DE2400452A1 - Verfahren zur gewinnung und trennung von aromatischen kohlenwasserstoffen von grosser reinheit aus rohoelfraktionen - Google Patents
Verfahren zur gewinnung und trennung von aromatischen kohlenwasserstoffen von grosser reinheit aus rohoelfraktionenInfo
- Publication number
- DE2400452A1 DE2400452A1 DE2400452A DE2400452A DE2400452A1 DE 2400452 A1 DE2400452 A1 DE 2400452A1 DE 2400452 A DE2400452 A DE 2400452A DE 2400452 A DE2400452 A DE 2400452A DE 2400452 A1 DE2400452 A1 DE 2400452A1
- Authority
- DE
- Germany
- Prior art keywords
- hydrocarbons
- zone
- reaction zone
- catalyst
- fraction
- 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.)
- Ceased
Links
- 150000004945 aromatic hydrocarbons Chemical class 0.000 title claims description 38
- 238000000034 method Methods 0.000 title claims description 36
- 238000011084 recovery Methods 0.000 title description 8
- 238000000926 separation method Methods 0.000 title description 7
- 239000010779 crude oil Substances 0.000 title 1
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 81
- 238000006243 chemical reaction Methods 0.000 claims description 77
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 64
- 239000003054 catalyst Substances 0.000 claims description 64
- 229930195733 hydrocarbon Natural products 0.000 claims description 33
- 150000002430 hydrocarbons Chemical class 0.000 claims description 33
- 239000002904 solvent Substances 0.000 claims description 30
- 238000000895 extractive distillation Methods 0.000 claims description 29
- 238000000605 extraction Methods 0.000 claims description 21
- 239000001257 hydrogen Substances 0.000 claims description 20
- 229910052739 hydrogen Inorganic materials 0.000 claims description 20
- 239000000203 mixture Substances 0.000 claims description 20
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 18
- 229930195734 saturated hydrocarbon Natural products 0.000 claims description 16
- 125000004432 carbon atom Chemical group C* 0.000 claims description 13
- 229910052751 metal Inorganic materials 0.000 claims description 13
- 239000002184 metal Substances 0.000 claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 238000004821 distillation Methods 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 239000008096 xylene Substances 0.000 claims description 7
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 claims description 6
- 125000003118 aryl group Chemical group 0.000 claims description 5
- 230000000737 periodic effect Effects 0.000 claims description 5
- 238000005194 fractionation Methods 0.000 claims description 4
- 150000002739 metals Chemical class 0.000 claims description 4
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 2
- 239000004927 clay Substances 0.000 claims 1
- 239000012071 phase Substances 0.000 description 16
- 238000011069 regeneration method Methods 0.000 description 12
- 230000008929 regeneration Effects 0.000 description 11
- 238000009835 boiling Methods 0.000 description 8
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 8
- 238000002407 reforming Methods 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 6
- 230000003197 catalytic effect Effects 0.000 description 6
- 239000004215 Carbon black (E152) Substances 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 5
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 4
- 230000002378 acidificating effect Effects 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- AFABGHUZZDYHJO-UHFFFAOYSA-N dimethyl butane Natural products CCCC(C)C AFABGHUZZDYHJO-UHFFFAOYSA-N 0.000 description 4
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 4
- QWTDNUCVQCZILF-UHFFFAOYSA-N isopentane Chemical compound CCC(C)C QWTDNUCVQCZILF-UHFFFAOYSA-N 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 150000005673 monoalkenes Chemical class 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 229910052697 platinum Inorganic materials 0.000 description 4
