WO2006054527A1 - Reforming catalyst for oxygen-containing hydrocarbon, method for producing hydrogen or synthesis gas using same, and fuel cell system - Google Patents
Reforming catalyst for oxygen-containing hydrocarbon, method for producing hydrogen or synthesis gas using same, and fuel cell system Download PDFInfo
- Publication number
- WO2006054527A1 WO2006054527A1 PCT/JP2005/020871 JP2005020871W WO2006054527A1 WO 2006054527 A1 WO2006054527 A1 WO 2006054527A1 JP 2005020871 W JP2005020871 W JP 2005020871W WO 2006054527 A1 WO2006054527 A1 WO 2006054527A1
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- WIPO (PCT)
- Prior art keywords
- hydrogen
- oxygen
- reforming
- reforming catalyst
- results
- Prior art date
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- 239000001257 hydrogen Substances 0.000 title claims abstract description 66
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 66
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 60
- 239000007789 gas Substances 0.000 title claims abstract description 48
- 239000000446 fuel Substances 0.000 title claims abstract description 23
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 22
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 21
- 230000015572 biosynthetic process Effects 0.000 title claims abstract description 21
- 239000001301 oxygen Substances 0.000 title claims abstract description 21
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 21
- 238000003786 synthesis reaction Methods 0.000 title claims abstract description 18
- 239000003054 catalyst Substances 0.000 title abstract description 16
- 238000002407 reforming Methods 0.000 title abstract 12
- 229930195733 hydrocarbon Natural products 0.000 title abstract 4
- 150000002430 hydrocarbons Chemical class 0.000 title abstract 4
- 239000004215 Carbon black (E152) Substances 0.000 title abstract 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims abstract description 30
- 229910052802 copper Inorganic materials 0.000 claims abstract description 30
- 239000010949 copper Substances 0.000 claims abstract description 30
- 229910052751 metal Inorganic materials 0.000 claims abstract description 28
- 239000002184 metal Substances 0.000 claims abstract description 28
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract 4
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract 2
- 239000001569 carbon dioxide Substances 0.000 claims abstract 2
- 238000000034 method Methods 0.000 claims description 34
- 239000002994 raw material Substances 0.000 claims description 10
- 238000006213 oxygenation reaction Methods 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 13
- 229910052761 rare earth metal Inorganic materials 0.000 abstract description 9
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract 2
- 229910021536 Zeolite Inorganic materials 0.000 abstract 1
- 238000002453 autothermal reforming Methods 0.000 abstract 1
- 239000000571 coke Substances 0.000 abstract 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 abstract 1
- 229910044991 metal oxide Inorganic materials 0.000 abstract 1
- 150000004706 metal oxides Chemical class 0.000 abstract 1
- 230000003647 oxidation Effects 0.000 abstract 1
- 238000007254 oxidation reaction Methods 0.000 abstract 1
- 229910052596 spinel Inorganic materials 0.000 abstract 1
- 239000011029 spinel Substances 0.000 abstract 1
- 238000000629 steam reforming Methods 0.000 abstract 1
- 239000010457 zeolite Substances 0.000 abstract 1
- 238000002156 mixing Methods 0.000 description 34
- 238000006243 chemical reaction Methods 0.000 description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 23
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 18
- 230000009467 reduction Effects 0.000 description 17
- 150000001875 compounds Chemical class 0.000 description 15
- 239000007788 liquid Substances 0.000 description 14
- 150000002500 ions Chemical class 0.000 description 13
- 150000004767 nitrides Chemical class 0.000 description 13
- 239000013256 coordination polymer Substances 0.000 description 11
- 239000000463 material Substances 0.000 description 11
- 241000234671 Ananas Species 0.000 description 9
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 9
- 229910052697 platinum Inorganic materials 0.000 description 9
- 239000000126 substance Substances 0.000 description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 238000005342 ion exchange Methods 0.000 description 8
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 8
- 150000002431 hydrogen Chemical class 0.000 description 7
- JCCNYMKQOSZNPW-UHFFFAOYSA-N loratadine Chemical compound C1CN(C(=O)OCC)CCC1=C1C2=NC=CC=C2CCC2=CC(Cl)=CC=C21 JCCNYMKQOSZNPW-UHFFFAOYSA-N 0.000 description 7
- 239000000203 mixture Substances 0.000 description 7
- 239000000843 powder Substances 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 230000007423 decrease Effects 0.000 description 6
- 239000011734 sodium Substances 0.000 description 6
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 5
