06-28 | 2015-08-11 | Uop Llc | Catalytic isomerization of paraffins using ionic liquids |
US9096485B2 (en) | 2013-06-28 | 2015-08-04 | Uop Llc | Catalytic isomerization of heptane using ionic liquids |
US20150005554A1 (en) * | 2013-06-28 | 2015-01-01 | Uop Llc | Catalytic isomerization of butane using ionic liquids |
RU2621031C1 (ru) * | 2016-03-29 | 2017-05-31 | Рауф Раисович Юнусов | Установка для переработки стабильного газового конденсата и входящая в ее состав установка для получения высокооктанового бензина |
US10124294B2 (en) | 2016-06-23 | 2018-11-13 | Saudi Arabian Oil Company | On-board fuel adjustment by molecular separation |
CN109574851B (zh) * | 2018-11-27 | 2021-08-06 | 浙江工业大学上虞研究院有限公司 | 一种离子液体催化氯苯硝化制备2,4-二硝基氯苯的方法 |
CN111659462B (zh) * | 2020-06-30 | 2023-10-27 | 中化泉州石化有限公司 | 一种高活性异构降凝催化剂的制备方法 |
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GB567875A (en) * | 1940-12-23 | 1945-03-07 | Shell Dev | Process for the isomerization of hydrocarbons |
US3839489A (en) * | 1972-02-28 | 1974-10-01 | Phillips Petroleum Co | Isomerization with asf5 and/or sbf5 and with trifluoromethanesulfonic acid or hf and high h2 partial pressure |
IT1129809B (it) * | 1979-03-26 | 1986-06-11 | Ugine Kuhlmann | Composizione catalitica per la conversione di idrocarburi e procedimento per la disidratazione di acidi perfluoroalcansolfonici destinati a fare parte bella composizione |
FR2566794A1 (fr) * | 1984-06-28 | 1986-01-03 | El Paso Products Co | Procede pour ameliorer une essence naturelle de faible indice d'octane derivee du gaz naturel |
DE3586228D1 (de) * | 1984-09-10 | 1992-07-23 | Light Oil Utilization Res Ass | Fester starksauerer katalysator. |
US5095169A (en) * | 1988-03-30 | 1992-03-10 | Uop | Normal paraffin hydrocarbon isomerization process using activated zeolite beta |
US4956521A (en) * | 1988-10-06 | 1990-09-11 | Uop | Adsorption and isomerization of normal and mono-methyl paraffins |
US5069794A (en) * | 1990-06-05 | 1991-12-03 | Mobil Oil Corp. | Separation of mixture components over membrane composed of a pure molecular sieve |
US5233121A (en) * | 1990-10-23 | 1993-08-03 | Amoco Corporation | Process for the catalytic isomerization of light hydrocarbons |
CA2103876A1 (fr) * | 1992-08-27 | 1994-02-28 | Stuart Leon Soled | Zircone modifiee par un oxyde de tungstene et de la silice renfermant un metal du groupe viii comme catalyseur acide |
US5719097A (en) * | 1993-07-22 | 1998-02-17 | Chang; Clarence D. | Catalyst comprising a modified solid oxide |
KR100327099B1 (ko) * | 1993-07-22 | 2002-08-17 | 엑손모빌 오일 코포레이션 | 개질된고체산화촉매및그의제조방법 |
CA2135451A1 (fr) * | 1993-11-12 | 1995-05-13 | Pierre Grandvallet | Procede pour la preparation de paraffines a ramifications multiples |
US5744684A (en) * | 1994-11-03 | 1998-04-28 | Uop | Process for alkane isomerization using reactive chromatography and reactive desorbent |
FR2744458B1 (fr) * | 1996-02-05 | 1998-03-27 | Inst Francais Du Petrole | Procede d'isomerisation de paraffines par distillation reactive |
US5770783A (en) * | 1997-02-03 | 1998-06-23 | Uop Llc | Alkane isomerization using reversible flow reactive chromatography |
EP1172348A1 (fr) * | 2000-07-14 | 2002-01-16 | Haldor Topsoe A/S | Procédé pour l'isomérisation de parafffines |
US6348637B1 (en) * | 2000-09-26 | 2002-02-19 | Uop Llc | Multifunction fractionation column for adsorptive separation processes |
RU2001130402A (ru) * | 2001-11-13 | 2003-08-20 | Хальдор Топсеэ А/С (DK) | Способ изомеризации С5-С8 парафинового углеводородного сырья |
-
2003
- 2003-03-24 EP EP03006545A patent/EP1357167A1/fr not_active Withdrawn
- 2003-04-01 US US10/402,984 patent/US20030196931A1/en not_active Abandoned
- 2003-04-18 JP JP2003114687A patent/JP2003327972A/ja active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007217591A (ja) * | 2006-02-17 | 2007-08-30 | Japan Energy Corp | ガソリン基材の製造方法及びガソリン組成物 |
JP2007217589A (ja) * | 2006-02-17 | 2007-08-30 | Japan Energy Corp | ガソリン基材の製造方法及びガソリン組成物 |
JP2007217590A (ja) * | 2006-02-17 | 2007-08-30 | Japan Energy Corp | ガソリン基材の製造方法及びガソリン組成物 |
JP2010510351A (ja) * | 2006-11-20 | 2010-04-02 | ラマス テクノロジ インコーポレイテッド | 非還流型反応器ストリッパー |
JP2011241406A (ja) * | 2011-09-06 | 2011-12-01 | Jx Nippon Oil & Energy Corp | 環境対応型ガソリン組成物及びその製造方法 |
Also Published As
Publication number | Publication date |
---|---|
EP1357167A1 (fr) | 2003-10-29 |
US20030196931A1 (en) | 2003-10-23 |
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