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 3
- 238000005336 cracking Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 229910052741 iridium Inorganic materials 0.000 description 3
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 3
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 3
- ZONODCCBXBRQEZ-UHFFFAOYSA-N platinum tungsten Chemical compound [W].[Pt] ZONODCCBXBRQEZ-UHFFFAOYSA-N 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 229910052702 rhenium Inorganic materials 0.000 description 3
- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 150000003738 xylenes Chemical class 0.000 description 3
- GXDHCNNESPLIKD-UHFFFAOYSA-N 2-methylhexane Natural products CCCCC(C)C GXDHCNNESPLIKD-UHFFFAOYSA-N 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical class [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 2
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 230000001588 bifunctional effect Effects 0.000 description 2
- 238000004517 catalytic hydrocracking Methods 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 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
- 150000001875 compounds Chemical class 0.000 description 2
- 150000001993 dienes Chemical class 0.000 description 2
- 230000008030 elimination Effects 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000001282 iso-butane Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- GDOPTJXRTPNYNR-UHFFFAOYSA-N methylcyclopentane Chemical compound CC1CCCC1 GDOPTJXRTPNYNR-UHFFFAOYSA-N 0.000 description 2
- 229910052750 molybdenum Inorganic materials 0.000 description 2
- 239000011733 molybdenum Substances 0.000 description 2
- 229910052763 palladium Inorganic materials 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- CFQCIHVMOFOCGH-UHFFFAOYSA-N platinum ruthenium Chemical compound [Ru].[Pt] CFQCIHVMOFOCGH-UHFFFAOYSA-N 0.000 description 2
- GRLYPOPFNDQSKV-UHFFFAOYSA-N rhenium ruthenium Chemical compound [Ru].[Re] GRLYPOPFNDQSKV-UHFFFAOYSA-N 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 239000000126 substance Substances 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
- YUHZIUAREWNXJT-UHFFFAOYSA-N (2-fluoropyridin-3-yl)boronic acid Chemical class OB(O)C1=CC=CN=C1F YUHZIUAREWNXJT-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- NHTMVDHEPJAVLT-UHFFFAOYSA-N Isooctane Chemical class CC(C)CC(C)(C)C NHTMVDHEPJAVLT-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- DIHHPRGAZFQUHZ-UHFFFAOYSA-N [Mo].[Ir] Chemical compound [Mo].[Ir] DIHHPRGAZFQUHZ-UHFFFAOYSA-N 0.000 description 1
- NZPGFUCQQUDSQG-UHFFFAOYSA-N [Mo].[Re] Chemical compound [Mo].[Re] NZPGFUCQQUDSQG-UHFFFAOYSA-N 0.000 description 1
- KFOLLPUZRCFERL-UHFFFAOYSA-N [O-2].[Mg+2].O=[Si]=O Chemical class [O-2].[Mg+2].O=[Si]=O KFOLLPUZRCFERL-UHFFFAOYSA-N 0.000 description 1
- CNGGOAOYPQGTLH-UHFFFAOYSA-N [O-2].[O-2].[Mg+2].[Al+3] Chemical class [O-2].[O-2].[Mg+2].[Al+3] CNGGOAOYPQGTLH-UHFFFAOYSA-N 0.000 description 1
- HHUIAYDQMNHELC-UHFFFAOYSA-N [O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O Chemical class [O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O HHUIAYDQMNHELC-UHFFFAOYSA-N 0.000 description 1
- YEWLVPDHCCERJH-UHFFFAOYSA-N [Re].[Ir] Chemical compound [Re].[Ir] YEWLVPDHCCERJH-UHFFFAOYSA-N 0.000 description 1
- FNYLUKDQSKKYHG-UHFFFAOYSA-N [Ru].[W] Chemical compound [Ru].[W] FNYLUKDQSKKYHG-UHFFFAOYSA-N 0.000 description 1
- IGUHATROZYFXKR-UHFFFAOYSA-N [W].[Ir] Chemical compound [W].[Ir] IGUHATROZYFXKR-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000008431 aliphatic amides Chemical class 0.000 description 1
- 238000005899 aromatization reaction Methods 0.000 description 1