- 239000002253 acid Substances 0.000 description 5
- 229910052799 carbon Inorganic materials 0.000 description 5
- 239000011521 glass Substances 0.000 description 5
- 230000004044 response Effects 0.000 description 5
- 229910052708 sodium Inorganic materials 0.000 description 5
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 4
- 229910000040 hydrogen fluoride Inorganic materials 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 230000004048 modification Effects 0.000 description 4
- 238000012986 modification Methods 0.000 description 4
- 229910000510 noble metal Inorganic materials 0.000 description 4
- 229910052705 radium Inorganic materials 0.000 description 4
- HCWPIIXVSYCSAN-UHFFFAOYSA-N radium atom Chemical compound [Ra] HCWPIIXVSYCSAN-UHFFFAOYSA-N 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 241001648341 Orites Species 0.000 description 3
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- 239000012491 analyte Substances 0.000 description 3
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- 238000005755 formation reaction Methods 0.000 description 3
- 238000005470 impregnation Methods 0.000 description 3
- 239000007769 metal material Substances 0.000 description 3
- 125000001570 methylene group Chemical group [H]C([H])([*:1])[*:2] 0.000 description 3
- 229910052754 neon Inorganic materials 0.000 description 3
- GKAOGPIIYCISHV-UHFFFAOYSA-N neon atom Chemical compound [Ne] GKAOGPIIYCISHV-UHFFFAOYSA-N 0.000 description 3
- 235000006408 oxalic acid Nutrition 0.000 description 3
- -1 oxy- Chemical class 0.000 description 3
- 229910052698 phosphorus Inorganic materials 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 230000009257 reactivity Effects 0.000 description 3
- 241000234282 Allium Species 0.000 description 2
- 240000006108 Allium ampeloprasum Species 0.000 description 2
- 235000005254 Allium ampeloprasum Nutrition 0.000 description 2
- 235000002732 Allium cepa var. cepa Nutrition 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- CUJRVFIICFDLGR-UHFFFAOYSA-N acetylacetonate Chemical compound CC(=O)[CH-]C(C)=O CUJRVFIICFDLGR-UHFFFAOYSA-N 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 229910001882 dioxygen Inorganic materials 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229910021472 group 8 element Inorganic materials 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229910052741 iridium Inorganic materials 0.000 description 2
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 230000003287 optical effect Effects 0.000 description 2
- 239000005518 polymer electrolyte Substances 0.000 description 2
- 150000002910 rare earth metals Chemical class 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000010025 steaming Methods 0.000 description 2
- 241000241985 Cnides Species 0.000 description 1
- 241000255925 Diptera Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 241000545744 Hirudinea Species 0.000 description 1
- 241000234435 Lilium Species 0.000 description 1
- 150000001204 N-oxides Chemical class 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- FEWJPZIEWOKRBE-UHFFFAOYSA-N Tartaric acid Natural products [H+].[H+].[O-]C(=O)C(O)C(O)C([O-])=O FEWJPZIEWOKRBE-UHFFFAOYSA-N 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 238000000137 annealing Methods 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000003034 coal gas Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 150000002344 gold compounds Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 230000005923 long-lasting effect Effects 0.000 description 1
- 150000002736 metal compounds Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 150000002926 oxygen Chemical class 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
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- 229920002994 synthetic fiber Polymers 0.000 description 1
- 235000002906 tartaric acid Nutrition 0.000 description 1
- 239000011975 tartaric acid Substances 0.000 description 1
- NMJKIRUDPFBRHW-UHFFFAOYSA-N titanium Chemical compound [Ti].[Ti] NMJKIRUDPFBRHW-UHFFFAOYSA-N 0.000 description 1
- 230000001256 tonic effect Effects 0.000 description 1
Classifications
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- 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
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
- B01J29/42—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively containing iron group metals, noble metals or copper
-
- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/889—Manganese, technetium or rhenium
- B01J23/8892—Manganese
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- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
- B01J29/48—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively containing arsenic, antimony, bismuth, vanadium, niobium tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/323—Catalytic reaction of gaseous or liquid organic compounds other than hydrocarbons with gasifying agents
