JP2018520863A - メソポーラスシリカフォームメタセシス触媒を使用するプロピレン生成 - Google Patents
メソポーラスシリカフォームメタセシス触媒を使用するプロピレン生成 Download PDFInfo
- Publication number
- JP2018520863A JP2018520863A JP2017568232A JP2017568232A JP2018520863A JP 2018520863 A JP2018520863 A JP 2018520863A JP 2017568232 A JP2017568232 A JP 2017568232A JP 2017568232 A JP2017568232 A JP 2017568232A JP 2018520863 A JP2018520863 A JP 2018520863A
- Authority
- JP
- Japan
- Prior art keywords
- metathesis catalyst
- metathesis
- butene
- propylene
- catalyst
- 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.)
- Granted
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 126
- 238000005649 metathesis reaction Methods 0.000 title claims abstract description 113
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 title claims abstract description 103
- 239000000377 silicon dioxide Substances 0.000 title claims abstract description 47
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 title claims abstract description 44
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 title claims abstract description 44
- 239000006260 foam Substances 0.000 title claims abstract description 37
- 238000004519 manufacturing process Methods 0.000 title description 9
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 claims abstract description 72
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 claims abstract description 56
- 238000000034 method Methods 0.000 claims abstract description 46
- 239000011148 porous material Substances 0.000 claims abstract description 44
- 230000008569 process Effects 0.000 claims abstract description 36
- 229910044991 metal oxide Inorganic materials 0.000 claims abstract description 30
- 150000004706 metal oxides Chemical class 0.000 claims abstract description 30
- 238000009826 distribution Methods 0.000 claims abstract description 16
- XNMQEEKYCVKGBD-UHFFFAOYSA-N dimethylacetylene Natural products CC#CC XNMQEEKYCVKGBD-UHFFFAOYSA-N 0.000 claims description 26
- 238000006317 isomerization reaction Methods 0.000 claims description 18
- 229920000428 triblock copolymer Polymers 0.000 claims description 17
- 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 12
- 229910001930 tungsten oxide Inorganic materials 0.000 claims description 12
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims description 9
- 229910052721 tungsten Inorganic materials 0.000 claims description 9
- 239000010937 tungsten Substances 0.000 claims description 9
- 238000005686 cross metathesis reaction Methods 0.000 claims description 7
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical group OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 5
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 5
- 229920000463 Poly(ethylene glycol)-block-poly(propylene glycol)-block-poly(ethylene glycol) Polymers 0.000 claims description 5
- 229910052750 molybdenum Inorganic materials 0.000 claims description 5
- 239000011733 molybdenum Substances 0.000 claims description 5
- 229910052702 rhenium Inorganic materials 0.000 claims description 5
- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 description 16
- 239000000047 product Substances 0.000 description 14
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 12
- 239000003795 chemical substances by application Substances 0.000 description 9
- 150000001336 alkenes Chemical class 0.000 description 8
- 230000015572 biosynthetic process Effects 0.000 description 8
- 230000000694 effects Effects 0.000 description 8
- 239000000203 mixture Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 238000005865 alkene metathesis reaction Methods 0.000 description 7