- WIRUZQNBHNAMAB-UHFFFAOYSA-N benzene;cyclohexane Chemical compound C1CCCCC1.C1=CC=CC=C1 WIRUZQNBHNAMAB-UHFFFAOYSA-N 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 238000001833 catalytic reforming Methods 0.000 description 1
- WHDPTDWLEKQKKX-UHFFFAOYSA-N cobalt molybdenum Chemical compound [Co].[Co].[Mo] WHDPTDWLEKQKKX-UHFFFAOYSA-N 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000009918 complex formation Effects 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000006356 dehydrogenation reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- CVXDNAAVZJWUKJ-UHFFFAOYSA-N ethylbenzene;1,2-xylene Chemical group CCC1=CC=CC=C1.CC1=CC=CC=C1C CVXDNAAVZJWUKJ-UHFFFAOYSA-N 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 229910052732 germanium Inorganic materials 0.000 description 1
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- -1 hickel Chemical compound 0.000 description 1
- CJTCBBYSPFAVFL-UHFFFAOYSA-N iridium ruthenium Chemical compound [Ru].[Ir] CJTCBBYSPFAVFL-UHFFFAOYSA-N 0.000 description 1
- ZUBZATZOEPUUQF-UHFFFAOYSA-N isononane Chemical class CCCCCCC(C)C ZUBZATZOEPUUQF-UHFFFAOYSA-N 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- UAEPNZWRGJTJPN-UHFFFAOYSA-N methylcyclohexane Chemical compound CC1CCCCC1 UAEPNZWRGJTJPN-UHFFFAOYSA-N 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- LCEDQNDDFOCWGG-UHFFFAOYSA-N morpholine-4-carbaldehyde Chemical compound O=CN1CCOCC1 LCEDQNDDFOCWGG-UHFFFAOYSA-N 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- BKIMMITUMNQMOS-UHFFFAOYSA-N nonane Chemical class CCCCCCCCC BKIMMITUMNQMOS-UHFFFAOYSA-N 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 229910052762 osmium Inorganic materials 0.000 description 1
- SYQBFIAQOQZEGI-UHFFFAOYSA-N osmium atom Chemical compound [Os] SYQBFIAQOQZEGI-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- DBJYYRBULROVQT-UHFFFAOYSA-N platinum rhenium Chemical compound [Re].[Pt] DBJYYRBULROVQT-UHFFFAOYSA-N 0.000 description 1
- HWLDNSXPUQTBOD-UHFFFAOYSA-N platinum-iridium alloy Chemical compound [Ir].[Pt] HWLDNSXPUQTBOD-UHFFFAOYSA-N 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 238000007100 recyclization reaction Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 229910052703 rhodium Inorganic materials 0.000 description 1
- 239000010948 rhodium Substances 0.000 description 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 238000001577 simple distillation Methods 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000004230 steam cracking Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 239000003039 volatile agent Substances 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
- C10G35/00—Reforming naphtha
- C10G35/04—Catalytic reforming
- C10G35/06—Catalytic reforming characterised by the catalyst used
-
- 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
- C10G35/00—Reforming naphtha
- C10G35/04—Catalytic reforming
- C10G35/06—Catalytic reforming characterised by the catalyst used
- C10G35/085—Catalytic reforming characterised by the catalyst used containing platinum group metals or compounds thereof
- C10G35/09—Bimetallic catalysts in which at least one of the metals is a platinum group metal
-
- 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
- C10G61/00—Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen
- C10G61/02—Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen plural serial stages only
- C10G61/04—Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen plural serial stages only the refining step being an extraction
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR7300806A FR2213335B1 (enExample) | 1973-01-10 | 1973-01-10 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE2400452A1 true DE2400452A1 (de) | 1974-07-11 |