- C01B3/326—Catalytic reaction of gaseous or liquid organic compounds other than hydrocarbons with gasifying agents characterised by the catalyst
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
- H01M8/0618—Reforming processes, e.g. autothermal, partial oxidation or steam reforming
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- 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
- B01J23/005—Spinels
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- B01J35/19—
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
- C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
- C01B2203/0233—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam reforming step
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
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- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
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- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
- C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
- C01B2203/0238—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a carbon dioxide reforming step
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
- C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
- C01B2203/0244—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being an autothermal reforming step, e.g. secondary reforming processes
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/025—Processes for making hydrogen or synthesis gas containing a partial oxidation step
- C01B2203/0261—Processes for making hydrogen or synthesis gas containing a partial oxidation step containing a catalytic partial oxidation step [CPO]
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/06—Integration with other chemical processes
- C01B2203/066—Integration with other chemical processes with fuel cells
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1041—Composition of the catalyst
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1041—Composition of the catalyst
- C01B2203/1047—Group VIII metal catalysts
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1041—Composition of the catalyst
- C01B2203/1076—Copper or zinc-based catalysts
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- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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- 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
- Y02P20/141—Feedstock
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- 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
Definitions
- the present invention relates to a method for producing hydrogen syngas by making various modifications to hydrogen fluoride and oxygen, and to a battery system using this.
- 0002 gas is made up of oxygen and hydrogen, and is used as a gas for methano-, oxy-, and yat formations, and is widely used as a material for annealing and various products.
- This gas has been produced by conventional methods, or steam or partial methods using natural gas as a raw material.
- the coal law has a problem that it requires a complex and expensive coal gas furnace and a large-scale plant.
- the reaction of the steam in this case requires a large degree of reaction, requiring 7 to 2 ° C in the reaction line, requiring special modifications, and requiring the heat to be used. You.
- a high temperature is required, a special part is required, and a large amount of soot is generated with the reaction. Therefore, in order to solve this problem, in recent years,
- the fuel cell has been researched on hydrogen, such as gas mainly composed of methane and methane, city gas mainly composed of this gas, synthetic materials based on natural gas, and petroleum oil and NASA oil. It is.
- Various materials have been disclosed to be used in the production of hydrogen syngas by using various raw materials such as metite as raw materials.
- a technique to modify hydrogen oxyhydride for example, for C, a medium for producing gas from oxygen and dioxygen, and production of gas using the same (for example, a patent), C
- a medium for producing hydrogen from hydrogenated oxygen and water vapor and hydrogen using the medium for example, Patent 2
- a material bearing a genus including solid C for example, Patent 3, Patent 4
- a medium for producing hydrogen from oxygen and water vapor which is a mixture of a C-containing substance and a solid substance, and hydrogen produced using the medium.
- Patent 5 a medium for producing a gas from oxygen and water vapor, and a gas production using the medium (for example, Patent 6) made of a mixture of a C-containing substance and a solid substance are disclosed. It is.
- the purpose is to provide a method for producing hydrogen synthesis gas by making various modifications to oxygen. Also this excellent
- An object of the present invention is to provide an excellent fuel cell system having a fuel cell using hydrogen produced as a fuel.
- the heat is increased and the activity is increased and the durability is improved.
- it contains anana, group 8 and rare earth elements.