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 238000005470 impregnation Methods 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 229910052757 nitrogen Inorganic materials 0.000 description 6
- 238000003917 TEM image Methods 0.000 description 5
- 230000003197 catalytic effect Effects 0.000 description 5
- 239000006185 dispersion Substances 0.000 description 5
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 5
- 238000003786 synthesis reaction Methods 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
- 239000002243 precursor Substances 0.000 description 4
- 239000004094 surface-active agent Substances 0.000 description 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 3
- 229920002415 Pluronic P-123 Polymers 0.000 description 3
- 125000003118 aryl group Chemical group 0.000 description 3
- 239000012153 distilled water Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000007086 side reaction Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- DDFHBQSCUXNBSA-UHFFFAOYSA-N 5-(5-carboxythiophen-2-yl)thiophene-2-carboxylic acid Chemical compound S1C(C(=O)O)=CC=C1C1=CC=C(C(O)=O)S1 DDFHBQSCUXNBSA-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-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
- 239000004115 Sodium Silicate Substances 0.000 description 2
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- IAQRGUVFOMOMEM-ARJAWSKDSA-N cis-but-2-ene Chemical compound C\C=C/C IAQRGUVFOMOMEM-ARJAWSKDSA-N 0.000 description 2
- 238000004939 coking Methods 0.000 description 2
- 230000009849 deactivation Effects 0.000 description 2
- 239000003085 diluting agent Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 2
- 230000001788 irregular Effects 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 230000000737 periodic effect Effects 0.000 description 2
- 229920001983 poloxamer Polymers 0.000 description 2
- 229920001223 polyethylene glycol Polymers 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 2
- 229910052911 sodium silicate Inorganic materials 0.000 description 2
- 239000012265 solid product Substances 0.000 description 2
- 238000006276 transfer reaction Methods 0.000 description 2
- ZNOKGRXACCSDPY-UHFFFAOYSA-N tungsten trioxide Chemical compound O=[W](=O)=O ZNOKGRXACCSDPY-UHFFFAOYSA-N 0.000 description 2
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical group CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 1
- RVGRUAULSDPKGF-UHFFFAOYSA-N Poloxamer Chemical group C1CO1.CC1CO1 RVGRUAULSDPKGF-UHFFFAOYSA-N 0.000 description 1
- ONIBWKKTOPOVIA-UHFFFAOYSA-N Proline Natural products OC(=O)C1CCCN1 ONIBWKKTOPOVIA-UHFFFAOYSA-N 0.000 description 1
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000006356 dehydrogenation reaction Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000004231 fluid catalytic cracking Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- YWAKXRMUMFPDSH-UHFFFAOYSA-N pentene Chemical compound CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 description 1
- 229920001451 polypropylene glycol Polymers 0.000 description 1
- -1 polypropylene, propylene Polymers 0.000 description 1
- 238000000634 powder X-ray diffraction Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 238000004445 quantitative analysis Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 238000000527 sonication Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 125000001424 substituent group Chemical group 0.000 description 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 1
- IAQRGUVFOMOMEM-ONEGZZNKSA-N trans-but-2-ene Chemical compound C\C=C\C IAQRGUVFOMOMEM-ONEGZZNKSA-N 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