Family
ID=9113113
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE2400452A Ceased DE2400452A1 (de) | 1973-01-10 | 1974-01-05 | Verfahren zur gewinnung und trennung von aromatischen kohlenwasserstoffen von grosser reinheit aus rohoelfraktionen |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US3992465A (enExample) |
| JP (1) | JPS49133337A (enExample) |
| DE (1) | DE2400452A1 (enExample) |
| FR (1) | FR2213335B1 (enExample) |
| GB (1) | GB1430482A (enExample) |
| IT (1) | IT1006836B (enExample) |
Families Citing this family (38)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4069134A (en) * | 1976-10-26 | 1978-01-17 | Uop Inc. | Hydrogen-producing hydrocarbon conversion with gravity-flowing catalyst particles |
| US4167473A (en) * | 1977-06-27 | 1979-09-11 | Uop Inc. | Multiple-stage catalytic reforming with gravity-flowing dissimilar catalyst particles |
| US4193895A (en) * | 1977-10-14 | 1980-03-18 | Union Oil Company Of California | Aromatization process and catalyst |
| US4191637A (en) * | 1977-10-14 | 1980-03-04 | Union Oil Company Of California | Aromatization process and catalyst |
| US4233244A (en) | 1978-09-18 | 1980-11-11 | Texaco Inc. | Novel technique for reacting vinyl cyclohexene with nitrobenzene in the presence of a hydrogen-transfer catalyst |
| US4237070A (en) | 1978-09-20 | 1980-12-02 | Texaco Inc. | Novel process for preparing aniline by catalytic reaction of vinyl cyclohexene and nitrobenzene |
| US4322556A (en) | 1979-03-01 | 1982-03-30 | Texaco Inc. | Method for preparing aniline by reaction of nitrobenzene and vinylcyclohexene |
| US4235701A (en) * | 1979-03-30 | 1980-11-25 | Atlantic Richfield Company | Aromatics from dripolene |
| US4431521A (en) * | 1982-09-27 | 1984-02-14 | Exxon Research & Engineering Co. | Benzene recovery process |
| JPH0670225B2 (ja) * | 1985-09-13 | 1994-09-07 | 三菱石油株式会社 | ヘプタン製品の製造方法 |
| US4944849A (en) * | 1989-07-12 | 1990-07-31 | Phillips Petroleum Company | Extractive distillation of cycloalkane/alkane feed employing solvent mixture |
| CA2055929A1 (en) * | 1990-12-14 | 1992-06-15 | William C. Baird, Jr. | Process for reforming at low severities with high activity, high yield tin modified platinum-iridium catalysts |
| US5203988A (en) * | 1991-08-19 | 1993-04-20 | Exxon Research & Engineering Company | Multistage reforming with ultra-low pressure cyclic second stage |
| DE69230621T2 (de) * | 1991-12-09 | 2000-08-10 | Exxon Research And Engineering Co., Florham Park | Festbett/fliessbett-zweistufige, katalytische reformen |
| US5196110A (en) * | 1991-12-09 | 1993-03-23 | Exxon Research And Engineering Company | Hydrogen recycle between stages of two stage fixed-bed/moving-bed unit |
| US5221463A (en) * | 1991-12-09 | 1993-06-22 | Exxon Research & Engineering Company | Fixed-bed/moving-bed two stage catalytic reforming with recycle of hydrogen-rich stream to both stages |
| US5211838A (en) * | 1991-12-09 | 1993-05-18 | Exxon Research & Engineering Company | Fixed-bed/moving-bed two stage catalytic reforming with interstage aromatics removal |
| US5190639A (en) * | 1991-12-09 | 1993-03-02 | Exxon Research And Engineering Company | Multiple fixed-bed reforming units sharing common moving bed reactor |
| DE69229875T2 (de) * | 1991-12-09 | 2000-04-20 | Exxon Research And Engineering Co., Florham Park | Reformierung mit zwei festbetteinheiten; jede mit einem wanderbettendreaktor, die einen gemeinsamen regenerator teilen |
| US5354451A (en) * | 1991-12-09 | 1994-10-11 | Exxon Research And Engineering Company | Fixed-bed/moving-bed two stage catalytic reforming |
| US5190638A (en) * | 1991-12-09 | 1993-03-02 | Exxon Research And Engineering Company | Moving bed/fixed bed two stage catalytic reforming |