- the present invention provides a battery cell system for hydrogen synthesis gas having the following elements.
- Olite is 5 () ⁇ (3) deviation element 0.99 (5) contains copper, contains metal, olite and analyse () ⁇ (4) deviation Of the element described in. (6) Olyte contains 8 and / or earth elements () to (5).
- the genus of (6) is a genus of at least one kind selected from e and Co.
- Hydrogen fluoride is at least one of the elements selected from (1) to (9). 0010 () () () () to () for the production of hydrogen synthesis gas, characterized in that oxygen is steamed.
- a fuel cell system comprising: a fuel cell using hydrogen produced by (1) as a fuel provided in any of the deviations (1) to (5).
- FIG. 11 is an abbreviated diagram of a clear battery stem.
- the element contains copper
- It contains metal oleite having a structure, preferably further containing anana, 8 and a portion of earth element.
- a metal having a spine structure is a metal mold.
- It has a surface-shaped cube found in things. It is usually a divalent genus and is a genus of.
- metal materials containing copper are used, and examples of metal materials include C-type spines, Ce-type spines, and CC-type spines.
- the C-type spin is preferred.
- An example of the C-type spin is C
- an example of the Ce-type spin is C.
- Examples of the C C type sp include C C.
- the metal structure containing copper is superior to the spine structure containing copper in that it has excellent thermal properties, and when used as a raw material, has a high unit surface area.
- a soluble ngan salt such as ngan is used as a solubilizing material such as copper, and a solution containing these so that a substantial proportion thereof, that is, a ratio to C is substantially 2.
- a tonic agent such as oxalic acid
- this powder is heat-treated and the powder obtained by decomposing nitric acid etc. in the powder is about 3-5 degrees in air at a temperature of 3-5 degrees Celsius.
- C is obtained by further increasing the temperature by 5 to 5 degrees C. Also over 7 C
- the obtained metal compound becomes a compound with copper acid (C or C 2 O or a compound thereof).
- a soluble material such as iron may be used instead of the gun source.
- a metal material composed of C (e) can be obtained.
- Olite contains oleite.
- Olite includes ZS5, Denite, X-type, Mold, Mold, Mold,, Light, etc., and Denite ZS5 is preferred for durability, and ZS5 is particularly preferred.
- Denite ZS 5 is preferably a type that is completely or partially converted to a proton rather than a cation in terms of sex.
- it is from mass to 2 and more preferably from 2 to 5 with C-type spiolite.
- Olite is more preferable than this because the smallness decreases and the number of causes causing the increase increases.
- It can be prepared by the following method. In other words, after mixing the powder of the metal product containing copper and the oleite powder to the quality, it is molded into an appropriate size, or the material of the product containing copper.
- a clear preparation can be made by, for example, a method of mixing an appropriate size orite of an appropriate size.
- a V 0 X misaligned crystal form can be used. It is also possible to use baked anana such as Itoialite Gisite. In addition to this, you can add 8 ⁇ degree of aka to the aum to create a sinking thing. You can also use it. Also, aum soppod and other a are dissolved in 2 puno and other a, and an acid is prepared by adding water as a water splitting. I can do it.
- Ana content is 5 to 5, preferably 8 to 4 and more preferably to 3 for a mixture of oleite and anana of copper. By having 5 to 5 ana, it is possible to obtain the results of the control without significantly reducing the activity.
- anana may be performed simultaneously with the addition of neolite containing copper, or may be added before or after the addition of neolite containing copper.
- Examples of 8 contained in 0020 oleite include metals such as platinum and radium, iron, iron and iron.
- Examples of the metal include platinum, radium, um, and diadium, with platinum being particularly preferred.
- platinum products are P C 4 2PC6 P (0.05
- gold compounds may be used alone or in combination of two or more. The same is true for the radiium, um, dium and iridium below.
- radium examples include (
- Methods such as immersion, sp, and ion exchange methods such as ing, ing, and ncpen weness methods can be used, but impregnation and ion exchange methods using ing, ncpen weness methods are preferred.