- C07C6/02—Metathesis reactions at an unsaturated carbon-to-carbon bond
- C07C6/04—Metathesis reactions at an unsaturated carbon-to-carbon bond at a carbon-to-carbon double bond
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/08—Silica
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/30—Tungsten
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/03—Catalysts comprising molecular sieves not having base-exchange properties
- B01J29/0308—Mesoporous materials not having base exchange properties, e.g. Si-MCM-41
- B01J29/0341—Mesoporous materials not having base exchange properties, e.g. Si-MCM-41 containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/56—Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional monoliths
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/615—100-500 m2/g
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/617—500-1000 m2/g
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/63—Pore volume
- B01J35/635—0.5-1.0 ml/g
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/63—Pore volume
- B01J35/638—Pore volume more than 1.0 ml/g
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
- B01J35/647—2-50 nm
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
- B01J37/0018—Addition of a binding agent or of material, later completely removed among others as result of heat treatment, leaching or washing,(e.g. forming of pores; protective layer, desintegrating by heat)
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0201—Impregnation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
- C07C11/06—Propene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
- B01J2231/50—Redistribution or isomerisation reactions of C-C, C=C or C-C triple bonds
- B01J2231/54—Metathesis reactions, e.g. olefin metathesis
- B01J2231/543—Metathesis reactions, e.g. olefin metathesis alkene metathesis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
- B01J2523/40—Constitutive chemical elements of heterogeneous catalysts of Group IV (IVA or IVB) of the Periodic Table
- B01J2523/41—Silicon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
- B01J2523/60—Constitutive chemical elements of heterogeneous catalysts of Group VI (VIA or VIB) of the Periodic Table
- B01J2523/68—Molybdenum
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
- B01J2523/60—Constitutive chemical elements of heterogeneous catalysts of Group VI (VIA or VIB) of the Periodic Table
- B01J2523/69—Tungsten
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
- B01J2523/70—Constitutive chemical elements of heterogeneous catalysts of Group VII (VIIB) of the Periodic Table
- B01J2523/74—Rhenium
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
- C07C2521/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- C07C2521/08—Silica
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/24—Chromium, molybdenum or tungsten
- C07C2523/28—Molybdenum
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/24—Chromium, molybdenum or tungsten
- C07C2523/30—Tungsten
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/32—Manganese, technetium or rhenium
- C07C2523/36—Rhenium
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2529/00—Catalysts comprising molecular sieves
- C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
- C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- C07C2529/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups C07C2529/08 - C07C2529/65
- C07C2529/78—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups C07C2529/08 - C07C2529/65 containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Dispersion Chemistry (AREA)