| US5401386A (en) * | 1992-07-24 | 1995-03-28 | Chevron Research And Technology Company | Reforming process for producing high-purity benzene |
| DE19603901A1 (de) * | 1996-02-03 | 1997-08-07 | Krupp Uhde Gmbh | Verfahren zur Gewinnung von Reinaromaten aus Reformatbenzin und Vorrichtung zur Durchführung des Verfahrens |
| FR2801605B1 (fr) * | 1999-11-30 | 2002-02-01 | Inst Francais Du Petrole | Procede et dispositif pour la production d'aromatiques incluant une reduction du catalyseur |
| JP4260025B2 (ja) * | 2002-03-20 | 2009-04-30 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ | 炭化水素質供給原料の接触改質法 |
| JP5011127B2 (ja) | 2005-01-21 | 2012-08-29 | エクソンモービル リサーチ アンド エンジニアリング カンパニー | 水素源からの水素含有ストリーム中の水素の管理 |
| EP2050731B1 (en) * | 2006-08-07 | 2017-07-05 | Nippon Oil Corporation | Process for production of aromatic hydrocarbons |
| US20090018110A1 (en) * | 2007-06-06 | 2009-01-15 | Andrew Levy | Haptoglobin genotyping for prognosis and treatment of chronic vasospasm following subarachnoid hemorrhage (SAH) |
| US7811447B2 (en) * | 2007-08-01 | 2010-10-12 | Uop Llc | Method of transferring particles from one pressure zone to another pressure zone |
| US7803326B2 (en) * | 2007-08-01 | 2010-09-28 | Uop Llc | Hydrocarbon conversion unit including a reaction zone receiving transferred catalyst |
| FR2946660B1 (fr) * | 2009-06-10 | 2011-07-22 | Inst Francais Du Petrole | Procede de reformage pregeneratif des essences comportant le recyclage d'au moins une partie de l'effluent de la phase de reduction du catalyseur. |
| FR2961215B1 (fr) * | 2010-06-09 | 2013-11-08 | Inst Francais Du Petrole | Nouveau procede de reformage catalytique avec recyclage de l'effluent de reduction en amont du premier reacteur et recyclage du gaz de recyclage sur le ou les derniers reacteurs de la serie. |
| CN101967078A (zh) * | 2010-10-25 | 2011-02-09 | 内江天科化工有限责任公司 | 一种粗苯加氢精制方法 |
| US8679320B2 (en) * | 2011-04-29 | 2014-03-25 | Uop Llc | Process for increasing benzene and toluene production |
| US8679321B2 (en) * | 2011-04-29 | 2014-03-25 | Uop Llc | Process for increasing benzene and toluene production |
| US20120277500A1 (en) * | 2011-04-29 | 2012-11-01 | Uop Llc | High Temperature Platforming Process |
| US9199893B2 (en) | 2014-02-24 | 2015-12-01 | Uop Llc | Process for xylenes production |
| US9718042B2 (en) | 2015-12-23 | 2017-08-01 | Chevron Phillips Chemical Company Lp | Aromatization reactors with hydrogen removal and related reactor systems |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2834822A (en) * | 1958-05-13 | Toluene | ||
| US2877173A (en) * | 1955-03-23 | 1959-03-10 | Standard Oil Co | Hydroforming process |
| US2969317A (en) * | 1958-05-27 | 1961-01-24 | Texaco Inc | Petroleum treating process |
| US3387052A (en) * | 1966-05-11 | 1968-06-04 | Universal Oil Prod Co | Process for production of aromatic hydrocarbons |
| US3551327A (en) * | 1969-03-12 | 1970-12-29 | Universal Oil Prod Co | Extractive distillation of aromatics with a sulfolane solvent |
-
1973
- 1973-01-10 FR FR7300806A patent/FR2213335B1/fr not_active Expired
-
1974
- 1974-01-02 US US05/430,157 patent/US3992465A/en not_active Expired - Lifetime
- 1974-01-05 DE DE2400452A patent/DE2400452A1/de not_active Ceased
- 1974-01-08 GB GB83974A patent/GB1430482A/en not_active Expired
- 1974-01-09 JP JP49005825A patent/JPS49133337A/ja active Pending
- 1974-01-10 IT IT19253/74A patent/IT1006836B/it active
Also Published As
| Publication number | Publication date |
|---|---|
| US3992465A (en) | 1976-11-16 |
| GB1430482A (en) | 1976-03-31 |
| USB430157I5 (enExample) | 1976-02-17 |
| FR2213335A1 (enExample) | 1974-08-02 |
| IT1006836B (it) | 1976-10-20 |
| FR2213335B1 (enExample) | 1976-04-23 |
| JPS49133337A (enExample) | 1974-12-21 |
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