- the 8 minutes outside the noble metals contained in 00223 olite include e Co.
- the compound used as a material for the eCo component is not particularly limited but is preferably a soluble one, and an acid salt is generally used.
- Olite's e N Co law is not particularly limited.
- a method such as addition from the oleite period can also be employed.
- ion exchange method described below The addition of the Olite period by law is preferred.
- the abundance of e N Co is 5 to 2 or more to orite. By adding 5 to 2 olite, it is possible to obtain additional results.
- sodium for adjusting the amount of sodium can be added, and further, an accelerator such as sodium can be added.
- anatomium, aum, active anna, and ana can be used, and anatomium, anoum, etc. are particularly preferred.
- Acac can be supplied together with glass, idka, etc., or anana, etc., and examples thereof include sodium hydroxide, water hydroxide, etc. In particular, it is preferable to use sodium hydroxide.
- the agent is an organic substance. 2 3 Nnotanoan Nopnoan diguante tetrapiumum Tetrathianum and these amnesium ditin diananopun are used, especially diguantetrapium Is preferred.
- the S 2 2 3 ratio is ⁇ 3, preferably 2 ⁇ . If it does not progress further than this, the sex is bad and the sex is bad. Also, (M is e N Co.) The ratio is 5 ⁇ 2, preferably ⁇ . If this is not the case, it will be less effective.
- Gd b o is mentioned. These earth elements are not particularly limited. If the solubility is methanotanolytic, acid salts are generally used.
- the solution of the minute can be the methanotano solution or at the same time.
- the earth's part is ⁇ 2 is preferred. -By setting ⁇ 2, the effect of rare earth elements can be obtained economically advantageously. In fact, the activity can be further improved by the above.
- a gas phase method that uses an air stream containing hydrogen and a wet method that uses a base material.
- the normal air flow is 5 to 5 C, preferably 2 to 3 C, and preferably 3 to 24, and preferably between. Gases such as nitrogen, um, and ann coexist outside the gas.
- the following are the origins of chan- nes that use an aa a ana, enkese that use a methiae, etc.
- a method of treating with a reducing agent such as horn or hydrazine. In this case, it is usually from room temperature to C, up to 24, preferably 3 to.
- the catalyst is restored to the reaction by the generated hydrogen by flowing the reaction material.
- hydrogen synthesis gas is produced by using () steam, (2), (3) part (4) for elements such as metite.
- the ratio of water vapor methite is theoretically 3 when producing elemental gas, but 3 to 6 degrees is preferred. On the other hand, when producing synthesis gas, the ratio of water vapor methite is theoretically Is preferred, but 2 degrees is preferred.
- the temperature is 2 C, preferably 25 to 45 C. If the temperature is 2 C, there is a risk that the ratio of metite will be low, and if it exceeds 5, it will cause a problem.
- the MET range is preferred to OO range.
- the production rate of GS is low in OO, which is not practically preferable. If it exceeds OO, the rate of metite is too low, and it is not preferable in practical use.
- the reaction is usually from normal to Pa degrees. If this force is too high, the ratio of metite tends to decrease.
- the reaction of methenite and water vapor occurs in the same actor or in successive actors.
- the reaction between hydrogen production and synthetic gas production will be slight, but in general, the oxygen methylate ratio is preferably selected in the range of ⁇ , and the steam methylate ratio is preferably 5. It is selected in the range of ⁇ 3. If the metite ratio is •, the reaction due to exotherm may not be sufficiently supplied, and if the ratio exceeds 1, the completeness may occur and the element concentration may decrease. In addition, when the water vapor ratio is -5, the hydrogen concentration may decrease, while when it exceeds 3, there is a risk that the supply of heat will be insufficient.
- the GS force is the same as that of the steam.
- the ratio of oxygen metite is selected within the range of 3 to 5.
