DE60316415T2 - Mehrstufenverfahren zur umsetzung einer beschickung, die olefine mit drei, vier oder mehr kohlenstoffatomen enthält, zur herstellung von propylen - Google Patents
Mehrstufenverfahren zur umsetzung einer beschickung, die olefine mit drei, vier oder mehr kohlenstoffatomen enthält, zur herstellung von propylen Download PDFInfo
- Publication number
- DE60316415T2 DE60316415T2 DE60316415T DE60316415T DE60316415T2 DE 60316415 T2 DE60316415 T2 DE 60316415T2 DE 60316415 T DE60316415 T DE 60316415T DE 60316415 T DE60316415 T DE 60316415T DE 60316415 T2 DE60316415 T2 DE 60316415T2
- Authority
- DE
- Germany
- Prior art keywords
- oligomerization
- olefins
- cracking
- reactor
- feed
- 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.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title claims description 100
- QQONPFPTGQHPMA-UHFFFAOYSA-N Propene Chemical compound CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 title claims description 75
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title description 3
- 238000006384 oligomerization reaction Methods 0.000 claims description 165
- 150000001336 alkenes Chemical class 0.000 claims description 138
- 239000003054 catalyst Substances 0.000 claims description 110
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 claims description 101
- 238000005336 cracking Methods 0.000 claims description 85
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 69
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 68
- 239000010457 zeolite Substances 0.000 claims description 66
- 238000004523 catalytic cracking Methods 0.000 claims description 50
- 229910021536 Zeolite Inorganic materials 0.000 claims description 49
- 230000008569 process Effects 0.000 claims description 47
- 125000004432 carbon atom Chemical group C* 0.000 claims description 33
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 33
- 238000006243 chemical reaction Methods 0.000 claims description 31
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 30
- 239000005977 Ethylene Substances 0.000 claims description 29
- 238000005984 hydrogenation reaction Methods 0.000 claims description 28
- 150000001875 compounds Chemical class 0.000 claims description 26
- 229930195733 hydrocarbon Natural products 0.000 claims description 23
- 238000005194 fractionation Methods 0.000 claims description 22
- 150000002430 hydrocarbons Chemical class 0.000 claims description 22
- FXNDIJDIPNCZQJ-UHFFFAOYSA-N 2,4,4-trimethylpent-1-ene Chemical compound CC(=C)CC(C)(C)C FXNDIJDIPNCZQJ-UHFFFAOYSA-N 0.000 claims description 16
- 239000004215 Carbon black (E152) Substances 0.000 claims description 12
- 230000003197 catalytic effect Effects 0.000 claims description 11
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 claims description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 6
- 229910052782 aluminium Inorganic materials 0.000 claims description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 6
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 claims description 3
- GYHNNYVSQQEPJS-UHFFFAOYSA-N Gallium Chemical compound [Ga] GYHNNYVSQQEPJS-UHFFFAOYSA-N 0.000 claims description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 3
- 229910052796 boron Inorganic materials 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- 229910052733 gallium Inorganic materials 0.000 claims description 3
- 229910052742 iron Inorganic materials 0.000 claims description 3
- 229910052698 phosphorus Inorganic materials 0.000 claims description 3
- 239000011574 phosphorus Substances 0.000 claims description 3
- 229910052710 silicon Inorganic materials 0.000 claims description 3
- 239000010703 silicon Substances 0.000 claims description 3
- 239000011973 solid acid Substances 0.000 claims description 3
- 239000012530 fluid Substances 0.000 claims description 2
- 239000003502 gasoline Substances 0.000 description 29
- 230000008929 regeneration Effects 0.000 description 29
- 238000011069 regeneration method Methods 0.000 description 29
- 238000004519 manufacturing process Methods 0.000 description 23
- 238000004064 recycling Methods 0.000 description 23
