WO2018219986A1 - Procédé d'hydrogénation de dioxyde de carbone en présence d'un catalyseur contenant de l'iridium et/ou du rhodium - Google Patents
Procédé d'hydrogénation de dioxyde de carbone en présence d'un catalyseur contenant de l'iridium et/ou du rhodium Download PDFInfo
- Publication number
- WO2018219986A1 WO2018219986A1 PCT/EP2018/064142 EP2018064142W WO2018219986A1 WO 2018219986 A1 WO2018219986 A1 WO 2018219986A1 EP 2018064142 W EP2018064142 W EP 2018064142W WO 2018219986 A1 WO2018219986 A1 WO 2018219986A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- range
- catalyst
- iridium
- rhodium
- carbon dioxide
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 115
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims abstract description 82
- 238000000034 method Methods 0.000 title claims abstract description 69
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims abstract description 44
- 239000001569 carbon dioxide Substances 0.000 title claims abstract description 40
- 239000010948 rhodium Substances 0.000 title claims abstract description 37
- 229910052703 rhodium Inorganic materials 0.000 title claims abstract description 34
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 title claims abstract description 32
- 238000005984 hydrogenation reaction Methods 0.000 title claims abstract description 22
- 239000000203 mixture Substances 0.000 claims abstract description 32
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 20
- 239000001257 hydrogen Substances 0.000 claims abstract description 20
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 17
- 239000007789 gas Substances 0.000 claims description 45
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 39
- 229910052741 iridium Inorganic materials 0.000 claims description 36
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 claims description 33
- 239000000463 material Substances 0.000 claims description 19
- 229910052746 lanthanum Inorganic materials 0.000 claims description 13
- 229910052684 Cerium Inorganic materials 0.000 claims description 12
- MCMNRKCIXSYSNV-UHFFFAOYSA-N ZrO2 Inorganic materials O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims description 12
- 230000015572 biosynthetic process Effects 0.000 claims description 10
- 238000003786 synthesis reaction Methods 0.000 claims description 10
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 claims description 9
- 239000000376 reactant Substances 0.000 claims description 9
- 150000004645 aluminates Chemical class 0.000 claims description 8
- 239000002245 particle Substances 0.000 claims description 8
- 229910052727 yttrium Inorganic materials 0.000 claims description 8
- 229910052749 magnesium Inorganic materials 0.000 claims description 7
- 229910052726 zirconium Inorganic materials 0.000 claims description 7
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 6
- 229910052791 calcium Inorganic materials 0.000 claims description 6
- VWQVUPCCIRVNHF-UHFFFAOYSA-N yttrium atom Chemical compound [Y] VWQVUPCCIRVNHF-UHFFFAOYSA-N 0.000 claims description 6
- 229910052782 aluminium Inorganic materials 0.000 claims description 5
- 229910052712 strontium Inorganic materials 0.000 claims description 5
- 229910052719 titanium Inorganic materials 0.000 claims description 5
- 239000010936 titanium Substances 0.000 claims description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- GWXLDORMOJMVQZ-UHFFFAOYSA-N cerium Chemical compound [Ce] GWXLDORMOJMVQZ-UHFFFAOYSA-N 0.000 claims description 4
- 229910052566 spinel group Inorganic materials 0.000 claims description 4
- 229910052788 barium Inorganic materials 0.000 claims description 3
- 150000002431 hydrogen Chemical class 0.000 claims description 3
- FZLIPJUXYLNCLC-UHFFFAOYSA-N lanthanum atom Chemical compound [La] FZLIPJUXYLNCLC-UHFFFAOYSA-N 0.000 claims description 3
- 229910052710 silicon Inorganic materials 0.000 claims description 3
- 239000000377 silicon dioxide Substances 0.000 claims description 2
- 239000004408 titanium dioxide Substances 0.000 claims description 2
- 235000012239 silicon dioxide Nutrition 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- 239000000243 solution Substances 0.000 description 13
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 11
- 229910002091 carbon monoxide Inorganic materials 0.000 description 11
- 238000002360 preparation method Methods 0.000 description 11
- 238000001035 drying Methods 0.000 description 10
- 238000005470 impregnation Methods 0.000 description 10
- 238000004519 manufacturing process Methods 0.000 description 10
- 238000001354 calcination Methods 0.000 description 9
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 9
- 229910052751 metal Inorganic materials 0.000 description 9
- 239000002184 metal Substances 0.000 description 9
- 230000003197 catalytic effect Effects 0.000 description 8
- 238000011068 loading method Methods 0.000 description 8
- 229910000510 noble metal Inorganic materials 0.000 description 8
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 8
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 7
- 239000000571 coke Substances 0.000 description 7
- 239000011777 magnesium Substances 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 5
- 239000012876 carrier material Substances 0.000 description 5
- 230000008021 deposition Effects 0.000 description 5
- 239000000395 magnesium oxide Substances 0.000 description 5
- 239000011572 manganese Substances 0.000 description 5
- 238000000465 moulding Methods 0.000 description 5
- 229910052697 platinum Inorganic materials 0.000 description 5
- 238000001556 precipitation Methods 0.000 description 5
- 229910052742 iron Inorganic materials 0.000 description 4
- 229910052748 manganese Inorganic materials 0.000 description 4
- 229910052763 palladium Inorganic materials 0.000 description 4
- 238000012216 screening Methods 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 150000001768 cations Chemical class 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 229910052759 nickel Inorganic materials 0.000 description 3
- 238000002407 reforming Methods 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- 229910052721 tungsten Inorganic materials 0.000 description 3
- 229910052725 zinc Inorganic materials 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 description 2
- 229910052692 Dysprosium Inorganic materials 0.000 description 2