- the rate of metitete may be sufficiently high, while when it exceeds • 5, completeness occurs and causes a decrease in the hydrogen concentration.
- the G S force is the same as that of the steam.
- the ratio of CO metite is preferably 8-2, more preferably 9-9. ⁇ Selected within 5. If the ratio of CO metite is -8, the ratio of metite may be sufficiently high, while if the ratio exceeds 2, it will cause a large amount of C to be produced, resulting in a decrease in hydrogen. May be necessary and is preferred. In this reaction, water vapor can be introduced, and the hydrogen concentration can be increased by this introduction. The reactivity and G S force are the same as in the case of steam.
- the present invention has a fuel cell system characterized by having a fuel cell using hydrogen produced by the above-described preparation as described above.
- fuel desulfurization 23 in tank 2. Normally, it is not contained when using methyte suitable as oxygen, but desulfurization is effective when it contains a compound.
- 23 can be filled with, for example, sex charcoal, oleite or metal agents.
- the pump 24 is mixed with water from the tank desulfurized in 23, it is introduced into the gas, vaporized, and sent to 3. 3 is filled as described above, and the compounds (elements and water vapor) sent to 3 are The raw material is produced by the steam reaction described above.
- the degree is reduced to the extent that it does not affect the performance of the fuel cell.
- 32 includes cum-based or noble metals, and the converter 33 includes um-based, platinum or those. If the degree of hydrogen in the hydrogen produced is low, 32 may not be installed.
- the 037 battery 34 is an example of a polymer electrolyte battery having a polymer electrolyte 34C between the negative electrode 34 and the positive electrode 34.
- the hydrogen switch obtained by the above method is inserted into the positive electrode, and the air sent from the air 35 is inserted into the positive electrode if necessary.
- Hydrogen can be used as fuel, with the third na 3 connected to the 0038 34 side.
- an air separation 36 is connected to the positive electrode 34 side, and water and exhaust gas generated by the combination of hydrogen and air in the air supplied to the positive electrode 34 side are separated, and the water is used for the formation of water vapor. be able to.
- the battery 34 generates heat as it generates power.
- 37 can be attached to recover this heat for effective use.
- 37 is a heat exchanger attached to the fuel cell 34, an exchanger 37 for exchanging heat from the exchanger 37 with water, a cooling 37C, and these exchangers 37 37 37C.
- the water obtained in the heat exchanger 37 can be used effectively in other facilities.
- the catalyst SAP 8 (eCo) and earth (a Ce S) were measured by the following method using a CP optical spectroscopic analyzer.
- Sample 9 is taken in an analytical pot and heat-treated at 9 C for 6 hours. Then, the sample is taken into a ten () vessel and oxalic acid 4 is added. Next, add, and add 0, 2 of OOO as a watch cover, and adjust the volume to 5. Quantify P in this solution by CP. Add the same solution as above to P and measure. 3.Rare earth in ZS5 and 8 (eCo) method
- SPS type 5 which is a multi-element CP optical spectroscopic analyzer specified in CPJ 6, is used.
- the quasi G S (gas space) was 9; the gas (O) quasi G S was 54; Also, implementation, 3, 4-36 and
- the rate is the numerical value indicated by from the reaction gas.
- the reaction rate is 333 for GS (gas space) of the 5th class, 2 for GS (gas space), 2 for the gas (O) level, and 25C for the reaction.
- the time required to fall below 9 5 was defined as the interval.
- implementations 3 to 4 7 2 2 24 and 3 are steam 5 ⁇ O, quasi GS (gas space) 333, gas (O) quasi GS 2, reaction 28 C for 4 It was rated by later activity (after 4 minutes) and the above king ().
- C 2 ZS 5 2 was prepared by mixing 3 2) 5 with.
- the results of the obtained and the durability values are shown in Table.
- the C-neutral material is mixed with Olite such as ZS 5 denite, which has higher vapority than the C-Neana mixture, and the conventional C system
- Table 2 also shows the results of performing durability in the same way as in implementations 0 to 3. ⁇ 3 From implementation 3, C It is confirmed that the addition of the chemical compound and the ZS 5ana is less active and the kin rate is also reduced.