- 238000004230 steam cracking Methods 0.000 description 23
- 239000007789 gas Substances 0.000 description 20
- 239000000203 mixture Substances 0.000 description 15
- 238000004821 distillation Methods 0.000 description 13
- 239000001257 hydrogen Substances 0.000 description 13
- 229910052739 hydrogen Inorganic materials 0.000 description 13
- 229910000323 aluminium silicate Inorganic materials 0.000 description 11
- 150000001993 dienes Chemical class 0.000 description 11
- 238000005516 engineering process Methods 0.000 description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 10
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 10
- 238000001816 cooling Methods 0.000 description 10
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 9
- 230000015572 biosynthetic process Effects 0.000 description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 8
- 239000003921 oil Substances 0.000 description 8
- 239000000047 product Substances 0.000 description 8
- 238000011144 upstream manufacturing Methods 0.000 description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 7
- 239000002585 base Substances 0.000 description 7
- 230000008901 benefit Effects 0.000 description 7
- 230000008030 elimination Effects 0.000 description 7
- 238000003379 elimination reaction Methods 0.000 description 7
- 238000000605 extraction Methods 0.000 description 7
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 7
- 239000001301 oxygen Substances 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 7
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 6
- 238000009835 boiling Methods 0.000 description 6
- 235000013844 butane Nutrition 0.000 description 6
- 239000000543 intermediate Substances 0.000 description 6
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 6
- 239000003350 kerosene Substances 0.000 description 6
- 150000005673 monoalkenes Chemical class 0.000 description 6
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 5
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 description 5
- 125000004122 cyclic group Chemical group 0.000 description 5
- 238000000151 deposition Methods 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- -1 olefin hydrocarbons Chemical class 0.000 description 5
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 4
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 4
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 4
- 238000004939 coking Methods 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 4
- 230000008021 deposition Effects 0.000 description 4
- 150000002431 hydrogen Chemical class 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000003208 petroleum Substances 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 239000000377 silicon dioxide Substances 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- 238000011282 treatment Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000000571 coke Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 238000009795 derivation Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000032050 esterification Effects 0.000 description 3
- 238000005886 esterification reaction Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 239000001282 iso-butane Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000011159 matrix material Substances 0.000 description 3
- 238000005649 metathesis reaction Methods 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 229910052763 palladium Inorganic materials 0.000 description 3
- 125000004817 pentamethylene group Chemical class [H]C([H])([*:2])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[*:1] 0.000 description 3
- YWAKXRMUMFPDSH-UHFFFAOYSA-N pentene Chemical compound CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 239000002841 Lewis acid Substances 0.000 description 2
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical class CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 2
- WTEOIRVLGSZEPR-UHFFFAOYSA-N boron trifluoride Chemical compound FB(F)F WTEOIRVLGSZEPR-UHFFFAOYSA-N 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000000567 combustion gas Substances 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 239000000539 dimer Substances 0.000 description 2