- Catalysts (AREA)
- Nanotechnology (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Description
超大細孔を有するメソポーラスシリカフォームを以下の方法で合成した。典型的な合成では、3.0グラム(g)の中性トリブロック共重合体界面活性剤、Pluronic(登録商標)P123を、酢酸(3.0g)、脱イオン(DI)水(52g)、及びフッ化アンモニウム(0.3g)の混合物中で、40℃で溶解した。2時間撹拌した後、水(40g)中のケイ酸ナトリウム(2.35g)の溶液を添加し、結果として得られた混合物を5分間強く撹拌しながら反応させた。次いで、混合物を40℃で24時間静止状態下に置き、その後、70℃で一晩エイジングした。固体生成物をDI水で洗浄し、濾過で収集し、空気乾燥させた。次いで、得られた固体を560℃で6時間焼成し、鋳型を取り除いた。
トリブロック共重合体、ポリ(エチレングリコール)−ブロック−ポリ(プロピレングリコール)−ブロック−ポリ(エチレングリコール)を構造指向剤として使用して、SBA−15物質を合成した。典型的な合成では、4gのPluronic P123を30mlの水に添加した。数時間撹拌した後、透明な溶液を得た。約70gの0.28Molar(M)塩酸をそれに添加し、その溶液をさらに2時間撹拌した。次いで、9gのオルトケイ酸テトラエチル(TEOS)を添加し、結果として得られた混合物を40℃で24時間撹拌し、最終的に48時間で100℃まで加熱した。固体生成物を濾過によって回収し、水で数回洗浄し、100℃で一晩乾燥させた。最終的に、その生成物を550℃で6時間焼成し、鋳型を取り除いた。
MCM−41を、Beckら[J.S.Beck,J.C.Vartuli,W.J.Roth,M.E.Leonowicz,C.T.Kresge,K.D.Schmitt,C.T.−U.Chu,D.H.Olsen,E.W.Sheppard,S.B.McCullen,J.B.Higgins,J.L.Schlenker,J.Am.Chem.Soc.114,10834(1992)]の手順に従って合成した。
調製した触媒を、ブテンメタセシス反応に対するその活性及び選択性について、固定床連続流式反応器(ID 0.25in、Autoclave Engineers Ltd)において大気圧で検査した。一定量の触媒試料(2ml)を、炭化ケイ素が反応器の上部及び底部にある状態で反応器の管に詰めた。触媒をN2下で550℃で1時間前処理した。全反応を、550℃、900h−1のGHSV(ガス空間速度)、大気圧で、窒素を希釈剤(25ml/分)として含む供給物として2−ブテン(5ml/分)を使用して実行した。CP−Al2O3/Na2SO4キャピラリーカラム(50メートル(m)長×0.32ミリメートル(mm)I.D.×膜厚(df)=5マイクロメートル(μm))を備えるフレームイオン化検出器(FID)を含むVarianガスクロマトグラフ(Varian 450−GC)を使用して、反応生成物の定量分析をオンラインで実行した。
図4のグラフは、900h−1のGHSV(ガス空間速度)で、大気圧で、窒素を希釈剤(25ml/分)として含む供給物として2−ブテン(5ml/分)を使用する図1〜図3の触媒の異性化活性及び2−ブテン変換を示す。図示するように、2−ブテン変換(左側のY軸で示す)は、触媒A〜Cについて類似の結果をもたらした。しかしながら、2−ブテンの1−ブテンへの異性化は、触媒A〜C間で大きく異なる。具体的には、シリカフォーム触媒Aは、450Cで95重量%の選択性の値を有するが、他の触媒B及びCは、90%以下である。上述のように、異性化選択性が高くなると、交差メタセシス工程で産生されるプロピレンの量が増加する。また、異性化選択性が高くなると、コーキング及び触媒失活を引き起こし得る副反応も減少する。
表2は、550℃(GHSV 900h−1)での触媒A〜Cのメタセシス活性を示す。2−ブテンのメタセシス反応(反応温度:550℃、大気圧、GHSV900h−1)における触媒A〜Cの触媒性能。シリカフォームを担体として調製された触媒Aは、触媒B及びCと比較して、より高い2−ブテン変換及びより良好なプロピレン収率を示す。触媒Aのより高い収率は、2−ブテンの1−ブテンへの選択的異性化に関連し、これが、さらなる交差メタセシス反応を受けてプロピレンを生成する。触媒Aは、大きな細孔径を有し、これが、高メタセシス活性をもたらすWO3種のより高い分散を提供する。物質の酸性は、2−ブテンの1−ブテンへの異性化において重要な役割を果たし、これが、2−ブテンと1−ブテンとの間のメタセシス反応の活性を強化する。芳香族及びより高い化合物の収率が、他の触媒と比較して、触媒Aについて、少ないことが分かり、それによって、触媒Aのより高いメタセシス活性が示された。
試料の表面積を、AUTOSORB−1(Quanta Chrome)を使用して77Kで窒素吸着によって測定した。吸着測定前に、試料(約0.1g)を220℃で2時間窒素フロー下で加熱した。触媒の窒素吸着等温線を液体窒素温度(77K)で測定した。表面積及び細孔径分布をBrunauer Emmett−Teller(BET)方法及びBarrett−Joyner−Halenda(BJH)方法によってそれぞれ計算した。全細孔容積を、P/P0=0.99で吸着したN2の量から推定した。Barret EP、Joyner LJ、Halenda PH、J.Am.Chem.Soc.73(1951)373−380。
Claims (20)
- プロピレンを生成するためのメタセシス工程であって、
金属酸化物を含浸させた非晶質メソポーラスシリカフォームを含むメタセシス触媒を提供することであって、前記メタセシス触媒は、少なくとも3nm〜40nmの細孔径分布及び少なくとも0.700cm3/gの全細孔容積を有する、提供することと、
ブテンを含む供給流を前記メタセシス触媒と接触させることによって、プロピレンを含む生成物流を生成することと、を含む、メタセシス工程。 - トリブロック共重合体構造化剤をさらに含み、前記トリブロック共重合体構造化剤は、ポリ(エチレングリコール)−ブロック−ポリ(プロピレングリコール)−ブロック−ポリ(エチレングリコール)構造である、請求項1に記載の工程。
- 前記メタセシス触媒は、2−ブテンの1−ブテンへの異性化、続いて、プロピレンを含むメタセシス生成物流への2−ブテン及び1−ブテンの交差メタセシスを触媒する、請求項2に記載の工程。
- 前記2−ブテンの少なくとも90%は、異性化を介して1−ブテンに変換される、請求項3に記載の工程。
- 前記細孔径分布は、少なくとも4nm〜10nmであり、前記全細孔容積は、少なくとも0.800cm3/g〜1.5cm3/gである、請求項1に記載の工程。
- 前記メタセシス触媒は、0.125mmol/g〜0.500mmol/gの総酸度、及び400〜500m2/gの表面積を有する、請求項1に記載の工程。
- 前記金属酸化物は、モリブデン、レニウム、タングステン、またはそれらの組み合わせの酸化物である、請求項1に記載の工程。
- 前記金属酸化物は、酸化タングステンである、請求項1に記載の工程。
- 前記メタセシス触媒は、1〜50の酸化タングステンに対するシリカのモル比を有する、請求項8に記載の工程。
- 前記メタセシス触媒は、5〜15重量%の酸化タングステンを含む、請求項8に記載の工程。
- プロピレンを生成するためのメタセシス触媒であって、
金属酸化物を含浸させた非晶質メソポーラスシリカフォームであって、前記メタセシス触媒は、少なくとも3nm〜40nmの細孔径分布及び少なくとも0.700cm3/gの全細孔容積を有する、非晶質メソポーラスシリカフォーム、を含む、メタセシス触媒。 - トリブロック共重合体構造化剤をさらに含み、前記トリブロック共重合体構造化剤は、ポリ(エチレングリコール)−ブロック−ポリ(プロピレングリコール)−ブロック−ポリ(エチレングリコール)構造である、請求項11に記載のメタセシス触媒。