- ZS 5 (S) was obtained.
- the obtained ZS 5 (S) was subjected to 3 element reduction with 5 C before mixing with C ne.
- the liquid obtained by mixing 26 8 (98 ⁇ 9) and 25 ton was designated as.
- the liquid obtained by mixing glass (S 3 SO 29 a 9 ⁇ 4 6 ⁇ 6) 5 6 manufactured by this chemical industry was used.
- C was a liquid obtained by mixing 99 ⁇ 5 aC 4 2 (684) 2 tons manufactured by Sodium Industries. While stirring this liquid C, the above and liquids were combined in C at the same time. To this compound, add 97 2 (9, 8) manufactured by Sangyo Co., Ltd., and adjust to g ⁇ 5. 2 The mixture is cooled to warm and solid
- ZS 5 (S A g) was subjected to hydrogen reduction treatment at 5 C for 3 hours before mixing with C ne.
- the CP confirmed that it was SO 2 2 3 35 • 9, Co 9 •.
- Example 3 results of activity and endurance value in Example 3 are also shown in Table 3. From this, it is confirmed that the addition of C nitride and ZS 5 suppresses the formation and further improves the durability. 075 24 (C 5a ZS 5 (
Abstract
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JP2006545021A JPWO2006054527A1 (en) | 2004-11-16 | 2005-11-14 | Oxygen-containing hydrocarbon reforming catalyst, hydrogen or synthesis gas production method using the same, and fuel cell system |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008068242A (en) * | 2006-09-15 | 2008-03-27 | Toshiba Corp | Hydrogen making catalyst, hydrogen making apparatus and hydrogen making method |
CN101808736A (en) * | 2007-02-21 | 2010-08-18 | 国立大学法人大分大学 | Catalyst for the production of hydrogen at low temperature, process for production of the catalyst, and process for production of hydrogen |
US11090640B2 (en) | 2016-10-17 | 2021-08-17 | Sabic Global Technologies B.V. | Process for producing BTX from a C5—C12 hydrocarbon mixture |
WO2023199557A1 (en) * | 2022-04-15 | 2023-10-19 | 古河電気工業株式会社 | Catalyst for liquefied petroleum gas synthesis, and method for producing liquefied petroleum gas |
Citations (1)
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JP2003320254A (en) * | 2002-05-01 | 2003-11-11 | National Institute Of Advanced Industrial & Technology | Catalyst for water gas shift reaction and steam reforming reaction of methanol |
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2005
- 2005-11-14 JP JP2006545021A patent/JPWO2006054527A1/en not_active Withdrawn
- 2005-11-14 WO PCT/JP2005/020871 patent/WO2006054527A1/en active Application Filing
- 2005-11-14 KR KR1020077010991A patent/KR20070084220A/en not_active Application Discontinuation
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JP2003320254A (en) * | 2002-05-01 | 2003-11-11 | National Institute Of Advanced Industrial & Technology | Catalyst for water gas shift reaction and steam reforming reaction of methanol |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008068242A (en) * | 2006-09-15 | 2008-03-27 | Toshiba Corp | Hydrogen making catalyst, hydrogen making apparatus and hydrogen making method |
CN101808736A (en) * | 2007-02-21 | 2010-08-18 | 国立大学法人大分大学 | Catalyst for the production of hydrogen at low temperature, process for production of the catalyst, and process for production of hydrogen |
US11090640B2 (en) | 2016-10-17 | 2021-08-17 | Sabic Global Technologies B.V. | Process for producing BTX from a C5—C12 hydrocarbon mixture |
WO2023199557A1 (en) * | 2022-04-15 | 2023-10-19 | 古河電気工業株式会社 | Catalyst for liquefied petroleum gas synthesis, and method for producing liquefied petroleum gas |
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JPWO2006054527A1 (en) | 2008-05-29 |
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