- 238000000895 extractive distillation Methods 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 125000004836 hexamethylene group Chemical class [H]C([H])([*:2])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[*:1] 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 150000007517 lewis acids Chemical class 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000002243 precursor Substances 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 238000000066 reactive distillation Methods 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- IAQRGUVFOMOMEM-ONEGZZNKSA-N trans-but-2-ene Chemical compound C\C=C\C IAQRGUVFOMOMEM-ONEGZZNKSA-N 0.000 description 2
- 238000006276 transfer reaction Methods 0.000 description 2
- 239000013638 trimer Substances 0.000 description 2
- 229910001868 water Inorganic materials 0.000 description 2
- PMJHHCWVYXUKFD-SNAWJCMRSA-N (E)-1,3-pentadiene Chemical compound C\C=C\C=C PMJHHCWVYXUKFD-SNAWJCMRSA-N 0.000 description 1
- LAAVYEUJEMRIGF-UHFFFAOYSA-N 2,4,4-trimethylpent-2-ene Chemical compound CC(C)=CC(C)(C)C LAAVYEUJEMRIGF-UHFFFAOYSA-N 0.000 description 1
- BKOOMYPCSUNDGP-UHFFFAOYSA-N 2-methylbut-2-ene Chemical group CC=C(C)C BKOOMYPCSUNDGP-UHFFFAOYSA-N 0.000 description 1
- YHQXBTXEYZIYOV-UHFFFAOYSA-N 3-methylbut-1-ene Chemical compound CC(C)C=C YHQXBTXEYZIYOV-UHFFFAOYSA-N 0.000 description 1
- 241001136792 Alle Species 0.000 description 1
- 229910015900 BF3 Inorganic materials 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 101001094044 Mus musculus Solute carrier family 26 member 6 Proteins 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229910021627 Tin(IV) chloride Inorganic materials 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 238000007259 addition reaction Methods 0.000 description 1
- 150000004996 alkyl benzenes Chemical class 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- NEHMKBQYUWJMIP-NJFSPNSNSA-N chloro(114C)methane Chemical compound [14CH3]Cl NEHMKBQYUWJMIP-NJFSPNSNSA-N 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000006471 dimerization reaction Methods 0.000 description 1
- 239000010771 distillate fuel oil Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 238000004231 fluid catalytic cracking Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- SYSQUGFVNFXIIT-UHFFFAOYSA-N n-[4-(1,3-benzoxazol-2-yl)phenyl]-4-nitrobenzenesulfonamide Chemical class C1=CC([N+](=O)[O-])=CC=C1S(=O)(=O)NC1=CC=C(C=2OC3=CC=CC=C3N=2)C=C1 SYSQUGFVNFXIIT-UHFFFAOYSA-N 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 238000010915 one-step procedure Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 150000002941 palladium compounds Chemical class 0.000 description 1
- 238000005504 petroleum refining Methods 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 210000002023 somite Anatomy 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000003457 sulfones Chemical class 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- NBRKLOOSMBRFMH-UHFFFAOYSA-N tert-butyl chloride Chemical compound CC(C)(C)Cl NBRKLOOSMBRFMH-UHFFFAOYSA-N 0.000 description 1
- 238000004227 thermal cracking Methods 0.000 description 1
- HPGGPRDJHPYFRM-UHFFFAOYSA-J tin(iv) chloride Chemical compound Cl[Sn](Cl)(Cl)Cl HPGGPRDJHPYFRM-UHFFFAOYSA-J 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 150000003738 xylenes Chemical class 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
- C07C11/06—Propene
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/02—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
- C07C2/04—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation
- C07C2/06—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation of alkenes, i.e. acyclic hydrocarbons having only one carbon-to-carbon double bond
- C07C2/08—Catalytic processes
- C07C2/12—Catalytic processes with crystalline alumino-silicates or with catalysts comprising molecular sieves
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Crystallography & Structural Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR0203211 | 2002-03-15 | ||
