JP5761814B2 - 石油留分の水素化転化のための触媒組成物を調製する方法 - Google Patents
石油留分の水素化転化のための触媒組成物を調製する方法 Download PDFInfo
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- JP5761814B2 JP5761814B2 JP2012236731A JP2012236731A JP5761814B2 JP 5761814 B2 JP5761814 B2 JP 5761814B2 JP 2012236731 A JP2012236731 A JP 2012236731A JP 2012236731 A JP2012236731 A JP 2012236731A JP 5761814 B2 JP5761814 B2 JP 5761814B2
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- Prior art keywords
- metal
- catalyst
- catalyst composition
- molybdenum
- nickel
- Prior art date
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- 239000003054 catalyst Substances 0.000 title claims description 200
- 239000000203 mixture Substances 0.000 title claims description 112
- 239000003208 petroleum Substances 0.000 title description 14
- 238000004519 manufacturing process Methods 0.000 title description 5
- 229910052751 metal Inorganic materials 0.000 claims description 96
- 239000002184 metal Substances 0.000 claims description 96
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 74
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 43
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 43
- 239000011230 binding agent Substances 0.000 claims description 43
- 229910052799 carbon Inorganic materials 0.000 claims description 42
- 229910052750 molybdenum Inorganic materials 0.000 claims description 41
- 239000011733 molybdenum Substances 0.000 claims description 41
- 229910052759 nickel Inorganic materials 0.000 claims description 35
- 150000002430 hydrocarbons Chemical class 0.000 claims description 33
- 229930195733 hydrocarbon Natural products 0.000 claims description 32
- 229910017052 cobalt Inorganic materials 0.000 claims description 28
- 239000010941 cobalt Substances 0.000 claims description 28
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 28
- 229910000510 noble metal Inorganic materials 0.000 claims description 24
- 239000004215 Carbon black (E152) Substances 0.000 claims description 19
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 claims description 18
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims description 18
- 229910052721 tungsten Inorganic materials 0.000 claims description 16
- 239000010937 tungsten Substances 0.000 claims description 16
- 238000002441 X-ray diffraction Methods 0.000 claims description 11
- KYYSIVCCYWZZLR-UHFFFAOYSA-N cobalt(2+);dioxido(dioxo)molybdenum Chemical compound [Co+2].[O-][Mo]([O-])(=O)=O KYYSIVCCYWZZLR-UHFFFAOYSA-N 0.000 claims description 7
- 229910052976 metal sulfide Inorganic materials 0.000 claims description 7
- 229910052809 inorganic oxide Inorganic materials 0.000 claims description 6
- 239000004005 microsphere Substances 0.000 claims description 6
- MEFBJEMVZONFCJ-UHFFFAOYSA-N molybdate Chemical compound [O-][Mo]([O-])(=O)=O MEFBJEMVZONFCJ-UHFFFAOYSA-N 0.000 claims description 4
- XMWRBQBLMFGWIX-UHFFFAOYSA-N C60 fullerene Chemical compound C12=C3C(C4=C56)=C7C8=C5C5=C9C%10=C6C6=C4C1=C1C4=C6C6=C%10C%10=C9C9=C%11C5=C8C5=C8C7=C3C3=C7C2=C1C1=C2C4=C6C4=C%10C6=C9C9=C%11C5=C5C8=C3C3=C7C1=C1C2=C4C6=C2C9=C5C3=C12 XMWRBQBLMFGWIX-UHFFFAOYSA-N 0.000 claims description 3
- QXZUUHYBWMWJHK-UHFFFAOYSA-N [Co].[Ni] Chemical compound [Co].[Ni] QXZUUHYBWMWJHK-UHFFFAOYSA-N 0.000 claims description 3
- 229910003472 fullerene Inorganic materials 0.000 claims description 2
- PBYZMCDFOULPGH-UHFFFAOYSA-N tungstate Chemical compound [O-][W]([O-])(=O)=O PBYZMCDFOULPGH-UHFFFAOYSA-N 0.000 claims 2
- OMAWWKIPXLIPDE-UHFFFAOYSA-N (ethyldiselanyl)ethane Chemical compound CC[Se][Se]CC OMAWWKIPXLIPDE-UHFFFAOYSA-N 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 description 80
- 238000000034 method Methods 0.000 description 77
- 239000000463 material Substances 0.000 description 76
- IYYZUPMFVPLQIF-UHFFFAOYSA-N dibenzothiophene Chemical compound C1=CC=C2C3=CC=CC=C3SC2=C1 IYYZUPMFVPLQIF-UHFFFAOYSA-N 0.000 description 52
- 239000012071 phase Substances 0.000 description 46
- 239000000243 solution Substances 0.000 description 41
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 36
- 150000003839 salts Chemical class 0.000 description 36
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N diphenyl Chemical compound C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 34
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 31
- 239000002243 precursor Substances 0.000 description 31
- 239000004094 surface-active agent Substances 0.000 description 31
- 150000002894 organic compounds Chemical class 0.000 description 29
- 230000008569 process Effects 0.000 description 27
- 239000011593 sulfur Substances 0.000 description 27
- 229910052717 sulfur Inorganic materials 0.000 description 27
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 26
- 239000001257 hydrogen Substances 0.000 description 24
- 229910052739 hydrogen Inorganic materials 0.000 description 24
- 238000005984 hydrogenation reaction Methods 0.000 description 24
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 22
- 239000012298 atmosphere Substances 0.000 description 22
- 238000010438 heat treatment Methods 0.000 description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 21