- 前記細孔径分布は、少なくとも4nm〜10nmであり、前記全細孔容積は、少なくとも0.800cm3/g〜1.5cm3/gである、請求項11に記載のメタセシス触媒。
- 前記メタセシス触媒は、0.125mmol/g〜0.500mmol/gの総酸度を有する、請求項11に記載のメタセシス触媒。
- 前記金属酸化物は、モリブデン、レニウム、タングステン、またはそれらの組み合わせの酸化物である、請求項11に記載のメタセシス触媒。
- 前記金属酸化物は、酸化タングステンである、請求項11に記載のメタセシス触媒。
- 前記メタセシス触媒は、1〜50の酸化タングステンに対するシリカのモル比を有する、請求項16に記載のメタセシス触媒。
- 前記メタセシス触媒は、5〜15重量%の金属酸化物を含む、請求項11に記載のメタセシス触媒。
- 前記メタセシス触媒は、2nm〜4nmの範囲の細孔径を有する、請求項11に記載のメタセシス触媒。
- 前記メタセシス触媒は、400〜500m2/gの表面積を有する、請求項11に記載のメタセシス触媒。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201562188129P | 2015-07-02 | 2015-07-02 | |
US62/188,129 | 2015-07-02 | ||
PCT/US2016/039025 WO2017003821A1 (en) | 2015-07-02 | 2016-06-23 | Propylene production using a mesoporous silica foam metathesis catalyst |
Publications (3)
Publication Number | Publication Date |
---|---|
JP2018520863A true JP2018520863A (ja) | 2018-08-02 |
JP2018520863A5 JP2018520863A5 (ja) | 2019-07-25 |
JP6802195B2 JP6802195B2 (ja) | 2020-12-16 |
Family
ID=56409171
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2017568232A Active JP6802195B2 (ja) | 2015-07-02 | 2016-06-23 | メソポーラスシリカフォームメタセシス触媒を使用するプロピレン生成 |
Country Status (7)
Country | Link |
---|---|
US (1) | US10005703B2 (ja) |
EP (1) | EP3317014B1 (ja) |
JP (1) | JP6802195B2 (ja) |
KR (1) | KR102592369B1 (ja) |
CN (1) | CN107921425B (ja) |
SA (1) | SA517390653B1 (ja) |
WO (1) | WO2017003821A1 (ja) |
Families Citing this family (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10005793B2 (en) * | 2012-10-01 | 2018-06-26 | The General Hospital Corporation | Bodipy dyes for biological imaging |
KR102387487B1 (ko) | 2015-07-02 | 2022-04-18 | 사우디 아라비안 오일 컴퍼니 | 프로필렌을 제조하기 위한 시스템 및 방법 |
WO2017003817A1 (en) | 2015-07-02 | 2017-01-05 | Saudi Arabian Oil Company | Systems and methods for producing propylene |
KR102178406B1 (ko) | 2015-07-02 | 2020-11-16 | 사우디 아라비안 오일 컴퍼니 | 프로필렌 제조용의 이중 촉매 시스템 |
US10010870B2 (en) | 2015-11-12 | 2018-07-03 | Saudi Arabian Oil Company | Synthesis of catalytic materials for metathesis and isomerization reactions and other catalytic applications via well controlled aerosol processing |
US9969621B2 (en) * | 2016-05-04 | 2018-05-15 | Saudi Arabian Oil Company | Methods for processing fumed metallic oxides |
US10550048B2 (en) * | 2017-01-20 | 2020-02-04 | Saudi Arabian Oil Company | Multiple-stage catalyst system for self-metathesis with controlled isomerization and cracking |
US10934231B2 (en) | 2017-01-20 | 2021-03-02 | Saudi Arabian Oil Company | Multiple-stage catalyst systems and processes for propene production |
US10329225B2 (en) | 2017-01-20 | 2019-06-25 | Saudi Arabian Oil Company | Dual catalyst processes and systems for propylene production |
US10407363B2 (en) * | 2017-08-16 | 2019-09-10 | Saudi Arabian Oil Company | Steam-less process for converting butenes to 1,3-butadiene |
CN111050910A (zh) | 2017-08-17 | 2020-04-21 | 沙特阿拉伯石油公司 | 用于表面物质的受控涂覆以生成催化剂的气溶胶处理方法 |
JP2021500226A (ja) * | 2017-10-24 | 2021-01-07 | サウジ アラビアン オイル カンパニー | 噴霧乾燥メタセシス触媒の製造方法およびその使用 |
US11369950B2 (en) | 2018-02-21 | 2022-06-28 | Saudi Arabian Oil Company | Multi-functional composite catalyst materials and methods of synthesizing the catalyst materials |
US11242299B2 (en) | 2018-10-10 | 2022-02-08 | Saudi Arabian Oil Company | Catalyst systems that include metal oxide co-catalysts for the production of propylene |
US10961171B2 (en) | 2018-10-10 | 2021-03-30 | Saudi Arabian Oil Company | Catalysts systems that include metal co-catalysts for the production of propylene |
US11033892B2 (en) | 2019-01-24 | 2021-06-15 | Saudi Arabian Oil Company | Methods for reacting chemical streams with catalysts comprising silica, alumina, and tungsten |