| FR0203211A FR2837199B1 (fr) | 2002-03-15 | 2002-03-15 | Procede de conversion en plusieurs etapes d'une charge comprenant des olefines a quatre, cinq atomes de carbone ou plus, en vue de produire du propylene |
| PCT/FR2003/000728 WO2003078364A1 (fr) | 2002-03-15 | 2003-03-06 | Procede de conversion en plusieurs etapes d'une charge comprenant des olefines a quatre, cinq atomes de carbone ou plus, en vue de produire du propylene |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| DE60316415D1 DE60316415D1 (de) | 2007-10-31 |
| DE60316415T2 true DE60316415T2 (de) | 2008-01-17 |
Family
ID=27772142
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE60316415T Expired - Lifetime DE60316415T2 (de) | 2002-03-15 | 2003-03-06 | Mehrstufenverfahren zur umsetzung einer beschickung, die olefine mit drei, vier oder mehr kohlenstoffatomen enthält, zur herstellung von propylen |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US7262332B2 (enExample) |
| EP (1) | EP1487768B1 (enExample) |
| JP (1) | JP4665397B2 (enExample) |
| CN (1) | CN100475755C (enExample) |
| AU (1) | AU2003227818A1 (enExample) |
| DE (1) | DE60316415T2 (enExample) |
| FR (1) | FR2837199B1 (enExample) |
| RU (1) | RU2299191C2 (enExample) |
| WO (1) | WO2003078364A1 (enExample) |
Families Citing this family (57)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2877590B1 (fr) * | 2004-11-09 | 2007-01-12 | Inst Francais Du Petrole | Dispositif reactionnel a plusieurs zones en lit mobile avec appoint dans chaque zone de catalyseur regenere ou frais |
| FR2879620B1 (fr) * | 2004-12-21 | 2007-02-23 | Inst Francais Du Petrole | Procede de conversion directe d'une charge comprenant des olefines a quatre et/ou cinq atomes de carbone, pour la production de propylene avec une co-production d'essence |
| CN100413826C (zh) * | 2005-08-15 | 2008-08-27 | 中国石油化工股份有限公司 | 生产丙烯的方法 |
| CN100413823C (zh) * | 2005-09-07 | 2008-08-27 | 中国石油化工股份有限公司 | 催化裂解生产丙烯的方法 |
| FR2892126B1 (fr) * | 2005-10-19 | 2010-04-30 | Inst Francais Du Petrole | Procede de conversion directe d'une charge comprenant des olefines a quatre, et/ou cinq atomes de carbone, pour la production de propylene avec une co-production d'essence desulfuree |
| US8299312B2 (en) * | 2005-10-28 | 2012-10-30 | Neste Oil Oyj | Process for dimerizing olefins |
| US7459593B1 (en) * | 2005-11-18 | 2008-12-02 | Uop Llc | Metathesis unit pretreatment process with formation of octene |
| KR101368416B1 (ko) * | 2006-02-03 | 2014-03-05 | 리액션 35, 엘엘씨 | 천연 가스를 액체 탄화수소로 변환시키는 연속 공정 |
| FR2905122B1 (fr) * | 2006-08-24 | 2009-07-24 | Inst Francais Du Petrole | Procede de production de propylene en presence d'un catalyseur macroporeux se presentant sous forme de billes spheriques |
| JP5355910B2 (ja) * | 2008-03-13 | 2013-11-27 | 旭化成ケミカルズ株式会社 | シリカ成形体 |
| JP5478253B2 (ja) * | 2007-09-18 | 2014-04-23 | 旭化成ケミカルズ株式会社 | プロピレンの製造方法 |
| TW200918486A (en) * | 2007-09-18 | 2009-05-01 | Asahi Kasei Chemicals Corp | Process for production of propylene |
| CN101492334B (zh) * | 2008-01-23 | 2012-11-14 | 中国石油化工股份有限公司 | 提高混合碳四化工利用价值的方法 |
| CN101492335B (zh) * | 2008-01-23 | 2013-07-31 | 中国石油化工股份有限公司 | 综合利用混合碳四的组合方法 |
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| US9434891B2 (en) | 2012-11-12 | 2016-09-06 | Uop Llc | Apparatus for recovering oligomerate |
| US9522375B2 (en) | 2012-11-12 | 2016-12-20 | Uop Llc | Apparatus for fluid catalytic cracking oligomerate |
| US9914673B2 (en) | 2012-11-12 | 2018-03-13 | Uop Llc | Process for oligomerizing light olefins |
| US9441173B2 (en) | 2012-11-12 | 2016-09-13 | Uop Llc | Process for making diesel by oligomerization |
| US9834492B2 (en) | 2012-11-12 | 2017-12-05 | Uop Llc | Process for fluid catalytic cracking oligomerate |
| US9663415B2 (en) | 2012-11-12 | 2017-05-30 | Uop Llc | Process for making diesel by oligomerization of gasoline |
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| US10011778B2 (en) | 2013-12-17 | 2018-07-03 | Uop Llc | Process and apparatus for improving propylene yield from a fluid catalytic cracking process |
| US9670425B2 (en) | 2013-12-17 | 2017-06-06 | Uop Llc | Process for oligomerizing and cracking to make propylene and aromatics |