- 230000003197 catalytic effect Effects 0.000 description 20
- 230000000694 effects Effects 0.000 description 19
- WVIIMZNLDWSIRH-UHFFFAOYSA-N cyclohexylcyclohexane Chemical group C1CCCCC1C1CCCCC1 WVIIMZNLDWSIRH-UHFFFAOYSA-N 0.000 description 18
- 229910052757 nitrogen Inorganic materials 0.000 description 18
- MVRPPTGLVPEMPI-UHFFFAOYSA-N 2-cyclohexylphenol Chemical compound OC1=CC=CC=C1C1CCCCC1 MVRPPTGLVPEMPI-UHFFFAOYSA-N 0.000 description 17
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 17
- 239000004305 biphenyl Substances 0.000 description 17
- 235000010290 biphenyl Nutrition 0.000 description 17
- 239000000047 product Substances 0.000 description 17
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 15
- -1 alumina Chemical class 0.000 description 15
- 239000011148 porous material Substances 0.000 description 15
- 238000005486 sulfidation Methods 0.000 description 15
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 14
- 239000007789 gas Substances 0.000 description 14
- 230000015572 biosynthetic process Effects 0.000 description 13
- 239000002798 polar solvent Substances 0.000 description 13
- 238000002360 preparation method Methods 0.000 description 13
- 239000013078 crystal Substances 0.000 description 12
- WQOXQRCZOLPYPM-UHFFFAOYSA-N dimethyl disulfide Chemical compound CSSC WQOXQRCZOLPYPM-UHFFFAOYSA-N 0.000 description 12
- 150000002739 metals Chemical class 0.000 description 12
- 239000002244 precipitate Substances 0.000 description 12
- 239000000843 powder Substances 0.000 description 11
- 239000002904 solvent Substances 0.000 description 11
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 10
- 239000007833 carbon precursor Substances 0.000 description 10
- 238000002425 crystallisation Methods 0.000 description 10
- 230000008025 crystallization Effects 0.000 description 10
- 238000011156 evaluation Methods 0.000 description 10
- 239000002245 particle Substances 0.000 description 10
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 9
- LZZYPRNAOMGNLH-UHFFFAOYSA-M Cetrimonium bromide Chemical compound [Br-].CCCCCCCCCCCCCCCC[N+](C)(C)C LZZYPRNAOMGNLH-UHFFFAOYSA-M 0.000 description 9
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 9
- 125000000217 alkyl group Chemical group 0.000 description 9
- 230000000052 comparative effect Effects 0.000 description 9
- 230000003647 oxidation Effects 0.000 description 9
- 238000007254 oxidation reaction Methods 0.000 description 9
- 238000005987 sulfurization reaction Methods 0.000 description 9
- 238000003786 synthesis reaction Methods 0.000 description 9
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 8
- 238000001704 evaporation Methods 0.000 description 8
- 239000000446 fuel Substances 0.000 description 8
- DCAYPVUWAIABOU-UHFFFAOYSA-N hexadecane Chemical compound CCCCCCCCCCCCCCCC DCAYPVUWAIABOU-UHFFFAOYSA-N 0.000 description 8
- 238000002156 mixing Methods 0.000 description 8
- 239000007787 solid Substances 0.000 description 8
- QGAVSDVURUSLQK-UHFFFAOYSA-N ammonium heptamolybdate Chemical compound N.N.N.N.N.N.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.[Mo].[Mo].[Mo].[Mo].[Mo].[Mo].[Mo] QGAVSDVURUSLQK-UHFFFAOYSA-N 0.000 description 7
- 125000003118 aryl group Chemical group 0.000 description 7
- 238000009835 boiling Methods 0.000 description 7
- NLPVCCRZRNXTLT-UHFFFAOYSA-N dioxido(dioxo)molybdenum;nickel(2+) Chemical compound [Ni+2].[O-][Mo]([O-])(=O)=O NLPVCCRZRNXTLT-UHFFFAOYSA-N 0.000 description 7
- 230000008020 evaporation Effects 0.000 description 7
- 230000003993 interaction Effects 0.000 description 7
- 229910052742 iron Inorganic materials 0.000 description 7
- 239000000377 silicon dioxide Substances 0.000 description 7
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 239000000908 ammonium hydroxide Substances 0.000 description 6
- 239000002585 base Substances 0.000 description 6
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 6
- 239000010410 layer Substances 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- CWQXQMHSOZUFJS-UHFFFAOYSA-N molybdenum disulfide Chemical compound S=[Mo]=S CWQXQMHSOZUFJS-UHFFFAOYSA-N 0.000 description 6
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 description 6
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 5
- 238000001354 calcination Methods 0.000 description 5
- 230000008859 change Effects 0.000 description 5
- 238000013329 compounding Methods 0.000 description 5
- 238000000354 decomposition reaction Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 5
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 description 5
- 239000011261 inert gas Substances 0.000 description 5
- 229910052982 molybdenum disulfide Inorganic materials 0.000 description 5
- 230000007935 neutral effect Effects 0.000 description 5
- 239000003921 oil Substances 0.000 description 5
- 239000008188 pellet Substances 0.000 description 5
- 238000001556 precipitation Methods 0.000 description 5
- 239000011541 reaction mixture Substances 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 4
- 229910002651 NO3 Inorganic materials 0.000 description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- YTPLMLYBLZKORZ-UHFFFAOYSA-N Thiophene Chemical compound C=1C=CSC=1 YTPLMLYBLZKORZ-UHFFFAOYSA-N 0.000 description 4