- 229910052691 Erbium Inorganic materials 0.000 description 2
- 229910052693 Europium Inorganic materials 0.000 description 2
- 229910052688 Gadolinium Inorganic materials 0.000 description 2
- 229910052689 Holmium Inorganic materials 0.000 description 2
- 229910052779 Neodymium Inorganic materials 0.000 description 2
- 229910052777 Praseodymium Inorganic materials 0.000 description 2
- 229910052772 Samarium Inorganic materials 0.000 description 2
- 229910052771 Terbium Inorganic materials 0.000 description 2
- 229910052775 Thulium Inorganic materials 0.000 description 2
- 229910052769 Ytterbium Inorganic materials 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 238000004364 calculation method Methods 0.000 description 2
- 229910052804 chromium Inorganic materials 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000002178 crystalline material Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000002223 garnet Substances 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 229910052735 hafnium Inorganic materials 0.000 description 2
- 229910052738 indium Inorganic materials 0.000 description 2
- 150000001247 metal acetylides Chemical class 0.000 description 2
- 229910052750 molybdenum Inorganic materials 0.000 description 2
- 229910052758 niobium Inorganic materials 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- 229910052573 porcelain Inorganic materials 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000011949 solid catalyst Substances 0.000 description 2
- 230000007306 turnover Effects 0.000 description 2
- 229910052720 vanadium Inorganic materials 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- KLZUFWVZNOTSEM-UHFFFAOYSA-K Aluminium flouride Chemical compound F[Al](F)F KLZUFWVZNOTSEM-UHFFFAOYSA-K 0.000 description 1
- 238000004438 BET method Methods 0.000 description 1
- 229910015999 BaAl Inorganic materials 0.000 description 1
- 229910003320 CeOx Inorganic materials 0.000 description 1
- 229910052765 Lutetium Inorganic materials 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 229910020068 MgAl Inorganic materials 0.000 description 1
- 229910003668 SrAl Inorganic materials 0.000 description 1
- 229910010413 TiO 2 Inorganic materials 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000002453 autothermal reforming Methods 0.000 description 1
- 235000012216 bentonite Nutrition 0.000 description 1
- 229910052790 beryllium Inorganic materials 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910052792 caesium Inorganic materials 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 229910000420 cerium oxide Inorganic materials 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- RKTYLMNFRDHKIL-UHFFFAOYSA-N copper;5,10,15,20-tetraphenylporphyrin-22,24-diide Chemical compound [Cu+2].C1=CC(C(=C2C=CC([N-]2)=C(C=2C=CC=CC=2)C=2C=CC(N=2)=C(C=2C=CC=CC=2)C2=CC=C3[N-]2)C=2C=CC=CC=2)=NC1=C3C1=CC=CC=C1 RKTYLMNFRDHKIL-UHFFFAOYSA-N 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000007210 heterogeneous catalysis Methods 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 description 1
- 229910052745 lead Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- AMWRITDGCCNYAT-UHFFFAOYSA-L manganese oxide Inorganic materials [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229910052762 osmium Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 229910052702 rhenium Inorganic materials 0.000 description 1
- 229910052701 rubidium Inorganic materials 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 229910052706 scandium Inorganic materials 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000000629 steam reforming Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229910052715 tantalum Inorganic materials 0.000 description 1
- 229910052716 thallium Inorganic materials 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- RUDFQVOCFDJEEF-UHFFFAOYSA-N yttrium(III) oxide Inorganic materials [O-2].[O-2].[O-2].[Y+3].[Y+3] RUDFQVOCFDJEEF-UHFFFAOYSA-N 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
- XLOMVQKBTHCTTD-UHFFFAOYSA-N zinc oxide Inorganic materials [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/40—Carbon monoxide
-
- 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
- B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
- B01J21/04—Alumina
-
- 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
- B01J21/066—Zirconium or hafnium; Oxides or hydroxides thereof
-
- 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
- B01J21/10—Magnesium; Oxides or hydroxides thereof
-
- 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
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
-
- 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
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/42—Platinum
-
- 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
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/44—Palladium
-
- 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
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/56—Platinum group metals
- B01J23/58—Platinum group metals with alkali- or alkaline earth metals
-
- 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
- B01J23/70—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
- B01J23/83—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 rare earths or actinides
-
- 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
- B01J35/613—10-100 m2/g
-
- 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
- C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
- C01B3/12—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide
- C01B3/16—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide using catalysts
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
- C10G2/50—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon dioxide with hydrogen
-
- 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
- C01B2203/1082—Composition of support materials
-
- 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
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
-
- 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
-
- 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 invention relates to a process for the hydrogenation of carbon dioxide, which is characterized in that carbon dioxide is reacted with hydrogen in the presence of a catalyst comprising an iridium- and / or rhodium-containing active material.
- a catalyst comprising an iridium- and / or rhodium-containing active material.