| US9732285B2 (en) | 2013-12-17 | 2017-08-15 | Uop Llc | Process for oligomerization of gasoline to make diesel |
| US10556229B2 (en) | 2014-08-01 | 2020-02-11 | Chiyoda Corporation | Composite catalyst, method for producing composite catalyst, method for producing lower olefin and method for regenerating composite catalyst |
| RU2701018C2 (ru) * | 2014-09-30 | 2019-09-24 | Дау Глоубл Текнолоджиз Ллк | Способ увеличения выхода этилена и пропилена на установке получения пропилена |
| FR3049954A1 (fr) | 2016-04-08 | 2017-10-13 | Ifp Energies Now | Utilisation de zeolithe nu-86 pour le procede de craquage catalytique de naphtha |
| CN111116287A (zh) * | 2018-10-30 | 2020-05-08 | 中国石油化工股份有限公司 | 制备丙烯和乙烯的方法 |
| CN111116288B (zh) * | 2018-10-30 | 2023-09-29 | 中国石油化工股份有限公司 | 生产丙烯和乙烯的方法 |
| CN109369319B (zh) * | 2018-12-07 | 2021-11-12 | 宁波旭合瑞石化工程有限公司 | 一种以c4-c8烯烃为原料最大化生产丙烯的方法 |
| CN111718753B (zh) * | 2019-03-22 | 2021-10-08 | 中国石油化工股份有限公司 | 一种多产丙烯的催化转化方法和系统 |
| CN111718230B (zh) * | 2019-03-22 | 2023-04-11 | 中国石油化工股份有限公司 | 一种生产丙烯的方法和系统 |
| CN111718752B (zh) * | 2019-03-22 | 2021-11-16 | 中国石油化工股份有限公司 | 一种多产丙烯的催化裂化方法和系统 |
| CN111718750B (zh) * | 2019-03-22 | 2021-12-17 | 中国石油化工股份有限公司 | 一种制取丙烯的方法和系统 |
| EP3990420A4 (en) * | 2019-06-27 | 2023-07-12 | GEVO, Inc. | OLIGOMERIZATION OF BIOLOGICALLY DERIVED OLEFINS THROUGH A CHABAZITE-TYPE ZEOLITE CATALYST |
| CN111825514B (zh) * | 2020-08-12 | 2021-06-01 | 浙江科茂环境科技有限公司 | 一种乙烯或丙烯最大化的生产方法 |
| CN115784830B (zh) * | 2021-09-10 | 2024-08-23 | 北京石油化工工程有限公司 | 一种提高低碳烯烃收率的耦合工艺方法和耦合工艺系统 |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0109059B1 (en) * | 1982-11-10 | 1987-07-15 | MONTEDIPE S.p.A. | Process for converting olefins having 4 to 12 carbon atoms into propylene |
| SU1385517A1 (ru) * | 1986-04-16 | 1999-09-27 | Институт катализа СО АН СССР | Способ получения пропилена |
| FR2663946B1 (fr) * | 1990-05-09 | 1994-04-29 | Inst Francais Du Petrole | Procede de craquage catalytique en presence d'un catalyseur renfermant une zeolite zsm a ouverture de pore intermediaire. |
| GB9225183D0 (en) * | 1992-12-02 | 1993-01-20 | British Petroleum Co Plc | Process for the production of branched olefins |
| FR2755958B1 (fr) * | 1996-11-19 | 1999-01-08 | Inst Francais Du Petrole | Zeolithe nu-86 desaluminee et son utilisation en conversion des hydrocarbures |
| EP0921181A1 (en) * | 1997-12-05 | 1999-06-09 | Fina Research S.A. | Production of propylene |
| EP0920911A1 (en) * | 1997-12-05 | 1999-06-09 | Fina Research S.A. | Production of catalysts for olefin conversion |
| US6049017A (en) * | 1998-04-13 | 2000-04-11 | Uop Llc | Enhanced light olefin production |
| FR2837213B1 (fr) * | 2002-03-15 | 2004-08-20 | Inst Francais Du Petrole | Procede de production conjointe de propylene et d'essence a partir d'une charge relativement lourde |
-
2002
- 2002-03-15 FR FR0203211A patent/FR2837199B1/fr not_active Expired - Fee Related
-
2003
- 2003-03-06 WO PCT/FR2003/000728 patent/WO2003078364A1/fr not_active Ceased
- 2003-03-06 AU AU2003227818A patent/AU2003227818A1/en not_active Abandoned
- 2003-03-06 CN CNB03806104XA patent/CN100475755C/zh not_active Expired - Lifetime
- 2003-03-06 EP EP03725271A patent/EP1487768B1/fr not_active Expired - Lifetime
- 2003-03-06 US US10/507,853 patent/US7262332B2/en not_active Expired - Lifetime
- 2003-03-06 RU RU2004130481/04A patent/RU2299191C2/ru active
- 2003-03-06 DE DE60316415T patent/DE60316415T2/de not_active Expired - Lifetime
- 2003-03-06 JP JP2003576373A patent/JP4665397B2/ja not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| RU2299191C2 (ru) | 2007-05-20 |
| FR2837199B1 (fr) | 2005-09-16 |
| WO2003078364A1 (fr) | 2003-09-25 |
| US20050222475A1 (en) | 2005-10-06 |
| JP2005520874A (ja) | 2005-07-14 |
| US7262332B2 (en) | 2007-08-28 |
| DE60316415D1 (de) | 2007-10-31 |
| CN100475755C (zh) | 2009-04-08 |
| EP1487768B1 (fr) | 2007-09-19 |
| RU2004130481A (ru) | 2005-07-20 |
| FR2837199A1 (fr) | 2003-09-19 |
| AU2003227818A1 (en) | 2003-09-29 |
| CN1642887A (zh) | 2005-07-20 |
| EP1487768A1 (fr) | 2004-12-22 |
| JP4665397B2 (ja) | 2011-04-06 |
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