- YRKCREAYFQTBPV-UHFFFAOYSA-N acetylacetone Chemical compound CC(=O)CC(C)=O YRKCREAYFQTBPV-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 229910021529 ammonia Inorganic materials 0.000 description 4
- 150000001450 anions Chemical class 0.000 description 4
- 229910052786 argon Inorganic materials 0.000 description 4
- 229910001593 boehmite Inorganic materials 0.000 description 4
- UFMZWBIQTDUYBN-UHFFFAOYSA-N cobalt dinitrate Chemical compound [Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O UFMZWBIQTDUYBN-UHFFFAOYSA-N 0.000 description 4
- 229910001981 cobalt nitrate Inorganic materials 0.000 description 4
- ZKKLPDLKUGTPME-UHFFFAOYSA-N diazanium;bis(sulfanylidene)molybdenum;sulfanide Chemical compound [NH4+].[NH4+].[SH-].[SH-].S=[Mo]=S ZKKLPDLKUGTPME-UHFFFAOYSA-N 0.000 description 4
- 238000004090 dissolution Methods 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 239000001307 helium Substances 0.000 description 4
- 229910052734 helium Inorganic materials 0.000 description 4
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 4
- NHNBFGGVMKEFGY-UHFFFAOYSA-N nitrate group Chemical group [N+](=O)([O-])[O-] NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 4
- 238000001179 sorption measurement Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 3
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 3
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 description 3
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 3
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 3
- 239000001099 ammonium carbonate Substances 0.000 description 3
- 235000012501 ammonium carbonate Nutrition 0.000 description 3
- APUPEJJSWDHEBO-UHFFFAOYSA-P ammonium molybdate Chemical compound [NH4+].[NH4+].[O-][Mo]([O-])(=O)=O APUPEJJSWDHEBO-UHFFFAOYSA-P 0.000 description 3
- 239000011609 ammonium molybdate Substances 0.000 description 3
- 229940010552 ammonium molybdate Drugs 0.000 description 3
- 235000018660 ammonium molybdate Nutrition 0.000 description 3
- 239000003945 anionic surfactant Substances 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000005540 biological transmission Effects 0.000 description 3
- 239000003093 cationic surfactant Substances 0.000 description 3
- 229910052804 chromium Inorganic materials 0.000 description 3
- 239000011651 chromium Substances 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 239000008367 deionised water Substances 0.000 description 3
- 229910021641 deionized water Inorganic materials 0.000 description 3
- 238000006477 desulfuration reaction Methods 0.000 description 3
- 230000023556 desulfurization Effects 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 238000009472 formulation Methods 0.000 description 3
- 238000010348 incorporation Methods 0.000 description 3
- 239000002563 ionic surfactant Substances 0.000 description 3
- 238000001000 micrograph Methods 0.000 description 3
- VLAPMBHFAWRUQP-UHFFFAOYSA-L molybdic acid Chemical compound O[Mo](O)(=O)=O VLAPMBHFAWRUQP-UHFFFAOYSA-L 0.000 description 3
- 239000002121 nanofiber Substances 0.000 description 3
- 229910017604 nitric acid Inorganic materials 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 230000000737 periodic effect Effects 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 238000000197 pyrolysis Methods 0.000 description 3
- 239000010453 quartz Substances 0.000 description 3
- 150000003242 quaternary ammonium salts Chemical class 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 150000004763 sulfides Chemical class 0.000 description 3
- 150000003464 sulfur compounds Chemical class 0.000 description 3
- CMPGARWFYBADJI-UHFFFAOYSA-L tungstic acid Chemical compound O[W](O)(=O)=O CMPGARWFYBADJI-UHFFFAOYSA-L 0.000 description 3
- POILWHVDKZOXJZ-ARJAWSKDSA-M (z)-4-oxopent-2-en-2-olate Chemical compound C\C([O-])=C\C(C)=O POILWHVDKZOXJZ-ARJAWSKDSA-M 0.000 description 2
- FCEHBMOGCRZNNI-UHFFFAOYSA-N 1-benzothiophene Chemical compound C1=CC=C2SC=CC2=C1 FCEHBMOGCRZNNI-UHFFFAOYSA-N 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-N Acrylic acid Chemical compound OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 2
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 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 2
- 229910021586 Nickel(II) chloride Inorganic materials 0.000 description 2
- XRTZIUVKXTTYRJ-UHFFFAOYSA-N O(O)O.[Mo].[Ni] Chemical compound O(O)O.[Mo].[Ni] XRTZIUVKXTTYRJ-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- QZYDAIMOJUSSFT-UHFFFAOYSA-N [Co].[Ni].[Mo] Chemical compound [Co].[Ni].[Mo] QZYDAIMOJUSSFT-UHFFFAOYSA-N 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 150000003863 ammonium salts Chemical class 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000003637 basic solution Substances 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 238000003763 carbonization Methods 0.000 description 2
- 125000002091 cationic group Chemical group 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- GVPFVAHMJGGAJG-UHFFFAOYSA-L cobalt dichloride Chemical compound [Cl-].[Cl-].[Co+2] GVPFVAHMJGGAJG-UHFFFAOYSA-L 0.000 description 2