- RWGS reverse water gas shift
- JP 3328847 B2 describes the use of rhodium-containing catalysts for the methanation, i. Hydrogenation of carbon dioxide with hydrogen to methane, described at temperatures of 200 to 550 ° C.
- WO 2015/091310 A1 discloses the use of iridium-containing catalysts for the dry reforming of mixtures of hydrocarbons and carbon dioxide to synthesis gas.
- Synthesis gas is to be understood as meaning a gas mixture containing hydrogen and carbon monoxide, which can be used as a basic chemical in a large number of industrial processes. Depending on their use, synthesis gases have different ratios of hydrogen to carbon monoxide.
- C02 emissions in Germany in 2010 amounted to approx. 960 million t C02 equivalent, with the chemical industry contributing around 5%.
- Suitable basic chemicals are, for example, hydrogen and synthesis gas. The latter forms the ideal interface to existing petrochemical processes for production of eg methanol, dimethyl ether or Fischer-Tropsch products.
- the global demand for hydrogen and syngas is currently 50 million t / a, or 220 million t / a.
- WO2015 / 135968 discloses catalysts based on Ni, Co, Zn, Fe mixed oxides.
- noble metal-containing catalysts for the hydrogenation of carbon dioxide to carbon monoxide are described in US Pat. No. 8,961,829 B2.
- a catalyst is disclosed in which platinum has been deposited on cerium, manganese and / or magnesium oxide. In the examples, a Pt loading of 0.3 wt .-% is given.
- US 201 1/0105630 discloses platinum or palladium based catalysts for the hydrogenation of carbon dioxide to carbon monoxide.
- Potential support materials include alumina, magnesia, silica, titania, optionally sulfated zirconia, tungsten zirconia, aluminum trifluoride, fluorinated alumina, bentonites, zeolites, carbon-based supports, molecular sieves, and combinations thereof.
- the stated preferred loading is 10 to 20 wt .-%.
- WO 2013/135710 discloses a carbon dioxide hydrogenation to carbon monoxide in a shell and tube reactor.
- the catalyst disclosed are hexaaluminates having the following formula:
- L Na, K, Rb, Cs, Mg, Ca, Sr, Ba, Sc, Y, Sn, Pb, Mn, In, Tl, La, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb and / or Lu
- M Ti, Zr, Hf, V, Nb, Ta, Cr, Mo, W, Mn, Re, Fe, Ru, Os, Co, Rh, Ir, Ni, Pd, Pt, Zn, Cu, Ag and / or Au.
- the method of preparation of these solid hexaaluminate catalysts involves a multi-step process involving the steps of precipitation, filtration, washing, drying, molding and calcining. Examples of carbon dioxide hydrogenation are not disclosed.
- WO 2015/135968 discloses a process for preparing a catalyst for high temperature carbon dioxide hydrogenation to carbon monoxide.
- the disclosed catalyst contains at least one crystalline material comprising yttrium and aluminum, wherein it is characteristic of the crystalline material that it has at least one of the following structures: cubic garnet structure, orthhombic perovskite structure, hexagonal perovskite structure and / or monoclinic perovskite structure (ie Y4AI209), wherein the catalyst contains Cu, Fe, Co, Zn and / or Ni.
- the loading of the yttrium-containing material is 0.1 to 10 mol .-% indicate.
- the examples show good performance in carbon dioxide hydrogenation, as well as low carbon deposition on the catalyst.
- the experiments were carried out at a GHSV of 30,000 and 40,000 r 1 .
- the method of preparation of these catalysts comprises a multistage process comprising the stages, precipitation, filtration, drying, pre-calcination, molding, post-
- One of the objects underlying the invention is to provide a catalyst for carbon dioxide hydrogenation with high activity and stability, i. good resistance to coke buildup. Furthermore, the tendency to methanation should be low.
- this catalyst is inexpensive to produce, i. a manufacturing method can be selected that includes as few process steps.
- a supported catalyst can be prepared with the aid of the process steps impregnation, drying, calcination, whereby a period of typically V2 hours is estimated for impregnation on a laboratory scale.
- a full-body catalyst requires the process steps of precipitation, filtration, washing, drying / calcination, molding and (post) calcination, with half a working day being estimated for a laboratory scale precipitation.
- the active metal loading should be as low as possible to be energy efficient and resource efficient.
- a further object is also that the process according to the invention is suitable for the carbon dioxide hydrogenation to carbon monoxide in the presence of hydrocarbons, in particular methane, i. that methane present in the educt gas mixture is reformed.
- Another object within the scope of the invention is to identify particularly active catalysts which, even at high loads, in particular greater than 10,000 h-1, are still able to convert a reactant gas mixture into a composition close to the thermodynamically predicted equilibrium lies.
- Particularly active catalysts make it possible to make the reactor smaller and thus keep the investment for this part of the plant small.
- high temperature process is meant processes at temperatures of> 600 ° C, in particular> 600 ° C and ⁇ 1400 ° C.