US11185850B2 (en) | 2019-12-02 | 2021-11-30 | Saudi Arabian Oil Company | Dual functional composite catalyst for olefin metathesis and cracking |
US11311869B2 (en) | 2019-12-03 | 2022-04-26 | Saudi Arabian Oil Company | Methods of producing isomerization catalysts |
US11517892B2 (en) | 2019-12-03 | 2022-12-06 | Saudi Arabian Oil Company | Methods of producing isomerization catalysts |
US20210170367A1 (en) * | 2019-12-05 | 2021-06-10 | Saudi Arabian Oil Company | Metathesis catalysts and methods of producing propene |
US11339332B2 (en) | 2020-01-29 | 2022-05-24 | Saudi Arabian Oil Company | Systems and processes integrating fluidized catalytic cracking with metathesis for producing olefins |
US11572516B2 (en) | 2020-03-26 | 2023-02-07 | Saudi Arabian Oil Company | Systems and processes integrating steam cracking with dual catalyst metathesis for producing olefins |
US11679378B2 (en) | 2021-02-25 | 2023-06-20 | Saudi Arabian Oil Company | Methods of producing isomerization catalysts |
US11845705B2 (en) | 2021-08-17 | 2023-12-19 | Saudi Arabian Oil Company | Processes integrating hydrocarbon cracking with metathesis for producing propene |
CN114130363A (zh) * | 2021-11-08 | 2022-03-04 | 中国科学院山西煤炭化学研究所 | 煤灰提铝渣制备介孔SiO2泡沫基固态胺吸附剂的方法 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008136280A1 (ja) * | 2007-04-27 | 2008-11-13 | Mitsui Chemicals, Inc. | オレフィンの製造方法 |
JP2010013366A (ja) * | 2008-07-01 | 2010-01-21 | Sumitomo Chemical Co Ltd | プロピレンの製造方法 |
US8324440B2 (en) * | 2010-02-05 | 2012-12-04 | Uop Llc | Support properties of silica supported catalysts and their use in olefin metathesis |
JP2014523856A (ja) * | 2011-04-28 | 2014-09-18 | ビーエーエスエフ ソシエタス・ヨーロピア | 軽質α−オレフィンの軽質内部オレフィンへの異性化 |
Family Cites Families (36)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL135562C (ja) | 1967-04-03 | |||
GB1489300A (en) | 1974-08-26 | 1977-10-19 | Agency Ind Science Techn | Process for the selective disproportionation reaction of olefins |
US4071471A (en) | 1974-12-23 | 1978-01-31 | Phillips Petroleum Company | Catalysts for conversion of olefins |
DE3775059D1 (de) | 1983-03-10 | 1992-01-16 | Dow Chemical Co | Verfahren zur disproportionierung von alkenen. |
GB8828481D0 (en) * | 1988-12-06 | 1989-01-05 | Euro Matic Ltd | Date coding play balls |
US5026935A (en) | 1989-10-02 | 1991-06-25 | Arco Chemical Technology, Inc. | Enhanced production of ethylene from higher hydrocarbons |
US5026936A (en) | 1989-10-02 | 1991-06-25 | Arco Chemical Technology, Inc. | Enhanced production of propylene from higher hydrocarbons |
FR2733986B1 (fr) | 1995-05-11 | 1997-06-13 | Inst Francais Du Petrole | Procede et installation pour la conversion de coupes c4 olefiniques en polyisobutenes et en propylene |
DE19746040A1 (de) | 1997-10-17 | 1999-04-22 | Basf Ag | Verfahren zur Herstellung von Propen |
EP0921181A1 (en) | 1997-12-05 | 1999-06-09 | Fina Research S.A. | Production of propylene |
US6586649B1 (en) | 1998-09-04 | 2003-07-01 | Sasol Technology (Proprietary) Limited | Production of propylene |
DE19932060A1 (de) | 1999-07-12 | 2001-01-18 | Basf Ag | Verfahren zur Herstellung von C¶5¶-/C¶6¶-Olefinen |
US20050124839A1 (en) * | 2001-06-13 | 2005-06-09 | Gartside Robert J. | Catalyst and process for the metathesis of ethylene and butene to produce propylene |
MY139380A (en) | 2001-10-01 | 2009-09-30 | Basf Ag | Process for the preparation of alkylaryl compounds and sulfonates thereof |
US6777582B2 (en) | 2002-03-07 | 2004-08-17 | Abb Lummus Global Inc. | Process for producing propylene and hexene from C4 olefin streams |