- WHDPTDWLEKQKKX-UHFFFAOYSA-N cobalt molybdenum Chemical compound [Co].[Co].[Mo] WHDPTDWLEKQKKX-UHFFFAOYSA-N 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000002803 fossil fuel Substances 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 150000004679 hydroxides Chemical class 0.000 description 2
- 238000005470 impregnation Methods 0.000 description 2
- 238000011065 in-situ storage Methods 0.000 description 2
- 239000012263 liquid product Substances 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- 150000007522 mineralic acids Chemical class 0.000 description 2
- DDTIGTPWGISMKL-UHFFFAOYSA-N molybdenum nickel Chemical compound [Ni].[Mo] DDTIGTPWGISMKL-UHFFFAOYSA-N 0.000 description 2
- JKQOBWVOAYFWKG-UHFFFAOYSA-N molybdenum trioxide Chemical compound O=[Mo](=O)=O JKQOBWVOAYFWKG-UHFFFAOYSA-N 0.000 description 2
- 239000012452 mother liquor Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000002105 nanoparticle Substances 0.000 description 2
- 239000002055 nanoplate Substances 0.000 description 2
- QMMRZOWCJAIUJA-UHFFFAOYSA-L nickel dichloride Chemical compound Cl[Ni]Cl QMMRZOWCJAIUJA-UHFFFAOYSA-L 0.000 description 2
- 150000002823 nitrates Chemical class 0.000 description 2
- 150000007524 organic acids Chemical class 0.000 description 2
- 229930195734 saturated hydrocarbon Natural products 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011343 solid material Substances 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 229930192474 thiophene Natural products 0.000 description 2
- ZNOKGRXACCSDPY-UHFFFAOYSA-N tungsten trioxide Chemical compound O=[W](=O)=O ZNOKGRXACCSDPY-UHFFFAOYSA-N 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- UPPLJLAHMKABPR-UHFFFAOYSA-H 2-hydroxypropane-1,2,3-tricarboxylate;nickel(2+) Chemical compound [Ni+2].[Ni+2].[Ni+2].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O.[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O UPPLJLAHMKABPR-UHFFFAOYSA-H 0.000 description 1
- 238000004438 BET method Methods 0.000 description 1
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical group [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- KSGUUTWSWMLVHG-UHFFFAOYSA-N N.OOO Chemical compound N.OOO KSGUUTWSWMLVHG-UHFFFAOYSA-N 0.000 description 1
- MOTAPKWZJXGFIS-UHFFFAOYSA-N O(O)O.[Mo].[Ni].[Co] Chemical compound O(O)O.[Mo].[Ni].[Co] MOTAPKWZJXGFIS-UHFFFAOYSA-N 0.000 description 1
- NGGMJFQQECICSP-UHFFFAOYSA-N OOO.N.[Ni+2] Chemical compound OOO.N.[Ni+2] NGGMJFQQECICSP-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- YCOASTWZYJGKEK-UHFFFAOYSA-N [Co].[Ni].[W] Chemical compound [Co].[Ni].[W] YCOASTWZYJGKEK-UHFFFAOYSA-N 0.000 description 1
- LZUGDZHBFGHVOW-UHFFFAOYSA-N [Mo].[Ni].[W].[Cr].[Co] Chemical compound [Mo].[Ni].[W].[Cr].[Co] LZUGDZHBFGHVOW-UHFFFAOYSA-N 0.000 description 1
- RAFNAMHEPCFDRC-UHFFFAOYSA-N [W].[Mo].[Co].[Ni] Chemical compound [W].[Mo].[Co].[Ni] RAFNAMHEPCFDRC-UHFFFAOYSA-N 0.000 description 1
- 150000001242 acetic acid derivatives Chemical class 0.000 description 1
- MQRWBMAEBQOWAF-UHFFFAOYSA-N acetic acid;nickel Chemical compound [Ni].CC(O)=O.CC(O)=O MQRWBMAEBQOWAF-UHFFFAOYSA-N 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- VXAUWWUXCIMFIM-UHFFFAOYSA-M aluminum;oxygen(2-);hydroxide Chemical compound [OH-].[O-2].[Al+3] VXAUWWUXCIMFIM-UHFFFAOYSA-M 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 229910003481 amorphous carbon Inorganic materials 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 229910001680 bayerite Inorganic materials 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 1
- 239000004327 boric acid Substances 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Chemical group BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 1
- 229910052794 bromium Chemical group 0.000 description 1
- QGJOPFRUJISHPQ-NJFSPNSNSA-N carbon disulfide-14c Chemical compound S=[14C]=S QGJOPFRUJISHPQ-NJFSPNSNSA-N 0.000 description 1
- 238000004523 catalytic cracking Methods 0.000 description 1
- 238000004517 catalytic hydrocracking Methods 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000013522 chelant Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 238000000975 co-precipitation Methods 0.000 description 1
- 150000001868 cobalt Chemical class 0.000 description 1
- 229940011182 cobalt acetate Drugs 0.000 description 1
- SCNCIXKLOBXDQB-UHFFFAOYSA-K cobalt(3+);2-hydroxypropane-1,2,3-tricarboxylate Chemical compound [Co+3].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O SCNCIXKLOBXDQB-UHFFFAOYSA-K 0.000 description 1
- QAHREYKOYSIQPH-UHFFFAOYSA-L cobalt(II) acetate Chemical compound [Co+2].CC([O-])=O.CC([O-])=O QAHREYKOYSIQPH-UHFFFAOYSA-L 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000004320 controlled atmosphere Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 230000014509 gene expression Effects 0.000 description 1
- 229910001679 gibbsite Inorganic materials 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 150000002334 glycols Chemical class 0.000 description 1
- 229910021472 group 8 element Inorganic materials 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 238000010335 hydrothermal treatment Methods 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 239000003446 ligand Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 229910021518 metal oxyhydroxide Inorganic materials 0.000 description 1
- 238000000386 microscopy Methods 0.000 description 1
- 150000002751 molybdenum Chemical class 0.000 description 1
- 150000002815 nickel Chemical class 0.000 description 1
- XIKYYQJBTPYKSG-UHFFFAOYSA-N nickel Chemical compound [Ni].[Ni] XIKYYQJBTPYKSG-UHFFFAOYSA-N 0.000 description 1
- 229940078494 nickel acetate Drugs 0.000 description 1
- MOWMLACGTDMJRV-UHFFFAOYSA-N nickel tungsten Chemical compound [Ni].[W] MOWMLACGTDMJRV-UHFFFAOYSA-N 0.000 description 1
- 229910000008 nickel(II) carbonate Inorganic materials 0.000 description 1
- ZULUUIKRFGGGTL-UHFFFAOYSA-L nickel(ii) carbonate Chemical compound [Ni+2].[O-]C([O-])=O ZULUUIKRFGGGTL-UHFFFAOYSA-L 0.000 description 1
- BFDHFSHZJLFAMC-UHFFFAOYSA-L nickel(ii) hydroxide Chemical compound [OH-].[OH-].[Ni+2] BFDHFSHZJLFAMC-UHFFFAOYSA-L 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 238000010943 off-gassing Methods 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 239000006259 organic additive Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 125000002524 organometallic group Chemical group 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 238000005839 oxidative dehydrogenation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000004376 petroleum reforming Methods 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 239000005077 polysulfide Substances 0.000 description 1
- 229920001021 polysulfide Polymers 0.000 description 1
- 150000008117 polysulfides Polymers 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 238000011002 quantification Methods 0.000 description 1
- 125000001453 quaternary ammonium group Chemical group 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- CVHZOJJKTDOEJC-UHFFFAOYSA-N saccharin Chemical compound C1=CC=C2C(=O)NS(=O)(=O)C2=C1 CVHZOJJKTDOEJC-UHFFFAOYSA-N 0.000 description 1
- 229940081974 saccharin Drugs 0.000 description 1
- 235000019204 saccharin Nutrition 0.000 description 1
- 239000000901 saccharin and its Na,K and Ca salt Substances 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 125000000446 sulfanediyl group Chemical group *S* 0.000 description 1
- 230000019635 sulfation Effects 0.000 description 1
- 238000005670 sulfation reaction Methods 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 238000007669 thermal treatment Methods 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 238000004627 transmission electron microscopy Methods 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Classifications
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- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/02—Sulfur, selenium or tellurium; Compounds thereof
- B01J27/04—Sulfides
- B01J27/047—Sulfides with chromium, molybdenum, tungsten or polonium
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- B01J27/0515—Molybdenum with iron group metals or platinum group metals
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- 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
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- 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
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- 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
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- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
- B01J37/0018—Addition of a binding agent or of material, later completely removed among others as result of heat treatment, leaching or washing,(e.g. forming of pores; protective layer, desintegrating by heat)
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- 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
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
- C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
- C10G45/06—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
- C10G45/08—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/44—Hydrogenation of the aromatic hydrocarbons
- C10G45/46—Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used
- C10G45/48—Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
- C10G45/50—Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum or tungsten metal, or compounds thereof
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Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Catalysts (AREA)
Description
本発明の主題である触媒組成物調製プロセスにとって、成分は全て、有機化合物又は界面活性剤を含有する溶液の添加中に完全に溶解することがきわめて重要である。プロセスは、極性溶媒内で完全に溶解する関連する金属の錯体であって、溶媒結晶化又は蒸発プロセスによって後で結晶化される、関連する金属の錯体を形成するために、触媒成分金属を含有する溶液と有機化合物又は界面活性剤を含有する溶液を混合し、反応させることを含む。本文脈における「完全に溶解した(completely dissolved)」という用語は、前駆体塩と界面活性剤を含有する溶液の混合中に、懸濁液も沈殿物も形成されないこと、すなわち、透明溶液が得られることを意味する。
11.93gのヘプタモリブデン酸アンモニウム[(NH4)6Mo7O24]、21.18gの硝酸ニッケル[Ni(NO3)2.6H2O]、及び0.33gの臭化セチルトリメチルアンモニウム(CTAB)が、150mlの脱イオン水内で溶解される。4〜6のpHを有する緑色の結晶溶液が得られ、その後、28容積%水酸化アンモニウム、約125mlが、8〜10のpHに達するまで添加され、溶液は、結晶性を残し、その色が、緑から青に変わる。その後、溶液は、79〜90℃に加熱され、過剰の水(125ml)の蒸発及び緑の沈殿物の形成が可能になる。形成された懸濁液は、7.3のpHを呈する。得られた材料は、ろ過され、豊富な量の脱イオン水で洗浄され、18時間の間、120℃で乾燥される。
触媒組成物内に残渣炭素前駆体として添加された界面活性剤の影響を評価するために、実施例1で調製された材料は、空気雰囲気内で400℃の温度で焼成された。得られた材料の酸化相は、その形態が、ニッケルモリブデン混合酸化物のナノ粒子からなる、β−NiMoO4相及び少量のα−NiMoO4相に相当する結晶構造を呈し(図1(b)を参照されたい)、また、105m2/gのBET表面積、0.18cm3/gの平均孔容積、及び6.9nmの平均孔直径を呈した。
この実施例は、実施例1に述べる同じ方法に従う。この実施例では、材料は、炭素前駆体有機成分の添加無しで調製された。この実施例で使用される塩の量は、界面活性剤としてのCTABの添加の無い実施例1の場合と同じであった。得られた沈殿物は、ろ過され、豊富な量の脱イオン水で洗浄された。
比較例1で得られた乾燥材料は、実施例2に述べる同じ手順に従って空気雰囲気内で焼成された。酸化相では、材料は、実施例2で報告された同じ結晶構造を呈した。しかし、BET表面積は92m2/gであり、孔容積は0.132cm3/gであり、平均孔直径は5.1nmであった。酸化形態の材料は、硫化処置を受ける。硫化処置を受けるために、材料は、100ml/分の窒素流量を使用して石英管内で、400℃に達するまで4℃/分の速度で加熱される。400℃に達すると、窒素流は、10容積%のH2S及び90容積%のH2からなるガスの混合物に変更され、2時間の間維持される。粉末形態(80:100 Tyler mesh)の硫化材料の一部分は、実施例1に述べる手順及び条件によって、考えられる最大限、環境に対する暴露を回避しながら、ジベンゾチオフェン(DBT)の水素化脱硫反応において評価された。
この例では、触媒は、粘結剤又は結合剤の存在下でのニッケルモリブデン混合オキシ水酸化物の沈殿によって調製された。243m2/gの表面積、0.336cm3/gの平均孔容積、及び5.54nmの平均孔直径を有するベーマイト相のアルミナが使用された。このために、ちょうど実施例1と同様に、11.93gの硝酸ニッケル、21.18gのヘプタモリブデン酸アンモニウム、及び0.33gの界面活性剤(CTAB)が、150mlの水内に溶解された(pH=5)。溶液は、緑色を取得し、その後、この溶液は、90℃に加熱され、125mlの水酸化アンモニウム(pH=10)が添加され、結晶溶液は青色を取得した。この溶液は、90℃に加熱しながら、30分間維持され、その後、68.25gのベーマイト(Catapal)が添加された。蒸発によって水を除去するために、ベーマイトを添加された溶液は、青から緑、その後、浅緑への色の変化が認められるまで、先に示した温度で約3時間の間、加熱し続けた。得られた沈殿物は、室温で冷却されたままにされ、蒸留水で4回、洗浄ごとに600mlで洗浄された。最後に、得られた生成物は、18時間の間、120℃の温度で乾燥された。その後、材料は、実施例1で述べた手順に従って焼成された。酸化相では、材料は、ガンマ−アルミナに特有の回折パターンを示す。酸化相の触媒は、16.4重量%のMoO3、7.17重量%のNiO、及び76.4重量%のAl2O3を含有する。この材料は、271m2/gの窒素吸着によって測定された比面積、0.31cm3/gの孔容積、及び4.5nmの孔直径を示す。
比較例3は、有機化合物を添加することなく実施例3に述べる方法に従って実施された。この場合、ヘプタモリブデン酸アンモニウム塩及び硝酸ニッケル溶液の調製中に、界面活性剤は添加されなかった。結晶化は、粘結剤、実施例3で使用されるものと同じ粘結剤の存在下で実施された。
この例は、水素化脱硫触媒のために従来のアルミナ上に担持された本発明の目的である触媒組成物と同じ金属に基づく、市販の触媒の触媒活性の評価に相当する。触媒活性の評価は、実施例1に述べた手順に従ってDBT水素化脱硫反応において実施された。
実施例1に述べる方法に従って、ニッケル塩をコバルト塩で置換して、材料が調製された。こうするために、11.93gのヘプタモリブデン酸アンモニウム、21.18gの硝酸コバルト[Co(NO3)2.6H2O]、及び0.33gの臭化セチルトリメチルアンモニウム(CTAB)が使用された。
材料は、実施例1に述べる手順に従って調製された。こうするために、同じ量のヘプタモリブデン酸アンモニウム(11.93g)が使用され、第2金属塩の量が、2つの、10.6gの硝酸ニッケルと10.6gの硝酸コバルトに分割された。同じ方法に従って、コバルト、ニッケル、及びモリブデンの混合硝酸塩の一貫した沈殿物が得られた。沈殿物は、実施例1と同様に、洗浄され、乾燥された。
合成中に添加された界面活性剤の濃度の影響を観測するために、以下の2つの例では、組み込まれる界面活性剤の量を変えた。材料は、実施例1で述べた手順に従って調製され、同じ量の前駆体塩及び溶媒の量を使用し、1.65gのCTABである添加される界面活性剤の量だけが変わった。沈殿は、実施例1と同様に洗浄され、乾燥された。
実施例1で述べた同じ手順に従って、また、実施例6の場合と同じ目的で、界面活性剤の量は、この実施例では、実施例1の場合と同じ量の塩と溶媒を使用して、3.3gのCTABまで増加した。
触媒組成物は、実施例1で述べる手順に従って調製された。得られた沈殿物、ニッケル−モリブデンオキシ水酸化物は、触媒組成物の総重量に基づいて20重量%のアルミナベーマイト(alumina boehmite)を混合された。その後、蒸留水内に溶解された3重量%の硝酸の水性溶液が、ペーストが得られるように添加された。湿潤ペーストが、閉じた容器内に溜まる(left to stand)ように放置され、その後、成形された。得られる成形品は、実施例1で述べる手順に従って120℃で乾燥された。
Claims (8)
- 少なくとも1つの第VIII族非貴金属の硫化物、及び、少なくとも1つの第VIB族非貴金属の硫化物、及び/又は、第VIII族金属と第VIB族金属の混合硫化物、及び炭素を含み、酸化状態にある、かつ/又は、部分的に還元される、かつ/又は、硫化されることができる粘結剤として無機酸化物を含有し、前記第VIII族金属の硫化物と第VIB族金属の硫化物の少なくとも一部は、2の構造層から20の構造層の積層を有するフラーレン微小球の形態を呈する、炭化水素の水素化処理で使用される触媒組成物。
- 第VIII族非貴金属は、その濃度が、含まれる酸化物の全組成物の20重量%から50重量%まで変わる、ニッケル及び/又はコバルト或いはその混合物に相当する請求項1に記載の触媒組成物。
- 第VIB族金属は、その組成が、関係する金属の酸化物として判定される全組成物の30から50%まで変わる、モリブデン及び/又はタングステンに相当する請求項1に記載の触媒組成物。
- 第VIB族金属は、モリブデンである請求項3に記載の触媒組成物。
- 炭素は、アモルファス状態にあるか、又は、その濃度が、関係する酸化物の全濃度の0.05重量%から5重量%まで変わる、第VIB族金属と第VIII族金属を有するカーバイドを形成する請求項1に記載の触媒組成物。
- 第VIII族金属と第VIB族金属は、酸化物として判定される全触媒組成物の50〜100重量%を有する請求項1に記載の触媒組成物。
- 触媒組成物のX線回折パターンは、第VIB族から選択される金属がモリブデンである場合、第VIII族金属のモリブデン酸塩のアルファ相又はベータ相に、かつ/又は、選択される金属がタングステンである場合、第VIII族金属のタングステン酸塩に相当する請求項1に記載の触媒組成物。
- 触媒組成物のX線回折パターンは、第VIB族から選択される金属がモリブデンである場合、モリブデン酸塩アルファ相又はベータ相又はコバルトモリブデン酸塩又はニッケルコバルトモリブデン酸塩に、かつ/又は、第VIB族から選択される金属がタングステンである場合、タングステン酸塩又はコバルトタングステン酸塩又はニッケルコバルトタングステン酸塩に相当する請求項1に記載の触媒組成物。
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Families Citing this family (79)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010131588A (ja) * | 2008-10-28 | 2010-06-17 | Mitsubishi Heavy Ind Ltd | 排ガス処理触媒およびその選定方法 |
CA2764875A1 (en) * | 2009-06-12 | 2010-12-16 | Aggregate Energy, Llc. | Catalyst comprising a metal and a supplemental component and process for hydrogenating oxygen containing organic products |
US9254478B2 (en) | 2009-08-24 | 2016-02-09 | Albemarle Corporation | Solutions and catalysts comprising group VI metal, group VIII metal, phosphorus and an additive |
DK2484745T3 (da) | 2009-09-30 | 2021-01-25 | Jx Nippon Oil & Energy Corp | Hydroafsvovlingskatalysator for en carbonhydridolie, fremgangsmåde til fremstilling heraf og fremgangsmåde til hydroraffinering |
IT1398288B1 (it) | 2009-09-30 | 2013-02-22 | Eni Spa | Ossidi misti di metalli di transizione, catalizzatori di idrotrattamento da essi ottenuti, e processo di preparazione comprendente procedimenti sol-gel |
JP5871810B2 (ja) * | 2009-11-24 | 2016-03-01 | シェブロン ユー.エス.エー. インコーポレイテッド | 水素化プロセスのバルク触媒及びその製造方法 |
SG186776A1 (en) | 2010-06-25 | 2013-02-28 | Jx Nippon Oil & Energy Corp | Hydrodesulfurization catalyst for hydrocarbon oil, process of producing same and method for hydrorefining |
EP2439253A1 (en) * | 2010-10-05 | 2012-04-11 | Research Institute of Petroleum Industry (RIPI) | Hydrodesulfurization nanocatalyst comprising a support of nanotube / nanorod alumina, method of preparation and application |
ITMI20110510A1 (it) | 2011-03-30 | 2012-10-01 | Eni Spa | Ossidi misti di metalli di transizione, catalizzatori di idrotrattamento da essi ottenuti, e processo di preparazione |
RU2472583C1 (ru) * | 2011-06-09 | 2013-01-20 | Общество с ограниченной ответственностью Научно Производственная фирма "ОЛКАТ" | Шариковый катализатор для гидроочистки нефтяных фракций и способ его приготовления |
JP6120835B2 (ja) * | 2011-07-08 | 2017-04-26 | サウジ ベーシック インダストリーズ コーポレイションSaudi Basic Industries Corporaiton | 改善された炭素担持コバルトおよびモリブデン触媒、ならびに低級アルコールを生成するためのその使用 |
RU2473387C1 (ru) * | 2011-10-06 | 2013-01-27 | Учреждение Российской академии наук Институт проблем переработки углеводородов Сибирского отделения РАН (ИППУ СО РАН) | Способ получения массивного катализатора гидропереработки тяжелых нефтяных фракций |
US9776177B2 (en) | 2012-03-29 | 2017-10-03 | Wayne State University | Bimetal catalysts |
RU2492922C1 (ru) * | 2012-04-27 | 2013-09-20 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Самарский государственный технический университет" | Состав и способ синтеза катализатора гидродеоксигенации кислородсодержащего углеводородного сырья |
CN103191745B (zh) * | 2013-04-23 | 2014-09-10 | 安徽工业大学 | 一种芳烃加氢催化剂 |
MX360196B (es) | 2013-09-25 | 2018-10-11 | Mexicano Inst Petrol | Catalizador de titania nanoestructurada de acidez estabilizada y proceso de obtencion. |
EP3099762B1 (en) | 2014-01-28 | 2019-10-02 | Shell International Research Maatschappij B.V. | Conversion of biomass or residual waste material to biofuels |
JP6278727B2 (ja) * | 2014-02-04 | 2018-02-14 | 住友化学株式会社 | 共沈物の製造方法およびリチウム含有複合酸化物の製造方法 |
EP3164471B1 (en) * | 2014-07-01 | 2019-07-24 | Shell International Research Maatschappij B.V. | Conversion of solid biomass into a liquid hydrocarbon material |
DE102014013530A1 (de) * | 2014-09-12 | 2016-03-17 | Clariant International Ltd. | Extrudierter Cu-Al-Mn-Hydrierkatalysator |
WO2016065253A1 (en) * | 2014-10-23 | 2016-04-28 | Leal Juan | Synthesis of molybdenum sulfide (mos2) and tungsten sulfide (ws2) catalyst |
AU2016325487B2 (en) | 2015-09-25 | 2019-04-11 | Shell Internationale Research Maatschappij B.V. | Conversion of biomass into methane |
US10005812B2 (en) * | 2015-12-15 | 2018-06-26 | Uop Llc | Transition metal molybdotungsten oxy-hydroxide |
US10232357B2 (en) | 2015-12-15 | 2019-03-19 | Uop Llc | Crystalline ammonia transition metal molybdate |
US10053637B2 (en) | 2015-12-15 | 2018-08-21 | Uop Llc | Transition metal tungsten oxy-hydroxide |
US10052616B2 (en) | 2015-12-15 | 2018-08-21 | Uop Llc | Crystalline ammonia transition metal molybdotungstate |
US10233398B2 (en) * | 2015-12-15 | 2019-03-19 | Uop Llc | Crystalline transition metal oxy-hydroxide molybdotungstate |
US10399065B2 (en) | 2015-12-15 | 2019-09-03 | Uop Llc | Crystalline transition metal tungstate |
US10052614B2 (en) | 2015-12-15 | 2018-08-21 | Uop Llc | Mixed metal oxides |
US10400181B2 (en) | 2015-12-15 | 2019-09-03 | Uop Llc | Crystalline bis-ammonia metal molybdate |
US10399063B2 (en) | 2015-12-15 | 2019-09-03 | Uop Llc | Mixed metal oxides |
US10046315B2 (en) | 2015-12-15 | 2018-08-14 | Uop Llc | Crystalline transition metal molybdotungstate |
US10322404B2 (en) * | 2015-12-15 | 2019-06-18 | Uop Llc | Crystalline transition metal oxy-hydroxide molybdate |
US10449523B2 (en) * | 2015-12-15 | 2019-10-22 | Uop Llc | Crystalline bis-ammonia transition metal molybdotungstate |
RU2622040C1 (ru) * | 2016-08-22 | 2017-06-09 | Акционерное общество "Газпромнефть - Омский НПЗ" (АО "Газпромнефть - ОНПЗ") | Способ гидроочистки дизельного топлива |
RU2640210C1 (ru) * | 2016-10-06 | 2017-12-27 | Федеральное государственное бюджетное учреждение науки Ордена Трудового Красного Знамени Институт нефтехимического синтеза им. А.В. Топчиева Российской академии наук (ИНХС РАН) | Катализатор гидропереработки нефтяных фракций (варианты) |
CN107983405B (zh) * | 2016-10-26 | 2020-08-18 | 中国石油化工股份有限公司 | 一种加氢催化剂的制备方法 |
CN107983326B (zh) * | 2016-10-26 | 2020-08-18 | 中国石油化工股份有限公司 | 一种加氢催化剂成型载体的制备方法 |
US20190233741A1 (en) | 2017-02-12 | 2019-08-01 | Magēmā Technology, LLC | Multi-Stage Process and Device for Reducing Environmental Contaminates in Heavy Marine Fuel Oil |
US11788017B2 (en) | 2017-02-12 | 2023-10-17 | Magëmã Technology LLC | Multi-stage process and device for reducing environmental contaminants in heavy marine fuel oil |
US10604709B2 (en) | 2017-02-12 | 2020-03-31 | Magēmā Technology LLC | Multi-stage device and process for production of a low sulfur heavy marine fuel oil from distressed heavy fuel oil materials |
IT201700037970A1 (it) | 2017-04-06 | 2018-10-06 | Eni Spa | Idrotrattamento di cariche da fonti rinnovabili con catalizzatori ad elevato contenuto di fase attiva |
WO2018221706A1 (ja) | 2017-05-31 | 2018-12-06 | 古河電気工業株式会社 | メタノール改質触媒構造体、メタノール改質用装置、メタノール改質触媒構造体の製造方法及びオレフィンまたは芳香族炭化水素の少なくとも一方の製造方法 |
CN110709165A (zh) | 2017-05-31 | 2020-01-17 | 国立大学法人北海道大学 | 功能性结构体以及功能性结构体的制造方法 |
US11161101B2 (en) | 2017-05-31 | 2021-11-02 | Furukawa Electric Co., Ltd. | Catalyst structure and method for producing the catalyst structure |
WO2018221690A1 (ja) | 2017-05-31 | 2018-12-06 | 国立大学法人北海道大学 | 機能性構造体及び機能性構造体の製造方法 |
JP7352909B2 (ja) | 2017-05-31 | 2023-09-29 | 国立大学法人北海道大学 | 機能性構造体及び機能性構造体の製造方法 |
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US10882030B2 (en) | 2017-08-25 | 2021-01-05 | Uop Llc | Crystalline transition metal tungstate |
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US10737246B2 (en) | 2018-06-29 | 2020-08-11 | Uop Llc | Poorly crystalline transition metal tungstate |
WO2020116477A1 (ja) * | 2018-12-03 | 2020-06-11 | 古河電気工業株式会社 | 触媒構造体およびその製造方法、ならびに該触媒構造体を用いた炭化水素の製造方法 |
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CN110975909B (zh) * | 2019-08-22 | 2023-04-07 | 中国石油天然气股份有限公司 | 一种体相催化剂及其制备方法、包含其的加氢催化剂 |
CN114505089B (zh) * | 2020-11-16 | 2023-06-13 | 南开大学 | 一种用于萘加氢制备十氢萘的催化剂的制备方法及其使用方法 |
CN115505425A (zh) * | 2022-09-19 | 2022-12-23 | 连云港鹏辰特种新材料有限公司 | 一种双氧水生产用高沸点高纯度溶剂油的制备方法 |
Family Cites Families (31)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2911293A (en) * | 1956-05-28 | 1959-11-03 | Exxon Research Engineering Co | Production of gas |
US2853257A (en) * | 1956-06-22 | 1958-09-23 | Robert G Cook | Automatic aircraft holdback release device |
US4243554A (en) | 1979-06-11 | 1981-01-06 | Union Carbide Corporation | Molybdenum disulfide catalyst and the preparation thereof |
GB2101005B (en) * | 1981-06-02 | 1984-09-05 | Asia Oil Co Ltd | Hydrogenation catalyst |
JPS57201533A (en) * | 1981-06-04 | 1982-12-10 | Mitsubishi Chem Ind Ltd | Hydrodesulfurizing and demetallizing catalyst |
US4528089A (en) | 1982-07-20 | 1985-07-09 | Exxon Research And Engineering Co. | Hydrogenation processes using carbon-containing molybdenum and tungsten sulfide catalysts |
US4508847A (en) | 1982-07-20 | 1985-04-02 | Exxon Research & Engineering Co. | Carbon-containing molybdenum and tungsten sulfide catalysts |
US4581125A (en) * | 1983-07-29 | 1986-04-08 | Exxon Research And Engineering Co. | Hydrotreating using self-promoted molybdenum and tungsten sulfide catalysts formed from bis(tetrathiometallate) precursors |
US4514517A (en) * | 1983-07-29 | 1985-04-30 | Exxon Research And Engineering Co. | Supported, self-promoted molybdenum and tungsten sulfide catalysts formed from bis(tetrathiometallate) precursors, and their preparation |
US4650563A (en) | 1984-04-02 | 1987-03-17 | Exxon Research And Engineering Company | Transition metal sulfide promoted molybdenum or tungsten sulfide catalysts and their uses for hydroprocessing |
US4716139A (en) * | 1984-09-28 | 1987-12-29 | Exxon Research And Engineering Company | Amorphous sulfide catalysts of trivalent chromium and promoter metals and method of making same |
TW230217B (ja) | 1990-03-23 | 1994-09-11 | Cosmo Oil Co Ltd | |
US5089462A (en) * | 1990-06-25 | 1992-02-18 | Chevron Research And Technology Company | Hydroconversion catalyst and method for making the catalyst |
EP0469675B1 (en) | 1990-08-03 | 1996-05-08 | Akzo Nobel N.V. | Hydrodesulphurization process |
JPH0576766A (ja) * | 1991-09-20 | 1993-03-30 | Cosmo Oil Co Ltd | 炭化水素油の水素化脱硫用触媒の製造方法 |
JPH07284666A (ja) * | 1994-04-18 | 1995-10-31 | Idemitsu Kosan Co Ltd | 重質油の水素化処理用触媒及びそれを用いる重質油の水素化処理方法 |
US5928496A (en) * | 1996-06-20 | 1999-07-27 | Contract Materials Processing, Inc. | Hydrotalcite sulfer oxide sorption |
US6783663B1 (en) * | 1997-07-15 | 2004-08-31 | Exxonmobil Research And Engineering Company | Hydrotreating using bulk multimetallic catalysts |
US6582590B1 (en) * | 1997-07-15 | 2003-06-24 | Exxonmobil Research And Engineering Company | Multistage hydroprocessing using bulk multimetallic catalyst |
US6156695A (en) * | 1997-07-15 | 2000-12-05 | Exxon Research And Engineering Company | Nickel molybdotungstate hydrotreating catalysts |
US6635599B1 (en) | 1997-07-15 | 2003-10-21 | Exxonmobil Research & Engineering Company | Mixed metal catalyst, its preparation by co-precipitation, and its use |
US6162350A (en) * | 1997-07-15 | 2000-12-19 | Exxon Research And Engineering Company | Hydroprocessing using bulk Group VIII/Group VIB catalysts (HEN-9901) |
US6156693A (en) | 1998-10-09 | 2000-12-05 | Penn State Research Foundation | Method for preparing a highly active, unsupported high-surface-area ub. MoS.s2 catalyst |
US6534437B2 (en) | 1999-01-15 | 2003-03-18 | Akzo Nobel N.V. | Process for preparing a mixed metal catalyst composition |
IT1311512B1 (it) * | 1999-03-12 | 2002-03-13 | Agip Petroli | Composizione catalitica per l'upgrading di miscele idrocarburiche. |
DE60134140D1 (de) * | 2000-07-12 | 2008-07-03 | Albemarle Netherlands Bv | Verfahren zur herstellung eines ein additiv enthaltenden mischmetallkatalysators |
DK1299185T3 (da) * | 2000-07-12 | 2011-06-20 | Albemarle Netherlands Bv | Blandet metalkatalysator omfattende en brændbar binder |
CA2415417C (en) * | 2000-07-12 | 2010-05-04 | Akzo Nobel N.V. | Process for preparing an additive-based mixed metal catalyst |
US6759364B2 (en) * | 2001-12-17 | 2004-07-06 | Shell Oil Company | Arsenic removal catalyst and method for making same |
GB0214383D0 (en) * | 2002-06-21 | 2002-07-31 | Isis Innovation | Catalyst |
CA2521944C (en) | 2003-04-07 | 2012-10-02 | Board Of Regents, The University Of Texas System | Molybdenum sulfide/carbide catalysts |
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EP1941944A1 (en) | 2008-07-09 |
EP1941944A4 (en) | 2011-06-01 |
RU2417124C2 (ru) | 2011-04-27 |
JP2013018001A (ja) | 2013-01-31 |
US20150087502A1 (en) | 2015-03-26 |
RU2008112007A (ru) | 2009-10-10 |
US9776174B2 (en) | 2017-10-03 |
JP2009505830A (ja) | 2009-02-12 |
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