- the invention relates to a process for carbon dioxide hydrogenation, which is characterized in that carbon dioxide is reacted with hydrogen in the presence of a catalyst, wherein the catalyst comprises a support material and an active composition, wherein as support materials Ce, La, Zr, Al, Ti, Ca, Si, Mg oxides, SiC, MgAI spinels, Sr aluminates, La , Ba, Sr-hexa-aluminates and / or mixtures thereof, and the active composition contains at least iridium and / or rhodium as active component, wherein the content of iridium (calculated as metal) with respect to the total weight of the catalyst is in a range of 0.005 to 2 wt .-% and the content of rhodium (calculated as metal) relative to the total weight of the catalyst in a range of 0.005 to ⁇ 1 wt .-% and the temperature of the educt gases, carbon dioxide with Hydrogen, when contacted with the active composition in the range of 600 to 1
- Carbon dioxide is preferably reacted with hydrogen in the presence of a catalyst to give carbon monoxide and water.
- the content of rhodium in relation to the total weight of the catalyst is in a range of preferably 0.005 to 0.75 wt.%, More preferably 0.01 to 0.75 wt.%, In particular 0.025 to 0, 75% by weight.
- the content of iridium is in a range of preferably 0.005 to 1.5% by weight, more preferably 0.01 to 1% by weight, more preferably 0.01 to ⁇ 1% by weight, based on the total weight of the catalyst .-%, more preferably 0.01 to 0.75 wt .-%, in particular 0.025 to 0.75 wt .-%. All mixtures of iridium and rhodium known to the person skilled in the art are conceivable. Particularly preferred is iridium.
- the total content of a mixture of iridium and rhodium in relation to the total weight of the catalyst is in a range of preferably 0.005 to 2% by weight, preferably 0.005 to 1.5% by weight, more preferably 0.01 to 1% by weight %, more preferably 0.01 to ⁇ 1 wt .-%, more preferably 0.01 to 0.75 wt .-%, in particular 0.025 to 0.75 wt .-%.
- oxides As support materials, oxides, aluminates and carbides are preferred. Examples of oxides which may be mentioned as oxides are Ce, La, Zr, Al, Ti, Ca, Si, Mg oxides and mixtures thereof, carbides SiC and aluminates spinels, in particular MgAl spinels, Sr aluminates and La, Ba, Sr 2. Hexa-aluminates.
- the following support materials are preferred: Ce, La, Zr, Al-oxides, Zr-hydroxides doped with La & Ce, Al 2 O 3 (delta-theta), SiC, Y on ZrO 2, Ce on ZrO 2, Ca-Si-ZrO 2, 35% MgO 65% Al 2 O 3, 80% MgO 20% Al 2 O 3, 37% CaO, 63% Al 2 O 3, ZrO 2 (monoclinic), ZrO 2 (tetragonal), 44.6% CaO 54.9% ZnO, TiO 2, MgO, SrAl 2 O 4, BaAl 2 O 4, La 2 Zr 2 O 7.
- the content of doping elements is advantageously in the range from 0 to 5 wt .-%, in particular 1 to 3 wt .-%, with respect to the carrier material.
- the zirconium dioxide-containing active composition has a specific surface area of> 5 m 2 / g, preferably> 20 m 2 / g, more preferably> 50 m 2 / g and in particular> 80 m 2 / g.
- the determination of specific surface area of the catalyst was achieved by gas adsorption by the BET method (ISO 9277: 1995).
- the iridium and / or rhodium it is particularly advantageous for the iridium and / or rhodium to be present in finely divided form on the carrier, in particular zirconium dioxide carrier, since this achieves high catalytic activity with a low content of Ir and / or Rh.
- the iridium-containing and / or rhodium-containing particles have a size ⁇ 50 nm, preferably ⁇ 30 nm, preferably ⁇ 20 nm and more preferably ⁇ 10 nm.
- the iridium-containing and / or rhodium-containing particles have a size in the range from 1 to 100 nm, preferably in the range from 5 to 50 nm.
- the iridium and / or rhodium is homogeneously on the carrier or in the active mass.
- the iridium and / or rhodium is particularly preferably present in homogeneous and finely divided form on the carrier or in the active composition.
- the catalyst used according to the invention is characterized in that the Ir and / or Rh on a carrier, advantageously a zirkoni umdioxid Anlagenn carrier, is present and this doped with further elements.
- a carrier advantageously a zirkoni umdioxid ambiencen carrier
- elements from the group of rare earths ie from the group Sc, Y, La, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu.
- the catalyst also contains one or more doping elements in addition to the iridium and / or rhodium and optionally zirconium dioxide, then the proportion by weight of doping elements, in particular rare earth doping elements, based on the total weight of the catalyst is in the range from 0.01 to 80 Wt .-%, preferably in the range of 0.1 to 50 wt .-% and particularly preferably in the range of 1, 0 to 30 wt .-%.
- the catalyst used according to the invention is characterized in that it contains iridium and / or rhodium and a support material, advantageously zirconium dioxide, yttrium as a further doping element, wherein the yttrium is present in oxidic form.
- a support material advantageously zirconium dioxide, yttrium as a further doping element, wherein the yttrium is present in oxidic form.
- the yttria content based on the total weight of the catalyst, in the range of 0.01 to 80 wt .-%, preferably from 0.1 to 50 wt .-% and more preferably from 1, 0 to 30 wt .-% ,
- the catalyst used according to the invention is characterized in that, in addition to iridium and / or rhodium and a support material, preferably zirconium dioxide, additionally contains one or more, preferably two, elements from the group of rare earths as doping elements.
- the content is preferably to doping elements with respect to the total weight of the catalyst, in the range of 0.01-80 wt.%, preferably 0.1-50 wt.%, and more preferably 1-30 wt.%. Particular preference is given to using lanthanum (La) and cerium (Ce) as doping elements.
- catalysts used according to the invention which comprise Ir / ZrO 2 and / or Rh / ZrC 2 active compositions in which the zirconium dioxide has a doping with yttrium and / or a doping with lanthanum and / or cerium.
- the active compounds used according to the invention which are used for the process according to the invention also contain promoters and / or further metal cations, which further increase the efficiency of the catalysts.
- doping elements may include, but are not limited to: noble metal promoters, non-noble metal promoters, and other metal cations:
- the catalyst used according to the invention or the active composition contains at least one noble metal-containing promoter from the group Pt, Pd, Ru, Au, where the proportion of noble metal-containing promoters in relation to the total weight of the catalyst is 0.01. 5 wt .-% and more preferably in the range of 0.1 to 3 wt .-% have.
- the catalyst used according to the invention comprises at least one non-noble metal-containing promoter from the group Ni, Co, Fe, Mn, Mo, W, the fraction of non-noble metal-containing promoters being in the range from 0.1 to 50 based on the total weight of the catalyst Wt .-%, preferably in the range of 0.5 to 30 wt .-% and more preferably in the range 1-20 wt .-% is.
- the catalyst used according to the invention also comprises a proportion of further metal cations, which are preferably selected from the group Mg, Ca, Sr, Ba, Ga, Be, Cr, Mn, with Ca and / or Mg being particularly preferred.
- the components present in the catalyst used in the present invention i. the said noble metals, alkaline earth metals, doping elements, promoters and support materials can be present in elemental and / or oxidic form.
- examples being impregnation with impregnating solution, impregnation with pore volume, spraying of the impregnating solution, washcoating and precipitation powdery raw materials can be carried out by methods known to those skilled in the art, such as tableting, aggregation or extrusion, as described, inter alia, in the Handbook of Heterogenous Catalysis, Vol. 1, VCH Verlagsgesellschaft Weinheim, 1997, pp. 414-417.
- the iridium-containing and / or rhodium-containing active composition may also be applied to a carrier, monolith or honeycomb body.
- the monolith or honeycomb body may be made of metal or ceramic.
- the molding of the active composition or the application of the active composition on a carrier or carrier bodies is of great industrial significance for the fields of application of the catalyst used according to the invention.
- the shape of the particles affect the pressure drop caused by the fixed catalyst bed. Impression may be carried out by any method known to those skilled in the art of catalyst preparation (see, eg, Deutschmann, O., Knözinger, H., Kochloefl, K. and Turek, T. 201. 1. Heterogeneous Catalysis and Solid Catalysts, 2. Development and Types of Solid Catalysts, Ullmann's Encyclopedia of Industrial Chemistry).
- the present invention further relates to a catalytic process for the carbon dioxide hydrogenation to carbon monoxide, i. for the production of synthesis gas, characterized in that:
- the pressure of the reactant gas in contacting with the catalyst is in the range of 1 to 100 bar a bs and the temperature of the educt gas in contacting with the catalyst is in the range of 20 to 1400 ° C,
- the GHSV of the process has a value in the range of 1,000 to 1,000,000 r 1 ,
- the synthesis gas produced has a H 2 / CO ratio in the range of 0.1 to 10, more preferably in the range of 1 to 4, and most preferably in the range of 1, 5 to 3.
- the molar ratio of educt gas H2 / CO 2 in the range from 0.1 to 20, preferably from 0.3 to 10, more preferably from 1 to 7, in particular from 2 to 5, is advantageous.
- the educt gas has the following composition:
- the molar fraction of CO 2 is advantageously in the range from 1 to 90%, preferably from 3 to 75%, more preferably from 10 to 60%, in particular from 20 to 50%.
- the molar fraction of H 2 is advantageously in the range from 1 to 99%, preferably from 10 to 90%, more preferably from 20 to 85%, in particular from 40 to 80%.
- the molar fraction of CH4 is advantageously in the range from 0 to 30%, preferably from 0 to 20%, more preferably 0 to 15%, more preferably 0 to 10%, in particular from 0 to 5%.
- the molar fraction of N 2 is advantageously in the range from 0 to 80%, preferably from 0 to 20%, in particular from 0 to 5%.
- the molar fraction of O 2 is advantageously in the range from 0 to 5%, preferably from 0 to 2%, more preferably from 0 to 1%, in particular from 0 to 0.5%.
- the molar fraction of H 2 O is advantageously in the range from 0 to 99%, preferably from 0 to 90%, more preferably from 0 to 40%, more preferably 0 to 20%, further preferably 0 to 15%, further preferably 0 to 10%, in particular 0 to 5%.
- the pressure of the educt gas when contacting with the catalyst is advantageously in the range from 3 to 60 bar a bs, in particular from 10 to 30 bar a bs.
- the temperature of the educt gas when it comes into contact with the catalyst is in the range from 600 to 1300 ° C., preferably from 750 to 1200 ° C., in particular from 850 to 1200 ° C.
- the GHSV of the process is in the range from 2000 to 700,000 hr.sup.- 1 , preferably from 5000 to 500,000 hr.sup.- 1 , in particular from 10,000 to 300,000 hr.sup.- 1 .
- the process according to the invention can be advantageously used as an ATR process (autothermal reforming), such as, for example, in Reimert, et al. , 201 1. Gas Production, 2. Processes. Ullmann's Encyclopedia of Industrial Chemistry. described be performed.
- ATR process oxygen is thus introduced in addition to the educt gas.
- a characteristic of the process according to the invention for the hydrogenation of carbon dioxide, if appropriate in the presence of hydrocarbons, advantageously methane, and / or water, is that ZrO 2 -containing active compositions can be used which have a relatively low content of iridium and / or rhodium and nevertheless one have high catalytic efficiency.
- active compositions which, for example, have only 1% by weight or less than 1% by weight of iridium and / or rhodium.
- the process according to the invention can be carried out with a reactant fluid which has small amounts of water vapor.
- the water vapor / carbon dioxide content in the educt gas is less than 0.2, more preferably less than 0.1, and even more preferably less than 0.05.
- the iridium-containing and / or rhodium-containing active component is exposed to a strong physical and chemical load, since the process is carried out at a temperature in the range of 600 to 1300 "C, the process pressure in the range of 5 to 500 bar , preferably in the range of 10 to 250 bar, and more preferably in the range of 20 to 100.
- the coke deposit is ⁇ 2 wt .-% carbon content with respect to the catalyst used, more preferably ⁇ 1 wt .-%, more preferably ⁇ 0.5 wt .-%, in particular ⁇ 0.2 wt .-%. Due to the very high thermal stability and the operational stability under pressure at pressures of 5 to 40 bar of the catalyst this can be used over long process times, several thousand hours away.
- the corresponding amount of Sr (N 0.3) 2 (4.344 g with a purity of 99.7% by weight) was dissolved in 250 ml DI water with stirring in a 500 ml beaker.
- a dispersion of the AI source (15.462 g Disperal with 42.51 wt% AI) was added to this solution, whereupon a suspension has formed. This suspension was stirred for 30 minutes for homogenization.
- the suspension was flash frozen dropwise in liquid nitrogen. The frozen droplets were freeze-dried at -10 C and 2.56 mbar.
- the freeze-dried powder was calcined in air to decompose the nitrates and chlorides.
- the heating rate was 1 K / min.
- the sample was heated to 150 C, 250 C and 350 C with a residence time of 1 hour at the temperature reached.
- the final calcination temperature was 450 C and the residence time was again 1 hour, then cooled to ambient temperature.
- the precalcined sample was subjected to a molding process. 3% by weight of graphite was added to the sample and mixed thoroughly. The mixture was pelletized with a Korsch XP1 pelletizer in automatic mode. The direction finding tool had a diameter of 13 mm and the applied force for picking up pellets with a height of 2 mm was 40 kN. The pellets were crushed and sieved to 315-500 pm.
- the crushed and sieved sample (315-500 pm) was subjected to final calcination in air to remove the graphite and to form the desired hexaaluminate phase.
- the final calcination temperature was 1400 C with a heating rate of 5 K / min and a residence time of 2 hours.
- W015135968 Catalyst S2 was prepared as described in WO 15/135968 A1.
- the catalysts S3 and S4 were prepared analogously to the prior art, US 201 1/0105630, via impregnation process:
- the dried sample was calcined in air (6 l / min) in an oven (Nabertherm TH120 / 12) as follows: heating rate of 1 K / min up to a temperature of 250 ° C, residence time of 1 h, heating rate of 5 K / min up to a temperature of 400 C, residence time of 4 h, then cool to ambient temperature.
- the drying took place in a drying oven at 80 C for 16 hours.
- the dried sample was calcined as follows under air (6 I / min) in a furnace (Nabertherm TH120 / 12): heating rate of 1 K / min up to a temperature of 250 0 C, residence time of 1 hour, heating rate of 5K / min up to a temperature of 400 0 C, residence time of 4h, then cool to ambient temperature.
- Table III List of carrier materials used
- Table IV List of impregnating solutions used Table V summarizes the catalysts used according to the invention.
- Table V List of Ir and Rh catalysts used in the invention
- the determination of the loss on ignition (LOI) is a crucial point in the production of impregnated catalysts with a well-defined metal loading.
- the carrier used had an LOI of 2.43%.
- the impregnation was carried out as 100% incipient wetness impregnation (100% ICW) (moistening impregnation) using a solution of DI water with a 0.199 molar IrC solution.
- Table 2 Summary of hydrogen conversion, carbon dioxide conversion, and methane yield (without methane in the educt gas) or methane conversion (methane in educt gas) of the catalysts S1-S4 (prior art), E1-E6 (according to the invention) of the phase I - VI of the table 1
- the catalysts used in the invention show a comparable performance as the full catalysts S1 and S2 from the prior art. Furthermore, the performance is stable over all phases.
- the activity of prior art catalysts S3 and S4 decreases from phase V and phase VI, respectively; Furthermore, the conversion of H2 in phases I and II, in which no methane is added, worse than S1 and S2 and E1 -E6.
- Table 3 Carbon deposition from the catalysts after the screening according to Table 5 (indicator of stability)
- Table 7 Summary of hydrogen conversion, carbon dioxide conversion, and methane yield (without methane in the educt gas) or methane conversion (methane in educt gas) of the catalysts E4 (0.5% by weight Ir), E5 (0.05% by weight Ir) and E7 ( 0.1% by weight Ir) of phase I-XI II of Table 6
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Inorganic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Catalysts (AREA)
Abstract
L'invention concerne un procédé d'hydrogénation de dioxyde de carbone, caractérisé en ce qu'il consiste à faire réagir du dioxyde de carbone avec de l'hydrogène en présence d'un catalyseur qui contient une matière active à base d'iridium et/ou de rhodium.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP17174175 | 2017-06-02 | ||
EP17174175.4 | 2017-06-02 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2018219986A1 true WO2018219986A1 (fr) | 2018-12-06 |
Family
ID=59152626
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2018/064142 WO2018219986A1 (fr) | 2017-06-02 | 2018-05-30 | Procédé d'hydrogénation de dioxyde de carbone en présence d'un catalyseur contenant de l'iridium et/ou du rhodium |
Country Status (2)
Country | Link |
---|---|
TW (1) | TW201902818A (fr) |
WO (1) | WO2018219986A1 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11964872B2 (en) | 2018-12-03 | 2024-04-23 | Shell Usa, Inc. | Process and reactor for converting carbon dioxide into carbon monoxide |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3328847B2 (ja) | 1992-11-09 | 2002-09-30 | 株式会社日立製作所 | 水素化用触媒とその製造方法及び水素化方法 |
US20110105630A1 (en) | 2009-11-04 | 2011-05-05 | The Government Of The United States Of America, As Represented By The Secretary Of The Navy | Catalytic Support for use in Carbon Dioxide Hydrogenation Reactions |
WO2013135710A2 (fr) | 2012-03-13 | 2013-09-19 | Bayer Intellectual Property Gmbh | Procédé pour la réalisation d'une réaction rwgs dans un réacteur à faisceau tubulaire |
US8961829B2 (en) | 2007-04-27 | 2015-02-24 | Saudi Basic Industries Corporation | Catalytic hyrogenation of carbon dioxide into syngas mixture |
WO2015091310A1 (fr) | 2013-12-20 | 2015-06-25 | Basf Se | Procédé de reformage de mélanges d'hydrocarbures et de dioxyde de carbone |
WO2015135968A1 (fr) | 2014-03-14 | 2015-09-17 | Basf Se | Catalyseur contenant de l'yttrium pour l'hydrogénation du dioxyde de carbone à haute température, l'hydrogénation du dioxyde de carbone à haute température et le reformage combinés et/ou le reformage ainsi qu'un procédé d'hydrogénation du dioxyde de carbone à haute température, d'hydrogénation du dioxyde de carbone à haute température et de reformage combinés et/ou de reformage |
US20150336795A1 (en) * | 2012-12-21 | 2015-11-26 | Basf Se | Parallel preparation of hydrogen, carbon monoxide and a carbon-comprising product |
-
2018
- 2018-05-30 WO PCT/EP2018/064142 patent/WO2018219986A1/fr active Application Filing
- 2018-05-31 TW TW107118702A patent/TW201902818A/zh unknown
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3328847B2 (ja) | 1992-11-09 | 2002-09-30 | 株式会社日立製作所 | 水素化用触媒とその製造方法及び水素化方法 |
US8961829B2 (en) | 2007-04-27 | 2015-02-24 | Saudi Basic Industries Corporation | Catalytic hyrogenation of carbon dioxide into syngas mixture |
US20110105630A1 (en) | 2009-11-04 | 2011-05-05 | The Government Of The United States Of America, As Represented By The Secretary Of The Navy | Catalytic Support for use in Carbon Dioxide Hydrogenation Reactions |
WO2013135710A2 (fr) | 2012-03-13 | 2013-09-19 | Bayer Intellectual Property Gmbh | Procédé pour la réalisation d'une réaction rwgs dans un réacteur à faisceau tubulaire |
US20150336795A1 (en) * | 2012-12-21 | 2015-11-26 | Basf Se | Parallel preparation of hydrogen, carbon monoxide and a carbon-comprising product |
WO2015091310A1 (fr) | 2013-12-20 | 2015-06-25 | Basf Se | Procédé de reformage de mélanges d'hydrocarbures et de dioxyde de carbone |
US20160311684A1 (en) * | 2013-12-20 | 2016-10-27 | Basf Se | Method for reforming mixtures of hydrocarbons and carbondioxide |
WO2015135968A1 (fr) | 2014-03-14 | 2015-09-17 | Basf Se | Catalyseur contenant de l'yttrium pour l'hydrogénation du dioxyde de carbone à haute température, l'hydrogénation du dioxyde de carbone à haute température et le reformage combinés et/ou le reformage ainsi qu'un procédé d'hydrogénation du dioxyde de carbone à haute température, d'hydrogénation du dioxyde de carbone à haute température et de reformage combinés et/ou de reformage |
Non-Patent Citations (7)
Title |
---|
"Handbook of Heterogeneous Catalysis", vol. 1, 1997, VCH VERLAGSGESELLSCHAFT, pages: 414 - 417 |
A. BANSODE; A. URAKAWA, J. CATAL., vol. 309, 2014, pages 66 - 70 |
BOGDAN V I ET AL: "Reduction of carbon dioxide by hydrogen on metal-carbon catalysts under supercritical conditions", RUSSIAN JOURNAL OF PHYSICAL CHEMISTRY A, CHEMICAL SOCIETY, LONDON, GB, vol. 90, no. 12, 6 November 2016 (2016-11-06), pages 2352 - 2357, XP036092287, ISSN: 0036-0244, [retrieved on 20161106], DOI: 10.1134/S0036024416120050 * |
DEUTSCHMANN, O.; KNÖZINGER, H.; KOCHLOEFL, K.; TUREK, T.: "Ullmann's Encyclopedia of Industrial Chemistry", 2011, article "Heterogeneous Catalysis and Solid Catalysts, 2. Development and Types of Solid Catalysts" |
HABER ET AL.: "Manual of methods and procedures for catalyst characterization", PURE & APPL. CHEM., vol. 67, no. 8/9, 1995, pages 1257 - 1306 |
J. GRACIANI; K. MUDIYANSELAGE; F. XU; A.E. BABER; J. EVANS; S.D. SENANAYAKE; D.J. STACCHIOLA; P. LIU; J. HRBEK; J. FERNANDEZ SANZ, SCIENCE, vol. 345, 2014, pages 546 - 550 |
REIMERT ET AL.: "Ullmann's Encyclopedia of Industrial Chemistry", 2011, article "Gas Production, 2. Processes" |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11964872B2 (en) | 2018-12-03 | 2024-04-23 | Shell Usa, Inc. | Process and reactor for converting carbon dioxide into carbon monoxide |
Also Published As
Publication number | Publication date |
---|---|
TW201902818A (zh) | 2019-01-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP3116826B1 (fr) | Catalysezr contenant de l'yttrium pour la hydrogenation de dioxid de carbone, hydrogenation de dioxid de carbone a haute temperature et/ou reformage et procede pour la hydrogenation de dioxid de carbone et/ou reformage | |
JP7219474B2 (ja) | 複合酸化物、金属担持物及びアンモニア合成触媒 | |
US9475037B2 (en) | Nickel hexaaluminate-containing catalyst for reforming hydrocarbons in the presence of carbon dioxide | |
EP2033943B1 (fr) | Catalyseur pour la méthanation de monoxyde de carbone, procédé de préparation du catalyseur et procédé de méthanation | |
WO2015091310A1 (fr) | Procédé de reformage de mélanges d'hydrocarbures et de dioxyde de carbone | |
WO2013118078A1 (fr) | Catalyseur contenant de l'hexaaluminate pour le reformage d'hydrocarbures et procédé de reformage | |
JP7464738B2 (ja) | アンモニア分解触媒 | |
US10987660B2 (en) | Hexaaluminate-comprising catalyst for the reforming of hydrocarbons and a reforming process | |
JP2021130100A (ja) | アンモニア分解触媒 | |
EP2866930A1 (fr) | Procédé haute pression permettant de soumettre des hydrocarbure à un reformage au dioxyde de carbone réalisé en présence de matière actives contenant de l'iridium | |
KR101437072B1 (ko) | 효율적인 이산화탄소 전환 촉매 및 이의 제조 방법 | |
DE2420945A1 (de) | Katalysator fuer die umsetzung von dampf mit kohlenwasserstoffen | |
WO2018219986A1 (fr) | Procédé d'hydrogénation de dioxyde de carbone en présence d'un catalyseur contenant de l'iridium et/ou du rhodium | |
Squire et al. | In situ X-ray diffraction study of lanthanum oxide catalysts during the oxidative coupling of methane | |
CN103796949A (zh) | 在绝热反应级联中使用氧化铈催化剂制备氯气的方法 | |
Dongmei et al. | Steam reforming of dimethyl ether over coupled catalysts of CuO-ZnO-Al2O3-ZrO2 and solid-acid catalyst | |
WO2000016900A1 (fr) | Catalyseurs et procede de reformage a la vapeur d'hydrocarbures | |
WO2018219992A1 (fr) | Procédé d'hydrogénation de dioxyde de carbone en présence d'un catalyseur contenant du nickel et des spinelles de magnésium | |
KR102346850B1 (ko) | 삼산화황의 전환 및 수소 생산 방법을 위한 촉매 조성물 | |
Soisuwan et al. | Characteristics and catalytic properties of alumina–zirconia mixed oxides prepared by a modified Pechini method | |
JPH0371174B2 (fr) | ||
Bracciale et al. | Steam reforming of model compounds from biomass fermentation over nanometric ruthenium modified nickel-lanthanum perovskites catalysts | |
KR101950928B1 (ko) | 알코올 합성용 촉매, 이의 제조방법 및 그의 용도 | |
Perez-Luna et al. | Study of alumina-promoted SO 2-4/NiO/ZrO 2 catalyst performance | |
CN117751014A (zh) | 用于重质烃进料的蒸汽重整催化剂 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 18726177 Country of ref document: EP Kind code of ref document: A1 |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
122 | Ep: pct application non-entry in european phase |
Ref document number: 18726177 Country of ref document: EP Kind code of ref document: A1 |