CN100402148C (zh) | 2002-08-16 | 2008-07-16 | Sasol技术股份有限公司 | 复分解催化剂及方法 |
DE10319439A1 (de) | 2003-04-30 | 2004-11-18 | Basf Ag | Aktivierte Metathesekatalysatoren |
US7214841B2 (en) | 2003-07-15 | 2007-05-08 | Abb Lummus Global Inc. | Processing C4 olefin streams for the maximum production of propylene |
WO2005023420A1 (ja) * | 2003-09-03 | 2005-03-17 | The Circle For The Promotion Of Science And Engineering | メタセシス触媒およびそれを用いるオレフィンの製造方法 |
ITMI20040855A1 (it) | 2004-04-29 | 2004-07-29 | Polimeri Europa Spa | Catalizzatore di renio supportato su allimuna modificata e suo impiego nella reazione di metatesi delle olefine |
EP1770080B1 (en) | 2004-07-16 | 2015-05-27 | Asahi Kasei Chemicals Corporation | Process for producing ethylene and propylene |
DE102005009596A1 (de) | 2005-02-28 | 2006-08-31 | Basf Ag | Verfahren zur Metathese umfassend die Reinigung der Ausgangsstoffe |
CN1312038C (zh) * | 2005-06-16 | 2007-04-25 | 复旦大学 | 大孔容二氧化硅囊泡或泡沫材料及其制备方法 |
US7692057B2 (en) | 2005-08-15 | 2010-04-06 | China Petroleum & Chemical Corporation | Process for producing lower olefins by using multiple reaction zones |
US8648003B2 (en) | 2006-04-11 | 2014-02-11 | Agency For Science, Technology And Research | Catalysts for ring-closing metathesis |
US20090240010A1 (en) | 2008-03-20 | 2009-09-24 | Mcdaniel Max P | Alumina-silica activator-supports for metallocene catalyst compositions |
CN105367365A (zh) | 2008-08-12 | 2016-03-02 | 鲁姆斯科技公司 | 结合的丙烯生产 |
EP2330091A4 (en) | 2008-08-28 | 2013-02-06 | Mitsui Chemicals Inc | PREPARATION FOR OLEFIN |
BRPI0918229A2 (pt) | 2008-09-04 | 2016-03-01 | Basf Corp E Basf Ag | isomerizacao de olefina e catalisador de metatese |
US8586813B2 (en) | 2009-07-21 | 2013-11-19 | Lummus Technology Inc. | Catalyst for metathesis of ethylene and 2-butene and/or double bond isomerization |
US8895795B2 (en) | 2010-02-05 | 2014-11-25 | Uop Llc | Acid washed silica supported catalysts and their use in olefin metathesis |
US8722950B2 (en) | 2010-04-26 | 2014-05-13 | Saudi Basic Industries Corporation | Process for producing propylene and aromatics from butenes by metathesis and aromatization |
US20120289617A1 (en) | 2011-05-10 | 2012-11-15 | Saudi Arabian Oil Company | Hybrid Catalyst for Olefin Metathesis |
EP2862629A1 (en) | 2013-10-15 | 2015-04-22 | Borealis AG | Catalyst and process for olefin metathesis reaction |
CN104370676B (zh) | 2014-11-11 | 2016-06-08 | 中国石油天然气集团公司 | 一种以碳四烯烃为原料生产丙烯副产乙烯的方法 |
KR102178406B1 (ko) | 2015-07-02 | 2020-11-16 | 사우디 아라비안 오일 컴퍼니 | 프로필렌 제조용의 이중 촉매 시스템 |
-
2016
- 2016-06-23 WO PCT/US2016/039025 patent/WO2017003821A1/en active Application Filing
- 2016-06-23 JP JP2017568232A patent/JP6802195B2/ja active Active
- 2016-06-23 EP EP16738274.6A patent/EP3317014B1/en active Active
- 2016-06-23 US US15/190,950 patent/US10005703B2/en active Active
- 2016-06-23 CN CN201680038823.0A patent/CN107921425B/zh active Active
- 2016-06-23 KR KR1020187003228A patent/KR102592369B1/ko active IP Right Grant
-
2017
- 2017-12-31 SA SA517390653A patent/SA517390653B1/ar unknown
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008136280A1 (ja) * | 2007-04-27 | 2008-11-13 | Mitsui Chemicals, Inc. | オレフィンの製造方法 |
JP2010013366A (ja) * | 2008-07-01 | 2010-01-21 | Sumitomo Chemical Co Ltd | プロピレンの製造方法 |
US8324440B2 (en) * | 2010-02-05 | 2012-12-04 | Uop Llc | Support properties of silica supported catalysts and their use in olefin metathesis |
JP2014523856A (ja) * | 2011-04-28 | 2014-09-18 | ビーエーエスエフ ソシエタス・ヨーロピア | 軽質α−オレフィンの軽質内部オレフィンへの異性化 |
Non-Patent Citations (1)
Title |
---|
THE JOURNAL OF PHYSICAL CHEMISTRY C, vol. VOL:117, NR:49, JPN5018004161, 2013, pages 26385 - 26395, ISSN: 0004142079 * |
Also Published As
Publication number | Publication date |
---|---|
CN107921425B (zh) | 2021-11-30 |
KR102592369B1 (ko) | 2023-10-25 |
US20170001925A1 (en) | 2017-01-05 |
EP3317014B1 (en) | 2022-03-02 |
WO2017003821A1 (en) | 2017-01-05 |
US10005703B2 (en) | 2018-06-26 |
SA517390653B1 (ar) | 2021-06-15 |
JP6802195B2 (ja) | 2020-12-16 |
KR20180055800A (ko) | 2018-05-25 |
CN107921425A (zh) | 2018-04-17 |
EP3317014A1 (en) | 2018-05-09 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP6802195B2 (ja) | メソポーラスシリカフォームメタセシス触媒を使用するプロピレン生成 | |
JP2018520863A5 (ja) | ||
KR102178406B1 (ko) | 프로필렌 제조용의 이중 촉매 시스템 | |
DK1616846T3 (en) | A process for the oligomerization of olefins using a catalyst based on silica-alumina | |
CN110267932B (zh) | 用于自复分解连同受控异构化和裂化的多级催化剂系统 | |
KR102293960B1 (ko) | 프로필렌 생산을 위한 이중 촉매 공정 및 시스템 | |
Meng et al. | Synthesis of novel hierarchically porous NiMo/ZSM-5-KIT-5 catalysts and their superior performance in hydrodenitrogenation of quinoline | |
JP2011080063A (ja) | マクロ細孔性シリカ−アルミナをベースとする触媒を用いるオレフィン炭化水素供給原料のオリゴマー化方法 | |
Zheng et al. | Study of mesoporous catalysts for conversion of 2, 3-butanediol to butenes | |
JP2017510556A (ja) | 脱水‐加水分解方法およびそのための触媒 | |
JP2014151253A (ja) | オレフィン低重合方法およびそれに用いる触媒 | |
Hu et al. | Metathesis of 1-butene and ethene to propene over mesoporous W-KIT-6 catalysts: the influence of Si/W ratio | |
KR20210059783A (ko) | 프로필렌 제조를 위한 금속 산화물 공촉매를 포함하는 촉매 | |
US20190118164A1 (en) | Methods of Making Spray-dried Metathesis Catalysts and Uses Thereof | |
KR20210068066A (ko) | 프로필렌 제조를 위한 금속 산화물 공촉매를 포함하는 촉매 | |
Martín et al. | Synthesis and characterization of a mesoporous HMS and its use as support of platinum catalysts |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20180508 |
|
A524 | Written submission of copy of amendment under article 19 pct |
Free format text: JAPANESE INTERMEDIATE CODE: A524 Effective date: 20190621 |
|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20190621 |
|
A871 | Explanation of circumstances concerning accelerated examination |
Free format text: JAPANESE INTERMEDIATE CODE: A871 Effective date: 20190621 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20191024 |
|
A975 | Report on accelerated examination |
Free format text: JAPANESE INTERMEDIATE CODE: A971005 Effective date: 20191024 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20191030 |
|
A601 | Written request for extension of time |
Free format text: JAPANESE INTERMEDIATE CODE: A601 Effective date: 20200130 |
|
A601 | Written request for extension of time |
Free format text: JAPANESE INTERMEDIATE CODE: A601 Effective date: 20200330 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20200430 |
|
A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20200603 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20201005 |
|
C60 | Trial request (containing other claim documents, opposition documents) |
Free format text: JAPANESE INTERMEDIATE CODE: C60 Effective date: 20201005 |
|
A911 | Transfer to examiner for re-examination before appeal (zenchi) |
Free format text: JAPANESE INTERMEDIATE CODE: A911 Effective date: 20201012 |
|
C21 | Notice of transfer of a case for reconsideration by examiners before appeal proceedings |
Free format text: JAPANESE INTERMEDIATE CODE: C21 Effective date: 20201014 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20201028 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20201126 |
|
R150 | Certificate of patent or registration of utility model |
Ref document number: 6802195 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |