JP2008279432A - Method of manufacturing catalyst for producing alkenyl acetate - Google Patents
Method of manufacturing catalyst for producing alkenyl acetate Download PDFInfo
- Publication number
- JP2008279432A JP2008279432A JP2008043176A JP2008043176A JP2008279432A JP 2008279432 A JP2008279432 A JP 2008279432A JP 2008043176 A JP2008043176 A JP 2008043176A JP 2008043176 A JP2008043176 A JP 2008043176A JP 2008279432 A JP2008279432 A JP 2008279432A
- Authority
- JP
- Japan
- Prior art keywords
- carrier
- catalyst
- acetate
- palladium
- solution
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 79
- -1 alkenyl acetate Chemical compound 0.000 title claims abstract description 44
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 28
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims abstract description 110
- 229910052763 palladium Inorganic materials 0.000 claims abstract description 55
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims abstract description 53
- 150000001875 compounds Chemical class 0.000 claims abstract description 47
- 238000000034 method Methods 0.000 claims abstract description 44
- 229910052697 platinum Inorganic materials 0.000 claims abstract description 26
- 230000009467 reduction Effects 0.000 claims abstract description 17
- 230000008569 process Effects 0.000 claims abstract description 14
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 61
- 239000010931 gold Substances 0.000 claims description 49
- 229910052737 gold Inorganic materials 0.000 claims description 47
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical group [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims description 42
- 239000002994 raw material Substances 0.000 claims description 31
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 27
- 229910052751 metal Inorganic materials 0.000 claims description 27
- 239000002184 metal Substances 0.000 claims description 27
- 150000001342 alkaline earth metals Chemical class 0.000 claims description 23
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 claims description 22
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 20
- 239000001301 oxygen Substances 0.000 claims description 20
- 229910052760 oxygen Inorganic materials 0.000 claims description 20
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 claims description 16
- 150000001336 alkenes Chemical class 0.000 claims description 14
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 11
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 9
- 239000005977 Ethylene Substances 0.000 claims description 9
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims description 7
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 6
- 229910052788 barium Inorganic materials 0.000 claims description 6
- 229910052802 copper Inorganic materials 0.000 claims description 6
- 239000010949 copper Substances 0.000 claims description 6
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 claims description 5
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 5
- 239000011575 calcium Substances 0.000 claims description 4
- 229910052712 strontium Inorganic materials 0.000 claims description 4
- 229910052791 calcium Inorganic materials 0.000 claims description 3
- 229910052749 magnesium Inorganic materials 0.000 claims description 3
- 239000011777 magnesium Substances 0.000 claims description 3
- HVAMZGADVCBITI-UHFFFAOYSA-M pent-4-enoate Chemical compound [O-]C(=O)CCC=C HVAMZGADVCBITI-UHFFFAOYSA-M 0.000 claims description 3
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 claims description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 12
- 150000001242 acetic acid derivatives Chemical class 0.000 abstract description 3
- FFBHFFJDDLITSX-UHFFFAOYSA-N benzyl N-[2-hydroxy-4-(3-oxomorpholin-4-yl)phenyl]carbamate Chemical compound OC1=C(NC(=O)OCC2=CC=CC=C2)C=CC(=C1)N1CCOCC1=O FFBHFFJDDLITSX-UHFFFAOYSA-N 0.000 abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 65
- 239000000243 solution Substances 0.000 description 51
- 239000007864 aqueous solution Substances 0.000 description 40
- 238000006243 chemical reaction Methods 0.000 description 37
- 238000010521 absorption reaction Methods 0.000 description 26
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 23
- 239000007789 gas Substances 0.000 description 19
- 238000006722 reduction reaction Methods 0.000 description 17
- 239000000203 mixture Substances 0.000 description 14
- SCVFZCLFOSHCOH-UHFFFAOYSA-M potassium acetate Chemical compound [K+].CC([O-])=O SCVFZCLFOSHCOH-UHFFFAOYSA-M 0.000 description 13
- 150000003839 salts Chemical class 0.000 description 13
- 239000011734 sodium Substances 0.000 description 13
- 230000000052 comparative effect Effects 0.000 description 12
- 229910052708 sodium Inorganic materials 0.000 description 12
- 239000000377 silicon dioxide Substances 0.000 description 11
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 10
- 239000002253 acid Substances 0.000 description 10
- 238000002360 preparation method Methods 0.000 description 10
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 9
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 9
- 101150003085 Pdcl gene Proteins 0.000 description 7
- 239000003513 alkali Substances 0.000 description 7
- 239000003638 chemical reducing agent Substances 0.000 description 7
- 238000005406 washing Methods 0.000 description 7
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 6
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 6
- 239000012018 catalyst precursor 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
- 150000002940 palladium Chemical class 0.000 description 6
- 235000011056 potassium acetate Nutrition 0.000 description 6
- 229910004806 Na2 SiO3.9H2 O Inorganic materials 0.000 description 5
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 5
- 238000010306 acid treatment Methods 0.000 description 5
- 229910052783 alkali metal Inorganic materials 0.000 description 5
- 150000001340 alkali metals Chemical class 0.000 description 5
- 238000004458 analytical method Methods 0.000 description 5
- 239000003085 diluting agent Substances 0.000 description 5
- 238000004817 gas chromatography Methods 0.000 description 5
- 239000011148 porous material Substances 0.000 description 5
- 229910052700 potassium Inorganic materials 0.000 description 5
- 239000011591 potassium Substances 0.000 description 5
- 229960003975 potassium Drugs 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 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
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 230000000977 initiatory effect Effects 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 239000012071 phase Substances 0.000 description 4
- 239000002243 precursor Substances 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- NWZSZGALRFJKBT-KNIFDHDWSA-N (2s)-2,6-diaminohexanoic acid;(2s)-2-hydroxybutanedioic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O.NCCCC[C@H](N)C(O)=O NWZSZGALRFJKBT-KNIFDHDWSA-N 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 3
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000012159 carrier gas Substances 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 238000011156 evaluation Methods 0.000 description 3
- IKDUDTNKRLTJSI-UHFFFAOYSA-N hydrazine monohydrate Substances O.NN IKDUDTNKRLTJSI-UHFFFAOYSA-N 0.000 description 3
- 238000005470 impregnation Methods 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 238000011068 loading method Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 150000007524 organic acids Chemical class 0.000 description 3
- 235000006408 oxalic acid Nutrition 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000009834 vaporization Methods 0.000 description 3
- 230000008016 vaporization Effects 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N Hydroquinone Chemical compound OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 description 2
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 2
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 150000001299 aldehydes Chemical class 0.000 description 2
- XXROGKLTLUQVRX-UHFFFAOYSA-N allyl alcohol Chemical compound OCC=C XXROGKLTLUQVRX-UHFFFAOYSA-N 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
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- IWOUKMZUPDVPGQ-UHFFFAOYSA-N barium nitrate Chemical compound [Ba+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O IWOUKMZUPDVPGQ-UHFFFAOYSA-N 0.000 description 2
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 description 2
- ZCCIPPOKBCJFDN-UHFFFAOYSA-N calcium nitrate Chemical compound [Ca+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ZCCIPPOKBCJFDN-UHFFFAOYSA-N 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 239000001307 helium Substances 0.000 description 2
- 229910052734 helium Inorganic materials 0.000 description 2
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 2
- 239000011964 heteropoly acid Substances 0.000 description 2
- 238000010813 internal standard method Methods 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 229910052744 lithium Inorganic materials 0.000 description 2
- YIXJRHPUWRPCBB-UHFFFAOYSA-N magnesium nitrate Chemical compound [Mg+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O YIXJRHPUWRPCBB-UHFFFAOYSA-N 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 150000007522 mineralic acids Chemical class 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 150000003057 platinum Chemical class 0.000 description 2
- YKYONYBAUNKHLG-UHFFFAOYSA-N propyl acetate Chemical compound CCCOC(C)=O YKYONYBAUNKHLG-UHFFFAOYSA-N 0.000 description 2
- 239000012495 reaction gas Substances 0.000 description 2
- 230000009257 reactivity Effects 0.000 description 2
- 239000001632 sodium acetate Substances 0.000 description 2
- 235000017281 sodium acetate Nutrition 0.000 description 2
- DHEQXMRUPNDRPG-UHFFFAOYSA-N strontium nitrate Chemical compound [Sr+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O DHEQXMRUPNDRPG-UHFFFAOYSA-N 0.000 description 2
- UBXAKNTVXQMEAG-UHFFFAOYSA-L strontium sulfate Chemical compound [Sr+2].[O-]S([O-])(=O)=O UBXAKNTVXQMEAG-UHFFFAOYSA-L 0.000 description 2
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- 125000003903 2-propenyl group Chemical group [H]C([*])([H])C([H])=C([H])[H] 0.000 description 1
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 102000002322 Egg Proteins Human genes 0.000 description 1
- 108010000912 Egg Proteins Proteins 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 229910004373 HOAc Inorganic materials 0.000 description 1
- 239000005909 Kieselgur Substances 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- 239000004115 Sodium Silicate Substances 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 description 1
- IKHGUXGNUITLKF-XPULMUKRSA-N acetaldehyde Chemical compound [14CH]([14CH3])=O IKHGUXGNUITLKF-XPULMUKRSA-N 0.000 description 1
- CTUFHBVSYAEMLM-UHFFFAOYSA-N acetic acid;platinum Chemical compound [Pt].CC(O)=O.CC(O)=O CTUFHBVSYAEMLM-UHFFFAOYSA-N 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 229910000272 alkali metal oxide Inorganic materials 0.000 description 1
- 229910000318 alkali metal phosphate Inorganic materials 0.000 description 1
- 229910001617 alkaline earth metal chloride Inorganic materials 0.000 description 1
- 229910001860 alkaline earth metal hydroxide Inorganic materials 0.000 description 1
- 229910000316 alkaline earth metal phosphate Inorganic materials 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 125000003342 alkenyl group Chemical group 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- ITHZDDVSAWDQPZ-UHFFFAOYSA-L barium acetate Chemical compound [Ba+2].CC([O-])=O.CC([O-])=O ITHZDDVSAWDQPZ-UHFFFAOYSA-L 0.000 description 1
- 229910001626 barium chloride Inorganic materials 0.000 description 1
- WDIHJSXYQDMJHN-UHFFFAOYSA-L barium chloride Chemical compound [Cl-].[Cl-].[Ba+2] WDIHJSXYQDMJHN-UHFFFAOYSA-L 0.000 description 1
- RQPZNWPYLFFXCP-UHFFFAOYSA-L barium dihydroxide Chemical compound [OH-].[OH-].[Ba+2] RQPZNWPYLFFXCP-UHFFFAOYSA-L 0.000 description 1
- 229910001863 barium hydroxide Inorganic materials 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- VSGNNIFQASZAOI-UHFFFAOYSA-L calcium acetate Chemical compound [Ca+2].CC([O-])=O.CC([O-])=O VSGNNIFQASZAOI-UHFFFAOYSA-L 0.000 description 1
- 239000001639 calcium acetate Substances 0.000 description 1
- 235000011092 calcium acetate Nutrition 0.000 description 1
- 229960005147 calcium acetate Drugs 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 238000011088 calibration curve Methods 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 239000012295 chemical reaction liquid Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003426 co-catalyst Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- IRXRGVFLQOSHOH-UHFFFAOYSA-L dipotassium;oxalate Chemical compound [K+].[K+].[O-]C(=O)C([O-])=O IRXRGVFLQOSHOH-UHFFFAOYSA-L 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 210000003278 egg shell Anatomy 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 238000010574 gas phase reaction Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 230000003100 immobilizing effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000012770 industrial material Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- UEGPKNKPLBYCNK-UHFFFAOYSA-L magnesium acetate Chemical compound [Mg+2].CC([O-])=O.CC([O-])=O UEGPKNKPLBYCNK-UHFFFAOYSA-L 0.000 description 1
- 239000011654 magnesium acetate Substances 0.000 description 1
- 235000011285 magnesium acetate Nutrition 0.000 description 1
- 229940069446 magnesium acetate Drugs 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 1
- 235000019341 magnesium sulphate Nutrition 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 125000000896 monocarboxylic acid group Chemical group 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 229910052901 montmorillonite Inorganic materials 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- PIBWKRNGBLPSSY-UHFFFAOYSA-L palladium(II) chloride Chemical compound Cl[Pd]Cl PIBWKRNGBLPSSY-UHFFFAOYSA-L 0.000 description 1
- YJVFFLUZDVXJQI-UHFFFAOYSA-L palladium(ii) acetate Chemical compound [Pd+2].CC([O-])=O.CC([O-])=O YJVFFLUZDVXJQI-UHFFFAOYSA-L 0.000 description 1
- GPNDARIEYHPYAY-UHFFFAOYSA-N palladium(ii) nitrate Chemical compound [Pd+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O GPNDARIEYHPYAY-UHFFFAOYSA-N 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- CLSUSRZJUQMOHH-UHFFFAOYSA-L platinum dichloride Chemical compound Cl[Pt]Cl CLSUSRZJUQMOHH-UHFFFAOYSA-L 0.000 description 1
- NWAHZABTSDUXMJ-UHFFFAOYSA-N platinum(2+);dinitrate Chemical compound [Pt+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O NWAHZABTSDUXMJ-UHFFFAOYSA-N 0.000 description 1
- PQTLYDQECILMMB-UHFFFAOYSA-L platinum(2+);sulfate Chemical compound [Pt+2].[O-]S([O-])(=O)=O PQTLYDQECILMMB-UHFFFAOYSA-L 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 239000001508 potassium citrate Substances 0.000 description 1
- 229960002635 potassium citrate Drugs 0.000 description 1
- QEEAPRPFLLJWCF-UHFFFAOYSA-K potassium citrate (anhydrous) Chemical compound [K+].[K+].[K+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O QEEAPRPFLLJWCF-UHFFFAOYSA-K 0.000 description 1
- 235000011082 potassium citrates Nutrition 0.000 description 1
- WFIZEGIEIOHZCP-UHFFFAOYSA-M potassium formate Chemical compound [K+].[O-]C=O WFIZEGIEIOHZCP-UHFFFAOYSA-M 0.000 description 1
- 235000011118 potassium hydroxide Nutrition 0.000 description 1
- 229910052913 potassium silicate Inorganic materials 0.000 description 1
- 235000019353 potassium silicate Nutrition 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 125000004368 propenyl group Chemical group C(=CC)* 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 229910000033 sodium borohydride Inorganic materials 0.000 description 1
- 239000012279 sodium borohydride Substances 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 235000019795 sodium metasilicate Nutrition 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 229910052911 sodium silicate Inorganic materials 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 229910001631 strontium chloride Inorganic materials 0.000 description 1
- AHBGXTDRMVNFER-UHFFFAOYSA-L strontium dichloride Chemical compound [Cl-].[Cl-].[Sr+2] AHBGXTDRMVNFER-UHFFFAOYSA-L 0.000 description 1
- UUCCCPNEFXQJEL-UHFFFAOYSA-L strontium dihydroxide Chemical compound [OH-].[OH-].[Sr+2] UUCCCPNEFXQJEL-UHFFFAOYSA-L 0.000 description 1
- 229910001866 strontium hydroxide Inorganic materials 0.000 description 1
- RXSHXLOMRZJCLB-UHFFFAOYSA-L strontium;diacetate Chemical compound [Sr+2].CC([O-])=O.CC([O-])=O RXSHXLOMRZJCLB-UHFFFAOYSA-L 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 235000000346 sugar Nutrition 0.000 description 1
- 150000008163 sugars Chemical class 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- YWYZEGXAUVWDED-UHFFFAOYSA-N triammonium citrate Chemical compound [NH4+].[NH4+].[NH4+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O YWYZEGXAUVWDED-UHFFFAOYSA-N 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Description
本発明は、酢酸、低級オレフィンおよび酸素を原料として酢酸アルケニルを合成する際に使用する酢酸アルケニル製造用触媒の製造方法およびその触媒を用いた酢酸アルケニルの製造方法に関する。 The present invention relates to a method for producing a catalyst for producing alkenyl acetate which is used when synthesizing alkenyl acetate using acetic acid, a lower olefin and oxygen as raw materials, and a method for producing alkenyl acetate using the catalyst.
酢酸アルケニルは、酢酸とアルケニルアルコールとのエステル化合物である。アルケニル基としては、ビニル基、アリル基、プロペニル基などが例示される。酢酸アルケニルの代表例である酢酸ビニルは、酢酸ビニル樹脂の原料、ポリビニルアルコールの原料、さらにエチレン、スチレン、アクリレート、メタクリレート等との共重合用モノマーとして、塗料、接着剤、繊維処理剤等の広い分野に用いられている重要な工業材料である。また、酢酸アリルは、アリルアルコールの製造原料などとして用いられている。以下の記述では、酢酸アルケニルとして酢酸ビニルを代表例として例示して詳細を説明する。 Alkenyl acetate is an ester compound of acetic acid and alkenyl alcohol. Examples of the alkenyl group include a vinyl group, an allyl group, and a propenyl group. Vinyl acetate, which is a representative example of alkenyl acetate, is a wide range of materials for vinyl acetate resin, polyvinyl alcohol, and monomers for copolymerization with ethylene, styrene, acrylate, methacrylate, etc. It is an important industrial material used in the field. Allyl acetate is used as a raw material for producing allyl alcohol. In the following description, vinyl acetate is exemplified as a representative example of alkenyl acetate, and the details will be described.
酢酸ビニルの工業的製造において、酢酸ビニルの空時収率または選択率を上げることは非常に重要な技術課題である。
酢酸、低級オレフィンおよび酸素を原料とする酢酸アルケニル、特に酢酸ビニルの製造用触媒として、Ｐｄ／Ａｕ／ＫＯＡｃ／ＳｉＯ２系の担持型触媒が広く用いられている。かかる触媒の活性点は、パラジウムであると考えられている。助触媒である金は、パラジウムのシンタリングを抑制したり、パラジウムを微分散させることで酢酸ビニルの空時収率を向上させたり、炭酸ガス生成反応を低減させて酢酸ビニルの選択率を向上させたりする役割があるとされる。また、助触媒である金の効果が発揮されるためには、パラジウムと金の担持位置を揃える必要があると考えられる。
In the industrial production of vinyl acetate, increasing the space-time yield or selectivity of vinyl acetate is a very important technical issue.
Pd / Au / KOAc / SiO 2 supported catalysts are widely used as catalysts for the production of alkenyl acetate, particularly vinyl acetate using acetic acid, lower olefins and oxygen as raw materials. The active site of such a catalyst is believed to be palladium. Gold as a co-catalyst suppresses palladium sintering, improves the space-time yield of vinyl acetate by finely dispersing palladium, and reduces the carbon dioxide gas generation reaction to improve vinyl acetate selectivity. It is said that there is a role to let you. Further, in order to exert the effect of gold as a cocatalyst, it is considered necessary to align the supporting positions of palladium and gold.
酢酸ビニル製造用の触媒は、パラジウムや金を担体の表面にのみ担持したいわゆるシェル型のものが反応性に優れると考えられている。シェル型触媒の調製法は、特表２００４-５２６５５３号公報などに開示されている。しかし、この方法で調製した触媒では、ＰｄとＡｕの担持位置にずれがみられ、さらにＡｕの担持率が低いことが問題であり、改善が必要であった。 As a catalyst for producing vinyl acetate, a so-called shell type catalyst in which palladium or gold is supported only on the surface of a carrier is considered to have excellent reactivity. A method for preparing a shell-type catalyst is disclosed in JP-T-2004-526553. However, in the catalyst prepared by this method, there is a problem that the Pd and Au loading positions are shifted, and the Au loading ratio is low, which requires improvement.
特表２００３-５１３７８８号公報では、アルカリ固定剤によりパラジウム、銅を担体に固定化させた後に、金の原料塩とアルカリとの混合水溶液を担体に含浸させることで、金を担体に担持している。また、特表２００１-５２１８１７号公報では、パラジウムおよび第３金属の全てと、金の一部を担体に固定し、還元後、残りの金に対応する金原料塩とアルカリとの混合水溶液を担体に含浸させることで、残りの金を担持している。
これらの２つの公報では、金の担持量を上げる目的で、担体への担持方法として、金原料塩とアルカリとの混合水溶液を担体に含浸させる手法を採用している。しかし、この手法では、金原料塩とアルカリとの混合水溶液の含浸によって担体に担持した金は、担体全体に担持されてしまい、金を担体表面のみに担持できず、金が効率的に使用されていないという問題点があった。また、担持処理を２回行うため、工程も煩雑であり、改善する必要があった。
In JP-T-2003-513788, after immobilizing palladium and copper on a carrier with an alkali fixing agent, the carrier is impregnated with a mixed aqueous solution of gold raw material salt and alkali, thereby supporting the gold on the carrier. Yes. In Japanese Patent Publication No. 2001-521817, all of palladium and the third metal and a part of gold are fixed to a support, and after reduction, a mixed aqueous solution of a gold raw material salt and an alkali corresponding to the remaining gold is supported on the support. The remaining gold is supported by impregnating with.
In these two publications, for the purpose of increasing the amount of gold supported, a method of impregnating a carrier with a mixed aqueous solution of a gold raw material salt and an alkali is adopted as a method for supporting the carrier. However, in this method, the gold supported on the support by impregnation with the mixed aqueous solution of the gold raw material salt and the alkali is supported on the entire support, and the gold cannot be supported only on the surface of the support. There was a problem that not. Further, since the supporting process is performed twice, the process is complicated and needs to be improved.
本発明は、活性または選択性が向上した酢酸アルケニル製造用触媒を提供することを目的とする。 An object of the present invention is to provide a catalyst for producing alkenyl acetate having improved activity or selectivity.
本発明者らは、上記課題を解決するために鋭意研究を重ねた。その結果、酢酸アルケニル製造用触媒の製造において、金の原料塩とアルカリとの混合水溶液を用いて触媒調製を行うことにより、金を担体表面のみに担持することができ、触媒の活性または選択性を向上させ得ることを見出した。よって、本発明は以下の［１］〜［８］に関する。 The inventors of the present invention have made extensive studies to solve the above problems. As a result, in the production of a catalyst for alkenyl acetate production, gold can be supported only on the support surface by preparing a catalyst using a mixed aqueous solution of a gold raw material salt and an alkali, and the activity or selectivity of the catalyst. It has been found that can be improved. Therefore, the present invention relates to the following [1] to [8].
［１］ 少なくとも以下の工程
工程１．担体にパラジウムまたは白金を含む化合物の溶液Ａを接触含浸させる工程
工程２．担体に少なくとも第１１族元素を含む化合物およびアルカリ性化合物の溶液Ｂを接触含浸させる工程
工程３．還元処理を行う工程および
工程４．担体に酢酸塩を担持する工程
を含み、工程１と工程２とを連続して行うことを特徴とする、少なくとも（ａ）担体、（ｂ）パラジウムまたは白金、（ｃ）第１１族元素および（ｄ）酢酸塩からなる酢酸アルケニル製造用触媒の製造方法。
[1] At least the following process steps 1. 1. Step of impregnating a carrier with a solution A of a compound containing palladium or platinum. 2. Step of impregnating a carrier with a solution B of an alkaline compound and a compound containing at least a Group 11 element Step of performing reduction treatment and step 4. Including a step of supporting acetate on a carrier, and performing Step 1 and Step 2 in succession, comprising at least (a) a carrier, (b) palladium or platinum, (c) a Group 11 element and ( d) A process for producing a catalyst for producing alkenyl acetate comprising an acetate.
［２］ 溶液Ａがさらに（ｅ）アルカリ土類金属元素を含む化合物を溶解していることを特徴とする、上記［１］に記載の酢酸アルケニル製造用触媒の製造方法。 [2] The method for producing a catalyst for producing alkenyl acetate according to the above [1], wherein the solution A further dissolves (e) a compound containing an alkaline earth metal element.
［３］ （ｂ）パラジウムまたは白金がパラジウムである、上記［１］または［２］に記載の酢酸アルケニル製造用触媒の製造方法。 [3] (b) The method for producing a catalyst for producing alkenyl acetate according to the above [1] or [2], wherein the palladium or platinum is palladium.
［４］ （ｃ）第１１族元素が金または銅である、上記［１］〜［３］のいずれかに記載の酢酸アルケニル製造用触媒の製造方法。 [4] (c) The method for producing a catalyst for alkenyl acetate production according to any one of the above [1] to [3], wherein the Group 11 element is gold or copper.
［５］ （ｅ）アルカリ土類金属元素がバリウム、ストロンチウム、マグネシウムおよびカルシウムから選ばれるすくなくとも１種である、上記［２］〜［４］のいずれかに記載の酢酸アルケニル製造用触媒の製造方法。 [5] (e) The process for producing a catalyst for alkenyl acetate production according to any one of the above [2] to [4], wherein the alkaline earth metal element is at least one selected from barium, strontium, magnesium and calcium .
［６］ 上記［１］〜［５］のいずれかに記載した方法で製造された触媒を用いることを特徴とする、低級オレフィン、酸素および酢酸を原料とする酢酸アルケニルの製造方法。 [6] A method for producing alkenyl acetate using a lower olefin, oxygen and acetic acid as raw materials, wherein the catalyst produced by the method according to any one of [1] to [5] is used.
［７］ 上記［１］〜［５］のいずれかに記載した方法で製造された触媒を用いることを特徴とする、エチレン、酸素および酢酸を原料とする酢酸ビニルの製造方法。 [7] A method for producing vinyl acetate using ethylene, oxygen and acetic acid as raw materials, wherein the catalyst produced by the method described in any one of [1] to [5] above is used.
［８］ 上記［１］〜［５］のいずれかに記載した方法で製造された触媒を用いることを特徴とする、プロピレン、酸素および酢酸を原料とする酢酸アリルの製造方法。 [8] A method for producing allyl acetate using propylene, oxygen and acetic acid as raw materials, wherein the catalyst produced by the method described in any one of [1] to [5] is used.
本発明の方法によれば、パラジウムと金をシェル型担持した触媒を簡便に製造することができ、かつ、従来の方法と比較して、得られる触媒の初期活性、選択性を向上させることができる。 According to the method of the present invention, a catalyst in which palladium and gold are supported on a shell type can be easily produced, and the initial activity and selectivity of the resulting catalyst can be improved as compared with the conventional method. it can.
以下に本発明の好ましい実施の形態について説明するが、本発明はこれらの形態のみに限定されるものではなく、本発明の精神とその実施の範囲内において様々な変形が可能であることを理解されたい。 Hereinafter, preferred embodiments of the present invention will be described. However, the present invention is not limited to these embodiments, and it is understood that various modifications can be made within the spirit and scope of the present invention. I want to be.
［触媒の製造工程］
本発明の酢酸アルケニル製造用触媒は以下に示す工程を含む方法によって製造できる。
工程１．担体にパラジウムまたは白金を含む化合物および、必要に応じて、アルカリ土類金属元素を含む化合物の溶液Ａを接触含浸させる工程
工程２．担体に第１１族元素を含む化合物およびアルカリ性化合物を含む溶液Ｂを接触含浸させる工程
工程３．還元処理を行う工程および
工程４．担体に酢酸塩を担持する工程
[Catalyst production process]
The catalyst for producing alkenyl acetate of the present invention can be produced by a method including the following steps.
Step 1. Step of contact impregnation with a solution A of a compound containing palladium or platinum on a support and, if necessary, a compound containing an alkaline earth metal element. 2. Step of impregnating a support B with a solution B containing a compound containing a Group 11 element and an alkaline compound Step of performing reduction treatment and step 4. A process of supporting acetate on a carrier
各工程は上記の順序で行うことが好ましい。ただし、工程１と工程２は続けて行う必要があり、これらの工程の間に他の工程を挟んではならない。工程４の酢酸塩を含浸する工程は最後でなくともよい。工程１で担体にアルカリ土類金属元素を担持しない場合は、溶液Ａにはアルカリ土類金属元素を含む化合物は含まれない。溶液Ａには他の成分が含まれていてもよい。工程３の還元処理は、パラジウムまたは白金を含む化合物を金属パラジウム、金属白金とするためであるので、工程２よりも後でなくてはならない。また、得られる触媒の性能を向上させる目的で、他の工程が含まれていてもよい。以下、各工程を詳細に説明する。 It is preferable to perform each process in said order. However, step 1 and step 2 need to be performed continuously, and other steps should not be sandwiched between these steps. The step of impregnating the acetate in step 4 may not be the last step. When no alkaline earth metal element is supported on the support in Step 1, the solution A does not contain a compound containing an alkaline earth metal element. The solution A may contain other components. Since the reduction treatment in step 3 is to convert the compound containing palladium or platinum into metal palladium or metal platinum, it must be performed after step 2. In addition, other steps may be included for the purpose of improving the performance of the obtained catalyst. Hereinafter, each process will be described in detail.
工程１．担体に溶液Ａを接触含浸させる工程
この工程では所定量の溶液Ａを担体に接触させる。実操作上は、溶液Ａを担体に含浸させる。この操作は常温で行うことができる。溶液Ａが担体に均一に接触含浸されるようにする。
Step 1. Step of contacting and impregnating carrier with solution A In this step, a predetermined amount of solution A is brought into contact with the carrier. In actual operation, the support is impregnated with the solution A. This operation can be performed at room temperature. Solution A is uniformly contact impregnated on the support.
＜（ａ）担体＞
本発明で用いる担体に特に制限はない。一般に触媒用の担体として用いられている多孔質物質であればよい。好ましくはシリカ、アルミナ、シリカ−アルミナ、珪藻土、モンモリロナイトまたはチタニア等が挙げられ、より好ましくはシリカである。担体としてシリカを主成分とするものを用いる場合には、担体のシリカ含量は、担体の重量に対して通常少なくとも５０質量％、好適には少なくとも９０質量％である。
<(A) Carrier>
There is no restriction | limiting in particular in the support | carrier used by this invention. Any porous material generally used as a carrier for a catalyst may be used. Silica, alumina, silica-alumina, diatomaceous earth, montmorillonite, titania and the like are preferable, and silica is more preferable. When a carrier containing silica as a main component is used as a carrier, the silica content of the carrier is usually at least 50% by weight, preferably at least 90% by weight, based on the weight of the carrier.
担体は、Ｂ．Ｅ．Ｔ．法で測定した比表面積が少なくとも０．０１ｍ２／ｇ以上、特に１０〜１０００ｍ２／ｇの範囲、とりわけ１００〜５００ｍ２／ｇの範囲であることが好ましい。また、吸水率は０．０５〜３ｇ／ｇ−担体、特に０．１〜２ｇ／ｇ−担体であることが好ましい。担体の細孔構造は、その平均細孔直径が１〜１０００ｎｍにあることが好ましく、特に好ましくは２〜８００ｎｍの範囲である。平気細孔直径が１ｎｍより小さいと、ガスの拡散が困難となることがある。また、細孔直径が１０００ｎｍより大きいと、担体の比表面積が小さくなりすぎて、触媒活性が低下する恐れがある。 The carrier is B.I. E. T.A. Law in the measured specific surface area of at least 0.01 m 2 / g or more, in particular in the range of 10 to 1000 m 2 / g, is preferably in the range of especially 100 to 500 m 2 / g. The water absorption is preferably 0.05 to 3 g / g-carrier, particularly 0.1 to 2 g / g-carrier. The pore structure of the carrier preferably has an average pore diameter of 1 to 1000 nm, particularly preferably in the range of 2 to 800 nm. If the flat pore diameter is smaller than 1 nm, gas diffusion may be difficult. On the other hand, if the pore diameter is larger than 1000 nm, the specific surface area of the support becomes too small, and the catalytic activity may be lowered.
ここで、担体の吸水率は、以下の測定方法で測定した数値をいう。
１．担体約５ｇを天秤で計量（Ｗ１ｇ）し、１００ｃｃのビーカーに入れる。
２．担体を完全に覆うように純水（イオン交換水）約１５ｍｌをビーカーに加える。
３．３０分間放置する。
４．金網上に担体と純水を空けて、純水をきる。
５．担体の表面に付着した水を、表面の光沢がなくなるまで紙タオル等で軽く押して、除去する。
６．担体＋純水の重さを測定する（Ｗ２ｇ）。
７．以下の式から担体の吸水率を算出する。
Here, the water absorption rate of the carrier is a numerical value measured by the following measuring method.
1. About 5 g of the carrier is weighed with a balance (W1 g) and placed in a 100 cc beaker.
2. About 15 ml of pure water (ion exchange water) is added to the beaker so as to completely cover the carrier.
3. Leave for 30 minutes.
4). Empty the carrier and pure water on the wire mesh and drain the pure water.
5. The water adhering to the surface of the carrier is removed by gently pressing with a paper towel or the like until the surface is no longer glossy.
6). The weight of carrier + pure water is measured (W2 g).
7). The water absorption rate of the carrier is calculated from the following formula.
吸水率（ｇ／ｇ−担体）＝（Ｗ２−Ｗ１）／Ｗ１
したがって、担体の吸水量（ｇ）は、担体の吸水率（ｇ／ｇ−担体）×使用した担体の重量（ｇ）により計算される。
Water absorption rate (g / g-carrier) = (W2-W1) / W1
Therefore, the water absorption amount (g) of the carrier is calculated by the water absorption rate of the carrier (g / g-carrier) × the weight (g) of the carrier used.
担体の形状には特に制限はない。具体的には、粉末状、球状、ペレット状等が挙げられるが、これらに限定されるものではない。 There is no restriction | limiting in particular in the shape of a support | carrier. Specific examples include powders, spheres, and pellets, but are not limited thereto.
用いられる担体の粒子直径に特に制限はない。好ましくは、１〜１０ｍｍの範囲であるのが好ましく、より好ましくは３〜８ｍｍである。管状反応器に触媒を充填して反応を行う場合、粒子直径が１ｍｍより小さいと、ガスを流通させるときに大きな圧力損失が生じ、有効にガス循環ができなくなる恐れがある。また、粒子直径が１０ｍｍより大きいと、管状反応器内へ充填される担持触媒の数が減少し、結果としてトータルの触媒表面積が小さくなり、担体の表面に偏在する触媒成分（Ｐｄ、Ａｕなど）が少なくなるため好ましくない。 There is no restriction | limiting in particular in the particle diameter of the support | carrier used. Preferably, it is in the range of 1 to 10 mm, more preferably 3 to 8 mm. When the reaction is carried out by filling the tubular reactor with a catalyst, if the particle diameter is smaller than 1 mm, a large pressure loss occurs when the gas is circulated, and there is a possibility that the gas cannot be effectively circulated. On the other hand, if the particle diameter is larger than 10 mm, the number of supported catalysts filled in the tubular reactor is reduced, resulting in a reduction in the total catalyst surface area and catalyst components (Pd, Au, etc.) unevenly distributed on the surface of the support. Is not preferred because of a decrease in
＜（ｂ）パラジウムまたは白金＞
（ｂ）パラジウムまたは白金は、主触媒成分であり、特に酢酸ビニル選択性が高いという点からパラジウムが好ましい。以下、パラジウムを例に説明するが、白金についても同様である。
<(B) Palladium or platinum>
(B) Palladium or platinum is the main catalyst component, and palladium is particularly preferred from the viewpoint of high vinyl acetate selectivity. Hereinafter, palladium will be described as an example, but the same applies to platinum.
本発明において、パラジウムはいずれの価数を持つものでも構わないが、好ましくは金属パラジウムである。「金属パラジウム」とは０価の価数を持つものである。金属パラジウムは、通常、２価および／または４価のパラジウムイオンを、還元剤であるヒドラジン、水素等を用いて還元することで得ることができる。その際、全てのパラジウムが、金属状態でなくても構わない。 In the present invention, palladium may have any valence, but is preferably metallic palladium. “Metallic palladium” has a valence of zero. Metallic palladium can be usually obtained by reducing divalent and / or tetravalent palladium ions using hydrazine, hydrogen or the like as a reducing agent. At that time, not all palladium may be in a metal state.
パラジウムの原料すなわちパラジウム元素を含む化合物には特に制限はない。金属パラジウムを用いることはもちろん、還元反応により金属パラジウムに転化可能なパラジウム塩を用いることも可能である。金属パラジウムに転化可能なパラジウム塩の例としては、塩化パラジウム、硝酸パラジウム、硫酸パラジウム、塩化パラジウム酸ナトリウム、塩化パラジウム酸カリウム、塩化パラジウム酸バリウム、酢酸パラジウムなどがあるが、これらに限定されるものではない。特に好適には塩化パラジウム酸ナトリウムが用いられる。 There is no particular limitation on the raw material of palladium, that is, the compound containing palladium element. In addition to using metal palladium, it is also possible to use a palladium salt that can be converted to metal palladium by a reduction reaction. Examples of palladium salts that can be converted to metallic palladium include, but are not limited to, palladium chloride, palladium nitrate, palladium sulfate, sodium chloropalladate, potassium chloropalladate, barium chloropalladate, and palladium acetate. is not. Particularly preferably, sodium chloropalladate is used.
白金の原料すなわち白金元素を含む化合物には特に制限はない。金属白金を用いることはもちろん、還元反応により金属白金に転化可能な白金塩を用いることも可能である。金属白金に転化可能な白金塩の例としては、塩化白金、硝酸白金、硫酸白金、塩化白金酸ナトリウム、塩化白金酸カリウム、塩化白金酸バリウム、酢酸白金などがあるが、これらに限定されるものではない。 There is no particular limitation on the raw material of platinum, that is, the compound containing platinum element. In addition to using metal platinum, it is also possible to use a platinum salt that can be converted to metal platinum by a reduction reaction. Examples of platinum salts that can be converted to metallic platinum include, but are not limited to, platinum chloride, platinum nitrate, platinum sulfate, sodium chloroplatinate, potassium chloroplatinate, barium chloroplatinate, and platinum acetate. is not.
（ｂ）パラジウムまたは白金と（ａ）担体との質量比は、好ましくは（ｂ）：（ａ）＝１：１０〜１０００であり、より好ましくは１：３０〜５００である。なお、例えば、パラジウム塩を担持する場合、この塩中のパラジウム元素の質量と担体の質量との比で計算する。 The mass ratio of (b) palladium or platinum to (a) support is preferably (b) :( a) = 1: 10 to 1000, more preferably 1:30 to 500. For example, when a palladium salt is supported, the calculation is performed based on the ratio of the mass of the palladium element in the salt to the mass of the carrier.
＜（ｅ）アルカリ土類金属元素＞
本発明に用いる（ｅ）アルカリ土類金属元素としては、Ｍｇ，Ｃａ，Ｂａ，Ｓｒなどが挙げられる。特に好適にはＢａである。
<(E) Alkaline earth metal element>
Examples of the (e) alkaline earth metal element used in the present invention include Mg, Ca, Ba, Sr and the like. Particularly preferred is Ba.
アルカリ土類金属元素は当該元素を含む化合物を供給源とするが、これらの化合物には特に制限はない。アルカリ土類金属元素の塩化物、酢酸塩、硝酸塩、硫酸塩、水酸化物などをそれぞれ調製条件によって選択することができる。特に好適には、ＢａＣｌ２、（ＣＨ３ＣＯＯ）２Ｂａ、Ｂａ（ＮＯ３）２、ＣａＣｌ２、（ＣＨ３ＣＯＯ）２Ｃａなどが挙げられる。 The alkaline earth metal element is supplied from a compound containing the element, but these compounds are not particularly limited. Alkaline earth metal chlorides, acetates, nitrates, sulfates, hydroxides, and the like can be selected depending on the preparation conditions. Particularly preferred are BaCl 2 , (CH 3 COO) 2 Ba, Ba (NO 3 ) 2 , CaCl 2 , (CH 3 COO) 2 Ca, and the like.
＜溶液Ａ＞
本発明に用いる溶液Ａは、パラジウムまたは白金を含む化合物の溶液である。アルカリ土類金属元素をも担持する場合には、アルカリ土類金属元素を含む化合物をも溶解したものである。必要に応じて他の成分が溶解されていてもよい。
<Solution A>
Solution A used in the present invention is a solution of a compound containing palladium or platinum. When an alkaline earth metal element is also supported, the compound containing the alkaline earth metal element is also dissolved. Other components may be dissolved as necessary.
溶液Ａは、塩化パラジウム酸、塩化パラジウム酸ナトリウムおよび塩化パラジウム酸カリウムから選ばれる少なくとも１種を含むことが好ましい。アルカリ土類金属元素をも担持する場合には、さらに塩化バリウム、酢酸バリウム、硝酸バリウム、硫酸バリウム、塩化ストロンチウム、酢酸ストロンチウム、硝酸ストロンチウム、硫酸ストロンチウム、塩化マグネシウム、酢酸マグネシウム、硝酸マグネシウム、硫酸マグネシウム、塩化カルシウム、酢酸カルシウム、硝酸カルシウムおよび硫酸カルシウムから選ばれる少なくとも１種を含むことが好ましい。 The solution A preferably contains at least one selected from chloropalladic acid, sodium chloropalladate and potassium chloropalladate. When also carrying alkaline earth metal elements, barium chloride, barium acetate, barium nitrate, barium sulfate, strontium chloride, strontium acetate, strontium nitrate, strontium sulfate, magnesium chloride, magnesium acetate, magnesium nitrate, magnesium sulfate, It is preferable to include at least one selected from calcium chloride, calcium acetate, calcium nitrate, and calcium sulfate.
溶液Ａの溶媒としては、水、アルコール、有機酸などが挙げられる。担体へのダメージや、含まれる化合物に対して反応性を有さない点から水が好ましい。
溶液Ａは、必要に応じて塩酸、硫酸、硝酸、リン酸、ヘテロポリ酸などの無機酸や、酢酸、シュウ酸、クエン酸などの有機酸を添加することで、ｐＨを調節されてもよい。好ましいｐＨは、０．５から３．０の範囲である。
Examples of the solvent of the solution A include water, alcohol, and organic acid. Water is preferable from the viewpoint of damage to the carrier and lack of reactivity with the contained compound.
The pH of the solution A may be adjusted by adding an inorganic acid such as hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, or heteropoly acid, or an organic acid such as acetic acid, oxalic acid, or citric acid as necessary. A preferred pH is in the range of 0.5 to 3.0.
溶液Ａを（ａ）担体に含浸させる方法には特に制限はないが、例えば、Ｉ）大量の溶液Ａに担体をしばらく浸漬させた後、吸水量分の溶液Ａを含浸させた担体を取り出す方法や、ＩＩ）パラジウムまたは白金を含む化合物および、必要に応じて、アルカリ土類金属元素を含む化合物を溶媒に溶解し、（ａ）担体の吸水量相当になるようにメスアップしたものを担体に含浸させる方法などが挙げられる。廃液処理の観点からはＩＩ）の方法が望ましい。溶液Ａは、（ａ）担体の吸水量相当の０．９〜１．０質量倍が（ａ）担体に含浸されていることが望ましい。 The method for impregnating the solution A into the carrier (a) is not particularly limited. For example, I) A method in which the carrier is immersed in a large amount of the solution A for a while and then the carrier impregnated with the solution A for the amount of water absorption is taken out. Or II) a compound containing palladium or platinum and, if necessary, a compound containing an alkaline earth metal element dissolved in a solvent, and (a) a carrier that is made up to a volume equivalent to the amount of water absorbed by the carrier. Examples of the method include impregnation. From the viewpoint of waste liquid treatment, the method II) is desirable. The solution A is preferably (a) impregnated in the carrier at 0.9 to 1.0 mass times equivalent to the water absorption amount of the carrier (a).
工程２．担体に溶液Ｂを接触含浸させる工程
＜（ｃ）第１１族元素＞
本発明において、（ｃ）第１１族元素とは、ＩＵＰＡＣ無機化学命名法改訂版（１９８９）による周期律表の第１１族元素を指す。具体的には金、銀、銅を指し、好ましくは金あるいは銅である。
Step 2. Step of contact impregnating support with solution B <(c) Group 11 element>
In the present invention, the (c) group 11 element refers to a group 11 element in the periodic table according to the revised IUPAC inorganic chemical nomenclature (1989). Specifically, it refers to gold, silver and copper, preferably gold or copper.
（ｃ）第１１族元素は、当該元素を含む化合物（以下においては、「第１１族元素前駆物質」ということがある）の形で担体に担持されるが、最終的には「金属状態」であることが好ましい。例えば、金を例にとると、ここで言う「金属状態」とは「金属金」を指し、０価の価数を持つものである。金属金は、通常、第１１族元素前駆物質由来の１価および／または３価の金イオンを、還元剤であるヒドラジン、水素等を用いて還元することで得ることができる。この際、全ての金が金属状態になくても構わない。 (C) The Group 11 element is supported on the carrier in the form of a compound containing the element (hereinafter, sometimes referred to as “Group 11 element precursor”). It is preferable that For example, taking gold as an example, the “metal state” here refers to “metal gold” and has a valence of zero. Metallic gold can usually be obtained by reducing monovalent and / or trivalent gold ions derived from a Group 11 element precursor using hydrazine, hydrogen or the like as a reducing agent. At this time, all the gold may not be in a metal state.
金や銅の原料すなわち第１１族元素を含む化合物には特に制限はない。金属金を用いることはもちろん、金属金に転化可能な金前駆体を用いることも可能である。金前駆体としては、塩化金酸や塩化金酸ナトリウム、塩化金酸カリウムなどが挙げられるが、好適には塩化金酸が用いられる。 There are no particular restrictions on the raw materials for gold and copper, that is, compounds containing Group 11 elements. It is possible to use a gold precursor that can be converted into metal gold as well as metal gold. Examples of the gold precursor include chloroauric acid, sodium chloroaurate, and potassium chloroaurate. Preferably, chloroauric acid is used.
＜アルカリ性化合物＞
本発明に用いるアルカリ性化合物は、いかなるアルカリ性の化合物であってもよい。例えば、アルカリ金属やアルカリ土類金属の水酸化物、アルカリ金属やアルカリ土類金属の重炭酸塩、アルカリ金属やアルカリ土類金属の炭酸塩、アルカリ金属やアルカリ土類金属のリン酸塩、アルカリ金属やアルカリ土類金属のケイ酸塩といったアルカリ性化合物が挙げられる。アルカリ金属としては、リチウム、ナトリウムおよびカリウムが用いられる。アルカリ土類金属としては、バリウムやストロンチウムが用いられる。好適には、メタケイ酸ナトリウム、メタケイ酸カリウム、水酸化ナトリウム、水酸化カリウム、水酸化バリウム、水酸化ストロンチウムなどが用いられる。
<Alkaline compound>
The alkaline compound used in the present invention may be any alkaline compound. For example, alkali metal or alkaline earth metal hydroxide, alkali metal or alkaline earth metal bicarbonate, alkali metal or alkaline earth metal carbonate, alkali metal or alkaline earth metal phosphate, alkali Alkaline compounds such as silicates of metals and alkaline earth metals can be mentioned. As the alkali metal, lithium, sodium and potassium are used. Barium or strontium is used as the alkaline earth metal. Preferably, sodium metasilicate, potassium metasilicate, sodium hydroxide, potassium hydroxide, barium hydroxide, strontium hydroxide and the like are used.
アルカリ性化合物は、前述の（ｂ）パラジウムまたは白金や（ｃ）第１１族元素の合計に対して過剰に使用する。例えば、アルカリ性化合物は、（ｂ）パラジウムまたは白金１モル当たり、好ましくは１〜３モル、より好ましくは１．２〜２．５モルの量で用いる。また、第１１族元素を含む化合物１モル当たり、好ましくは２〜１０モル、より好ましくは３〜８モルを使用する。 The alkaline compound is used in excess with respect to the total of the aforementioned (b) palladium or platinum and (c) Group 11 elements. For example, the alkaline compound is used in an amount of (b) 1 to 3 mol, more preferably 1.2 to 2.5 mol, per mol of palladium or platinum. In addition, 2 to 10 moles, more preferably 3 to 8 moles are used per mole of the compound containing a Group 11 element.
＜溶液Ｂ＞
本発明に用いる溶液Ｂは、第１１族元素を含む化合物およびアルカリ性化合物の溶液である。必要に応じて他の成分が溶解されていてもよい。
溶液Ｂの溶媒としては、水、メタノール、エタノールなどが挙げられる。好ましくは水である。
<Solution B>
The solution B used in the present invention is a solution of a compound containing a Group 11 element and an alkaline compound. Other components may be dissolved as necessary.
Examples of the solvent of the solution B include water, methanol, ethanol and the like. Preferably it is water.
溶液Ｂの量は、（ａ）担体の吸水量の１．０〜１０．０質量倍が好ましく、さらに好ましくは２．０〜８．０質量倍、もっとも好ましくは２．０〜５．０質量倍である。 The amount of the solution B is preferably 1.0 to 10.0 mass times (a) the water absorption amount of the carrier, more preferably 2.0 to 8.0 mass times, most preferably 2.0 to 5.0 mass times. Is double.
本発明では、溶液Ａが含浸された担体と溶液Ｂを接触させることで、原料金属塩を水不溶性物質に変換し、ＰｄやＡｕなどの金属成分が担体にシェル型に担持された触媒前駆体を形成することができる。その条件には制限はないが、接触時間は０．５〜１００時間、好適には３〜５０時間が望ましい。０．５時間未満では、触媒成分が所望の量担持されにくく、触媒性能が十分ではないことがある。また、１００時間より長時間接触させることで、（ａ）担体がダメージを受ける可能性があり、好ましくない。 In the present invention, a catalyst precursor in which a raw metal salt is converted into a water-insoluble substance by bringing the carrier impregnated with the solution A into contact with the solution B, and a metal component such as Pd or Au is supported on the carrier in a shell shape. Can be formed. The conditions are not limited, but the contact time is preferably 0.5 to 100 hours, preferably 3 to 50 hours. If it is less than 0.5 hour, a desired amount of the catalyst component is hardly supported, and the catalyst performance may not be sufficient. In addition, it is not preferable to contact the substrate for a longer time than 100 hours because (a) the carrier may be damaged.
接触温度は特に制限はないが、１０℃〜８０℃、好適には２０℃〜６０℃が望ましい。１０℃より低いと、変換反応が不十分になる可能性がある。８０℃を超えると、パラジウムや金の凝集が進む恐れがある。 The contact temperature is not particularly limited, but is preferably 10 ° C to 80 ° C, preferably 20 ° C to 60 ° C. If it is lower than 10 ° C, the conversion reaction may be insufficient. If it exceeds 80 ° C., the aggregation of palladium and gold may proceed.
工程３．還元処理を行う工程
溶液Ａが含浸された担体と溶液Ｂを接触させることで、原料金属塩を水不溶性物質に変換し、ＰｄやＡｕなどの金属成分が担体にシェル型に担持された触媒前駆体に対して還元処理を行い、前記化合物を金属パラジウム、金属金とする。還元処理は、液相還元、気相還元のいずれによることもできる。
Step 3. Step of performing reduction treatment By contacting the support impregnated with the solution A with the solution B, the raw metal salt is converted into a water-insoluble substance, and a catalyst precursor in which metal components such as Pd and Au are supported on the support in a shell shape. The body is subjected to a reduction treatment, and the compound is converted to metallic palladium or metallic gold. The reduction treatment can be performed by either liquid phase reduction or gas phase reduction.
液相還元は、アルコールや炭化水素類を用いた非水系、水系のいずれで行なわれてもよい。還元剤としては、カルボン酸およびその塩、アルデヒド、過酸化水素、糖類、多価フェノール、ジボラン、アミン、ヒドラジンなどが用いられる。カルボン酸およびその塩としてはシュウ酸、シュウ酸カリウム、ギ酸、ギ酸カリウム、クエン酸アンモニウムなどが例示され、糖類としてはグルコースが挙げられる。好ましい還元剤としてはヒドラジン、ホルムアルデヒド、アセトアルデヒド、ハイドロキノン、水素化ホウ素ナトリウム、クエン酸カリウムなどが挙げられ、最も好ましい還元剤はヒドラジンである。 The liquid phase reduction may be performed either in a non-aqueous system or an aqueous system using alcohol or hydrocarbons. As the reducing agent, carboxylic acid and its salt, aldehyde, hydrogen peroxide, saccharide, polyhydric phenol, diborane, amine, hydrazine and the like are used. Examples of carboxylic acids and salts thereof include oxalic acid, potassium oxalate, formic acid, potassium formate, ammonium citrate, and sugars include glucose. Preferred reducing agents include hydrazine, formaldehyde, acetaldehyde, hydroquinone, sodium borohydride, potassium citrate and the like, and the most preferred reducing agent is hydrazine.
気相還元に用いる還元剤は、水素、一酸化炭素、アルコール、アルデヒドや、エチレン、プロペン、イソブテンなどのオレフィンから選択される。好ましくは水素である。気相還元では希釈剤として、不活性ガスを加えてもよい。不活性ガスとしては、例えば、ヘリウム、アルゴン、窒素がある。 The reducing agent used for the gas phase reduction is selected from hydrogen, carbon monoxide, alcohol, aldehyde, and olefins such as ethylene, propene, and isobutene. Preferably it is hydrogen. In gas phase reduction, an inert gas may be added as a diluent. Examples of the inert gas include helium, argon, and nitrogen.
還元処理された担体には、必要に応じて純水等で洗浄を行う。洗浄は連続であるいはバッチで行われてもよい。洗浄温度は、好ましくは５〜２００℃の範囲、より好ましくは１５〜８０℃の範囲である。洗浄時間には特に制限はない。残存する好ましくない不純物の除去という目的に対して十分な条件を選択することができる。ここで、好ましくない不純物としてはナトリウムや塩素が挙げられる。 The reduced carrier is washed with pure water or the like as necessary. Washing may be performed continuously or batchwise. The washing temperature is preferably in the range of 5 to 200 ° C, more preferably in the range of 15 to 80 ° C. There is no particular limitation on the cleaning time. Conditions sufficient for the purpose of removing the remaining undesirable impurities can be selected. Here, sodium and chlorine are mentioned as an unpreferable impurity.
還元処理された担体には、必要に応じて酸を接触（以下、「酸処理」という）させてもよい。酸処理を行うことで、好ましくない不純物を除去し、特に（ｅ）アルカリ土類金属元素を添加した触媒では、過剰の（ｅ）アルカリ土類金属元素をある程度除去することで触媒性能が向上する。酸処理は、これらの物質を除去する目的を達成できる条件であればどのような条件で行ってもよい。特に、（ｅ）アルカリ土類金属元素は金属の分散状態を向上させる働きがあるが、触媒中に大量に存在する状態では、好ましくない副反応を引き起こす可能性があるため、余剰分を除去することが必要な場合がある。 The reduced carrier may be contacted with an acid (hereinafter referred to as “acid treatment”) as necessary. By performing an acid treatment, undesirable impurities are removed. In particular, in a catalyst to which (e) an alkaline earth metal element is added, the catalyst performance is improved by removing the excess (e) alkaline earth metal element to some extent. . The acid treatment may be performed under any conditions that can achieve the purpose of removing these substances. In particular, (e) the alkaline earth metal element works to improve the dispersion state of the metal, but in a state where the alkaline earth metal element is present in a large amount in the catalyst, it may cause an undesirable side reaction. Sometimes it is necessary.
酸処理の方法としては、担体を酸溶液に浸漬した後、水洗等によって酸溶液を洗い流す方法が挙げられる。
酸処理に使用される酸としては、塩酸、硫酸、硝酸、リン酸、ヘテロポリ酸などの無機酸や、酢酸、シュウ酸、クエン酸などの有機酸が挙げられる。これらの酸は、前述の目的を勘案して選択することができ、これらの酸の塩であってもかまわない。
Examples of the acid treatment method include a method of immersing the carrier in an acid solution and then washing off the acid solution by washing with water or the like.
Examples of the acid used for the acid treatment include inorganic acids such as hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, and heteropolyacid, and organic acids such as acetic acid, oxalic acid, and citric acid. These acids can be selected in view of the above-mentioned purpose, and salts of these acids may be used.
工程４．担体に酢酸塩を担持する工程
（ｄ）酢酸塩は、担体に（ｄ）酢酸塩の必要量を含む、好ましくは担体吸水量の０．９〜１質量倍の、溶液を含浸させ、乾燥することで担持される。担持するのは還元処理前でも後でもかまわない。好適には還元後である。
＜（ｄ）酢酸塩＞
本発明に用いる（ｄ）酢酸塩は、好ましくは、アルカリ金属酢酸塩およびアルカリ土類金属酢酸塩から選ばれる少なくとも１種の化合物である。より好ましくは、アルカリ金属酢酸塩である。具体的にはリチウム、ナトリウム、カリウムの酢酸塩などが挙げられる。なかでも酢酸ナトリウム、酢酸カリウムが好ましく、酢酸カリウムが特に好ましい。
Step 4. (D) Acetate is impregnated with a solution containing the necessary amount of (d) acetate, preferably 0.9 to 1 times the amount of water absorption of the carrier, and dried. It is supported by. It may be supported before or after the reduction treatment. Preferably after reduction.
<(D) Acetate>
The (d) acetate used in the present invention is preferably at least one compound selected from alkali metal acetates and alkaline earth metal acetates. More preferred is alkali metal acetate. Specific examples include lithium, sodium, and potassium acetate. Of these, sodium acetate and potassium acetate are preferable, and potassium acetate is particularly preferable.
＜触媒成分組成＞
本発明の酢酸アルケニル製造用触媒における（ｂ）パラジウムまたは白金、（ｃ）第１１族元素、（ｄ）酢酸塩、（ｅ）アルカリ土類金属元素の質量比は、好ましくは（ｂ）：（ｃ）：（ｄ）：（ｅ）＝１：０．００１〜１０：０．１〜１００：０〜１００であり、より好ましくは（ｂ）：（ｃ）：（ｄ）：（ｅ）＝１：０．１〜２：０．５〜２０：０〜３０である。なお、（ｂ）、（ｃ）、（ｅ）成分については、当該元素を含む化合物中の当該元素自体の質量（金属自体の場合はその金属の質量）、（ｄ）は酢酸塩の質量での組成比である。また、触媒が（ｅ）成分を含まない場合、（ｅ）成分の比は０である。
<Catalyst component composition>
The mass ratio of (b) palladium or platinum, (c) group 11 element, (d) acetate, (e) alkaline earth metal element in the catalyst for producing alkenyl acetate of the present invention is preferably (b) :( c) :( d) :( e) = 1: 0.001 to 10: 0.1 to 100: 0 to 100, more preferably (b) :( c) :( d) :( e) = It is 1: 0.1-2: 0.5-20: 0-30. In addition, about (b), (c), (e) component, the mass of the said element itself in the compound containing the said element (in the case of metal itself, the mass of the metal), (d) is the mass of acetate. It is a composition ratio. When the catalyst does not contain the component (e), the ratio of the component (e) is 0.
本発明の各触媒成分の原料化合物については、所望の触媒組成になるように各溶液中の量を調整する。各溶液中の触媒成分の原料化合物の濃度は、担体へ担持すべき原料化合物の量と溶液量とから計算することができる。実操作上は、まず、担体へ担持すべき原料化合物の所定量（ｇ数）をはかり取り、それを上記に例示したような溶液量となるように溶媒に溶かせばよい。
（ｂ）パラジウムまたは白金、（ｃ）第１１族元素、（ｄ）酢酸塩、（ｅ）アルカリ土類金属元素の（ａ）担体への担持量は、（ａ）担体１ｇあたり、（ｂ）０．００１〜０．０５ｇ、（ｃ）０．００１〜０．０５ｇ、（ｄ）０．０１〜１ｇ、（ｅ）０〜０．１ｇであるのが好ましい。
About the raw material compound of each catalyst component of this invention, the quantity in each solution is adjusted so that it may become a desired catalyst composition. The concentration of the raw material compound of the catalyst component in each solution can be calculated from the amount of the raw material compound to be supported on the carrier and the amount of the solution. In actual operation, first, a predetermined amount (g number) of the raw material compound to be supported on the carrier is weighed and dissolved in a solvent so as to obtain a solution amount as exemplified above.
(B) Palladium or platinum, (c) Group 11 element, (d) Acetate, (e) Alkaline earth metal element supported on (a) support is (b) per gram of support (a) It is preferable that they are 0.001-0.05g, (c) 0.001-0.05g, (d) 0.01-1g, (e) 0-0.1g.
本発明の方法により得られる触媒は、担体の表面部分に（ｂ）パラジウムまたは白金と（ｃ）第１１族元素の大部分が担持されたシェル構造（エッグシェル構造ともいう）をなしている。シェル部分の厚みは、用いる担体やアルカリ溶液、原料金属塩水溶液の種類によって変化する。直径５ｍｍの球体シリカを担体として使用した場合には、シェル部分は０．０５〜２ｍｍの厚みを有することが望ましい。さらに好適には０．１〜１ｍｍの厚みを有する。０．０５ｍｍ未満では、反応の間に担体表面部分のはがれなどによって活性低下が起こることがあるため望ましくない。２ｍｍより厚い場合には、シェル型担持のメリットが得られにくいことがある。
本発明の方法で調製した触媒においては、（ｄ）酢酸塩、（ｅ）アルカリ土類金属はシェル型に担持されていても、触媒全体に均一に存在していてもよい。
The catalyst obtained by the method of the present invention has a shell structure (also referred to as an egg shell structure) in which (b) palladium or platinum and (c) most of the Group 11 element are supported on the surface of the support. The thickness of the shell portion varies depending on the type of the carrier used, the alkaline solution, and the raw metal salt aqueous solution. When spherical silica having a diameter of 5 mm is used as the carrier, the shell portion preferably has a thickness of 0.05 to 2 mm. More preferably, it has a thickness of 0.1 to 1 mm. If it is less than 0.05 mm, the activity may decrease due to peeling of the surface portion of the carrier during the reaction, which is not desirable. If it is thicker than 2 mm, it may be difficult to obtain the advantage of carrying the shell type.
In the catalyst prepared by the method of the present invention, (d) acetate and (e) alkaline earth metal may be supported on the shell type or may exist uniformly throughout the catalyst.
＜触媒調製法の具体例＞
本発明の触媒調製法の例を、その工程順に、以下に示す。
工程１．（ｂ）パラジウムを含む化合物、必要に応じて（ｅ）アルカリ土類金属元素の原料金属塩および酸を純水に溶解し、さらに（ａ）担体吸水量相当分になるまで純水でメスアップして溶液Ａとし、この溶液Ａを（ａ）担体に含浸させる。
工程２．（ｃ）第１１族元素を含む化合物、アルカリ性化合物を純水に溶解し、さらに担体吸水量の２倍まで純水でメスアップして溶液Ｂとし、この溶液Ｂを（ａ）担体に接触含浸させ、触媒前駆体を形成する。
工程３．工程２の溶液に還元剤を投入する。
還元後の触媒前駆体を純水で洗浄する。
洗浄後の触媒前駆体を乾燥する。
工程４．触媒前駆体を（ｄ）酢酸塩溶液に浸漬し、乾燥する。
<Specific example of catalyst preparation method>
An example of the catalyst preparation method of the present invention is shown below in the order of the steps.
Step 1. (B) A compound containing palladium, and if necessary, (e) a raw metal salt of an alkaline earth metal element and an acid are dissolved in pure water, and (a) the volume is increased with pure water until the amount corresponding to the amount of water absorbed by the carrier. Then, the solution A is obtained, and (a) the carrier is impregnated with the solution A.
Step 2. (C) A compound containing a Group 11 element or an alkaline compound is dissolved in pure water, and further diluted with pure water to twice the amount of water absorbed by carrier to form solution B, and this solution B is contact impregnated on (a) the carrier. To form a catalyst precursor.
Step 3. A reducing agent is added to the solution of step 2.
The reduced catalyst precursor is washed with pure water.
The catalyst precursor after washing is dried.
Step 4. The catalyst precursor is immersed in (d) acetate solution and dried.
［酢酸アルケニルの製造］
以下、本発明で製造された酢酸アルケニル製造用触媒を用いた、酢酸アルケニルの製造法について説明する。本発明における酢酸アルケニルの製造のための反応は、酢酸、低級オレフィン、酸素を反応原料とし、気相で行うことが好ましい。
気相反応は、従来公知のいかなる形態で行ってもよいが、好ましくは固定床流通反応であることが望ましい。
[Production of alkenyl acetate]
Hereinafter, a method for producing alkenyl acetate using the alkenyl acetate production catalyst produced in the present invention will be described. The reaction for producing alkenyl acetate in the present invention is preferably carried out in the gas phase using acetic acid, lower olefin and oxygen as reaction raw materials.
The gas phase reaction may be performed in any conventionally known form, but is preferably a fixed bed flow reaction.
例えば、低級オレフィンがエチレンの場合には、反応式は次式のとおりである。
Ｃ２Ｈ４＋ＣＨ３ＣＯＯＨ＋１／２Ｏ２→ＣＨ２＝ＣＨＯＣＯＣＨ３＋Ｈ２Ｏ
原料の酢酸、低級オレフィン、酸素の比率は、モル比として酢酸：低級オレフィン：酸素＝１：０．０８〜１６：０．０１〜４であるのが好ましく、低級オレフィンがエチレンの場合は酢酸：エチレン：酸素＝１：０．２〜９：０．０７〜２であるのが好適である。また、低級オレフィンがプロピレンの場合は、酢酸：プロピレン: 酸素＝１：１〜１２：０．５〜２であるのが好ましい。
For example, when the lower olefin is ethylene, the reaction formula is as follows.
C 2 H 4 + CH 3 COOH + 1 / 2O 2 → CH 2 = CHOCOCH 3 + H 2 O
The ratio of acetic acid, lower olefin and oxygen as raw materials is preferably acetic acid: lower olefin: oxygen = 1: 0.08-16: 0.01-4 as a molar ratio. When the lower olefin is ethylene, acetic acid: It is preferred that ethylene: oxygen = 1: 0.2-9: 0.07-2. When the lower olefin is propylene, it is preferable that acetic acid: propylene: oxygen = 1: 1 to 12: 0.5 to 2.
反応原料ガスは、低級オレフィンと酢酸と酸素とを含み、さらに必要に応じて窒素、二酸化炭素または希ガスなどを希釈剤として含んでいてもよい。低級オレフィンと酢酸と酸素とを反応原料とすると、反応原料と希釈剤との比率は、モル比として反応原料：希釈剤＝１：０．０５〜９であるのが好ましく、より好ましくは反応原料：希釈剤＝１：０．１〜３である。 The reaction raw material gas contains a lower olefin, acetic acid, and oxygen, and may further contain nitrogen, carbon dioxide, or a rare gas as a diluent as necessary. When a lower olefin, acetic acid, and oxygen are used as reaction raw materials, the ratio of the reaction raw material to the diluent is preferably a reaction raw material: diluent = 1: 0.05 to 9, more preferably a reaction raw material. : Diluent = 1: 0.1-3.
固定床流通反応で反応を行う場合、反応原料ガスは、標準状態において、空間速度１０〜１５０００ｈｒ−１、特に３００〜８０００ｈｒ−１で反応器に通すのが好ましい。空間速度が１０ｈｒ−１より小さい場合、反応熱の除去が困難となる可能性がある。また、空間速度が１５０００ｈｒ−１より大きい場合、コンプレッサー等の設備が大きくなりすぎて、実用的でなくなることがある。 When the reaction is carried out in a fixed bed flow reaction, the reaction raw material gas, under standard conditions, space velocity 10～15000Hr -1, preferably particularly through the reactor at 300~8000hr -1. When the space velocity is smaller than 10 hr −1 , it may be difficult to remove reaction heat. Moreover, when space velocity is larger than 15000 hr < -1 >, equipment, such as a compressor, will become large and may become impractical.
反応原料ガス中には水を０．５〜２０ｍｏｌ％添加することが好ましい。さらに好適には、水を１〜１８ｍｏｌ％添加する。系内に水が存在することによって、理由は明かではないが、触媒からの（ｄ）酢酸塩の流出が減少する。一方、水を２０ｍｏｌ％より多く添加しても、上記効果は向上しないばかりか、酢酸アルケニルの加水分解が進む恐れがあるため、好ましくない。 It is preferable to add 0.5 to 20 mol% of water in the reaction raw material gas. More preferably, 1 to 18 mol% of water is added. The presence of water in the system reduces (d) acetate efflux from the catalyst for reasons that are not obvious. On the other hand, addition of water in an amount of more than 20 mol% is not preferable because the above effect is not improved and hydrolysis of alkenyl acetate may proceed.
反応器の材質については特に制限はないが、耐食性を有する材料で構成された反応器が好ましい。
反応温度は、１００〜３００℃であるのが好ましく、より好ましくは１２０〜２５０℃である。反応温度が１００℃より低い場合、反応速度が遅くなりすぎる可能性がある。反応温度が３００℃よりも高い場合、反応熱の除熱が困難となる可能性がある。
Although there is no restriction | limiting in particular about the material of a reactor, The reactor comprised with the material which has corrosion resistance is preferable.
The reaction temperature is preferably 100 to 300 ° C, more preferably 120 to 250 ° C. If the reaction temperature is lower than 100 ° C, the reaction rate may be too slow. When the reaction temperature is higher than 300 ° C., it may be difficult to remove the heat of reaction.
反応圧力は、好ましくは０〜３ＭＰａＧ（ゲージ圧）であり、より好ましくは０．１〜１．５ＭＰａＧである。反応圧力が０ＭＰａＧより小さい場合、反応速度が低下する恐れがあり、好ましくない。反応圧力が３ＭＰａＧより大きい場合、反応管等の設備が高価になり、実用的ではない。 The reaction pressure is preferably 0 to 3 MPaG (gauge pressure), more preferably 0.1 to 1.5 MPaG. If the reaction pressure is less than 0 MPaG, the reaction rate may decrease, which is not preferable. When the reaction pressure is larger than 3 MPaG, equipment such as a reaction tube becomes expensive, which is not practical.
反応原料のエチレン、プロピレン等の低級オレフィンには特に制限はない。一般的には高純度のものを用いることが好ましいが、メタン、エタン、プロパン等の低級飽和炭化水素が混入していても差し支えない。
また、酸素にも特に制限はない。窒素、炭酸ガス等の不活性ガスで希釈されたもの、例えば、空気の形でも供給できるが、反応ガスを循環させる場合には、一般には高濃度の酸素、好適には９９ＶＯＬ％以上の純度の酸素を用いる方が有利である。
There are no particular limitations on the lower olefins such as ethylene and propylene as reaction raw materials. In general, it is preferable to use a high-purity one, but it may be mixed with a lower saturated hydrocarbon such as methane, ethane, or propane.
Also, oxygen is not particularly limited. Although diluted with an inert gas such as nitrogen or carbon dioxide, for example, in the form of air, it can be supplied, but when the reaction gas is circulated, it generally has a high concentration of oxygen, preferably a purity of 99 VOL% or more. It is advantageous to use oxygen.
酢酸アルケニルとして酢酸ビニルを製造する場合、エチレンと酸素と酢酸とを反応させて、酢酸ビニルを製造する際の反応温度に特に制限はない。好ましくは１００〜３００℃であり、さらに好ましくは１２０℃〜２５０℃である。また、反応圧力は、設備の点から０．０〜３．０ＭＰａＧであることが実用上有利であるが、特に制限はない。より好ましくは０．１〜１．５ＭＰａＧの範囲である。 When vinyl acetate is produced as alkenyl acetate, there is no particular limitation on the reaction temperature for producing vinyl acetate by reacting ethylene, oxygen and acetic acid. Preferably it is 100-300 degreeC, More preferably, it is 120 degreeC-250 degreeC. Moreover, although it is practically advantageous that reaction pressure is 0.0-3.0 MPaG from the point of an installation, there is no restriction | limiting in particular. More preferably, it is the range of 0.1-1.5 MPaG.
反応混合ガスは、標準状態において、空間速度１０〜１５０００ｈｒ-1、特に３００〜８０００ｈｒ-1で反応器に通すのが好ましい。
反応形式としては、特に制限はなく、公知の方法、例えば、固定床、流動床などの形式を採り得る。好ましくは、耐蝕性を有する反応管に前述の触媒を充填した固定床を採用することが、実用上有利である。
The reaction gas mixture, at standard conditions, space velocity 10～15000Hr -1, preferably particularly through the reactor at 300~8000hr -1.
There is no restriction | limiting in particular as a reaction format, For example, formats, such as a fixed bed and a fluidized bed, can be taken. Preferably, it is practically advantageous to employ a fixed bed in which the above-described catalyst is packed in a reaction tube having corrosion resistance.
以下、実施例により本発明をさらに説明するが、本発明はこれらの実施例にのみ限定されるものではない。
実施例１ 触媒Ａの調製
シリカ球体担体（球体直径５ｍｍ、比表面積１５５ｍ２／ｇ、吸水率０．８５ｇ／ｇ−担体、上海海源化工科技有限公司のＨＳＶ−Ｉ）を用いて、触媒Ａを以下の手順で調製した。
EXAMPLES Hereinafter, although an Example demonstrates this invention further, this invention is not limited only to these Examples.
Preparation Silica spheres carrier catalyst of Example 1 A using (spherical diameter 5 mm, a specific surface area of 155m 2 / g, water absorption 0.85 g / g- carrier, HSV-I Shanghai sea source Chemical Technology Co., Ltd.), a catalyst A It was prepared by the following procedure.
工程１．シリカ球体担体２３ｇ（吸水量１９．７ｇ）に、５６質量％のＮａ２ＰｄＣｌ４水溶液１．５ｇを含む、担体吸水量相当の量の水溶液を含浸させた。担体と水溶液が入った容器を静かに振り動かし、溶液を完全に含浸させた。なお、吸水量は担体量２３ｇ、吸水率０．８５ｇ／ｇ−担体より計算した（以下の実施例、比較例でも同じ）。
工程２．工程１で得られた担体を、Ｎａ２ＳｉＯ３・９Ｈ２Ｏ２．５ｇおよび１７質量％のＨＡｕＣｌ４水溶液１．５ｇを含む、担体吸水量の２倍の水溶液に浸漬し、２０時間静置した。
Step 1. 23 g of silica sphere carrier (water absorption 19.7 g) was impregnated with an aqueous solution equivalent to the carrier water absorption amount containing 1.5 g of 56 mass% Na 2 PdCl 4 aqueous solution. The container containing the carrier and the aqueous solution was gently shaken to completely impregnate the solution. The water absorption was calculated from the carrier amount 23 g and the water absorption rate 0.85 g / g-carrier (the same applies to the following examples and comparative examples).
Step 2. The carrier obtained in Step 1 was immersed in an aqueous solution twice as much as the carrier water absorption amount containing 2.5 g of Na 2 SiO 3 .9H 2 O and 1.5 g of 17% by mass of HAuCl 4 aqueous solution, and allowed to stand for 20 hours. .
工程３．工程２の水溶液に５２質量％のヒドラジン水和物水溶液３．３ｍｌを加え、静かに混合し、室温で４時間静置した。このパラジウム／金／担体組成物を純水で洗浄し、水洗水に塩化物イオンが無くなるまで継続した。洗浄されたパラジウム／金／担体組成物を、約１１０℃で４時間乾燥した。
工程４．パラジウム／金／担体組成物に、担体吸水量相当の量の、２ｇの酢酸カリウムを含む水溶液を含浸させた後、約１１０℃で４時間乾燥した。
Step 3. To the aqueous solution of Step 2, 3.3 ml of a 52 mass% hydrazine hydrate aqueous solution was added, gently mixed, and allowed to stand at room temperature for 4 hours. This palladium / gold / carrier composition was washed with pure water and continued until the rinse water was free of chloride ions. The washed palladium / gold / support composition was dried at about 110 ° C. for 4 hours.
Step 4. The palladium / gold / carrier composition was impregnated with an aqueous solution containing 2 g of potassium acetate corresponding to the amount of water absorbed by the carrier, and then dried at about 110 ° C. for 4 hours.
実施例２ 触媒Ｂの調製
工程１．において、５６質量％のＮａ２ＰｄＣｌ４水溶液１．５ｇに、さらに０．５ＮのＨＣｌ７．０ｇを加えた、担体吸水量相当の量の水溶液を用いた。
これら以外は実施例１の操作を繰り返した。
Example 2 Preparation of Catalyst B Step 1. In Example 1, an aqueous solution corresponding to the amount of water absorbed by the carrier, in which 7.0 g of 0.5 N HCl was further added to 1.5 g of a 56 mass% Na 2 PdCl 4 aqueous solution, was used.
Except these, the operation of Example 1 was repeated.
実施例３ 触媒Ｃの調製
工程１．において、５６質量％のＮａ２ＰｄＣｌ４水溶液１．５ｇに、０．５ＮのＨＣｌ３．５ｇおよびＢａＣｌ２・２Ｈ２Ｏ１．1ｇを加えた、担体吸水量相当の量の水溶液を用いた。
これら以外は実施例１の操作を繰り返した。
Example 3 Preparation of Catalyst C Step 1. In Example 1, an aqueous solution having an amount corresponding to the amount of water absorbed by the carrier, in which 3.5 g of 0.5 N HCl and 1.1 g of BaCl 2 .2H 2 O were added to 1.5 g of a 56 mass% Na 2 PdCl 4 aqueous solution, was used.
Except these, the operation of Example 1 was repeated.
比較例１ 触媒Ｄの調製（従来技術の例）
シリカ球体担体（球体直径５ｍｍ、比表面積１５５ｍ２／ｇ、吸水率０．８５ｇ／ｇ−担体、上海海源化工科技有限公司のＨＳＶ−Ｉ）を用いて、触媒を以下の手順で調製した。
工程１．シリカ球体担体２３ｇ（吸水量１９．７ｇ）に、５６質量％のＮａ２ＰｄＣｌ４水溶液１．５ｇおよび１７質量％のＨＡｕＣｌ４水溶液１．５ｇを含む、担体吸水量相当（１倍）の量の水溶液を含浸させた。担体と水溶液が入った容器を静かに振り動かし、溶液を完全に含浸させた。
工程２．工程１で得られた担体を、Ｎａ２ＳｉＯ３・９Ｈ２Ｏを２．５ｇ含む、担体吸水量の２倍の量の水溶液に浸漬し、２０時間静置した。
Comparative Example 1 Preparation of Catalyst D (Example of Prior Art)
A catalyst was prepared by the following procedure using a silica sphere support (sphere diameter 5 mm, specific surface area 155 m 2 / g, water absorption 0.85 g / g-support, HSV-I from Shanghai Kaiyuan Chemical Co., Ltd.).
Step 1. The silica spheres carrier 23 g (water absorption amount 19.7 g), containing 56 wt% of Na 2 PdCl 4 solution 1.5g and 17% by weight of HAuCl 4 aqueous solution 1.5g, the amount of carrier water absorption equivalent (1X) Impregnated with aqueous solution. The container containing the carrier and the aqueous solution was gently shaken to completely impregnate the solution.
Step 2. The carrier obtained in step 1 was immersed in an aqueous solution containing 2.5 g of Na 2 SiO 3 .9H 2 O and having an amount twice the amount of water absorption of the carrier, and was allowed to stand for 20 hours.
工程３．工程２の水溶液に５２質量％のヒドラジン水和物水溶液３．３ｍｌを加え、静かに混合し、室温で４時間静置した。このパラジウム／金／担体組成物を純水で洗浄し、水洗水に塩化物イオンが無くなるまで継続した。洗浄されたパラジウム／金／担体組成物を、約１１０℃で４時間乾燥した。
工程４．パラジウム／金／担体組成物に、担体吸水量相当の量の、２ｇの酢酸カリウムを含む水溶液を含浸させた後、約１１０℃で４時間乾燥した。
Step 3. To the aqueous solution of Step 2, 3.3 ml of a 52 mass% hydrazine hydrate aqueous solution was added, gently mixed, and allowed to stand at room temperature for 4 hours. This palladium / gold / carrier composition was washed with pure water and continued until the rinse water was free of chloride ions. The washed palladium / gold / support composition was dried at about 110 ° C. for 4 hours.
Step 4. The palladium / gold / carrier composition was impregnated with an aqueous solution containing 2 g of potassium acetate corresponding to the amount of water absorbed by the carrier, and then dried at about 110 ° C. for 4 hours.
比較例２ 触媒Ｅの調製
工程１．において、５６質量％のＮａ２ＰｄＣｌ４水溶液１．５ｇおよび１７質量％のＨＡｕＣｌ４水溶液１．５ｇに、さらに０．５ＮのＨＣｌ３．５ｇおよびＢａＣｌ2・２Ｈ2Ｏ１．１ｇを加えた、担体吸水量相当の量の水溶液を用いた。
これ以外は比較例１の操作を繰り返した。
Comparative Example 2 Preparation of Catalyst E Step 1. In, 56 mass% of Na 2 PdCl 4 solution 1.5g and 17% by weight of HAuCl 4 aqueous solution 1.5g, further added HCl3.5g and BaCl 2 · 2H 2 O1.1g of 0.5 N, the carrier water An equivalent amount of aqueous solution was used.
Except this, the operation of Comparative Example 1 was repeated.
比較例３ 触媒Ｆの調製
シリカ球体担体（球体直径５ｍｍ、比表面積１５５ｍ２／ｇ、吸水率０．８５ｇ／ｇ−担体、上海海源化工科技有限公司のＨＳＶ−Ｉ）を用いて、触媒を以下の手順で調製した。
工程１．シリカ球体担体２３ｇ（吸水量１９．７ｇ）に、５６質量％のＮａ２ＰｄＣｌ４水溶液１．５ｇと０．５ＮのＨＣｌ７．０ｇとを加えた、担体吸水量相当の量の水溶液を含浸させた。担体と水溶液が入った容器を静かに振り動かし、溶液を完全に含浸させた。
Comparative Example 3 Preparation of Catalyst F Using a silica sphere support (sphere diameter 5 mm, specific surface area 155 m 2 / g, water absorption 0.85 g / g-support, HSV-I of Shanghai Haiyuan Chemical Co., Ltd.) It was prepared by the procedure.
Step 1. 23 g of silica sphere carrier (water absorption 19.7 g) was impregnated with an aqueous solution of an amount corresponding to the carrier water absorption amount by adding 1.5 g of 56 mass% Na 2 PdCl 4 aqueous solution and 7.0 g of 0.5 N HCl. . The container containing the carrier and the aqueous solution was gently shaken to completely impregnate the solution.
工程２．工程１で得られた担体を、Ｎａ２ＳｉＯ３・９Ｈ２Ｏ１．６ｇを含む、担体吸水量の２倍の量の水溶液に浸漬し、２０時間静置した。次いで、浸漬した水溶液から担体を取り出し、１００℃で１時間乾燥した。
工程２の２．工程２で得られた担体にＮａ２ＳｉＯ３・９Ｈ２Ｏ０．９ｇおよび１７質量％のＨＡｕＣｌ４水溶液１．５ｇを含む、担体吸水量相当の量の水溶液を含浸させ、１６時間静置した。
Step 2. The carrier obtained in Step 1 was immersed in an aqueous solution containing 1.6 g of Na 2 SiO 3 .9H 2 O and having an amount twice as much as the water absorption of the carrier, and was allowed to stand for 20 hours. Next, the carrier was taken out from the immersed aqueous solution and dried at 100 ° C. for 1 hour.
Step 2-2. The carrier obtained in Step 2 was impregnated with an aqueous solution equivalent to the amount of water absorbed by the carrier, including 0.9 g of Na 2 SiO 3 .9H 2 O and 1.5 g of 17 mass% HAuCl 4 aqueous solution, and allowed to stand for 16 hours.
工程３．工程２の２で得られた担体に担体吸水量の２倍の量の水を加え、さらに５２質量％ヒドラジン水和物水溶液３．３ｍｌを加え、静かに混合し、室温で４時間静置した。このパラジウム／金／担体組成物を純水で洗浄し、水洗水に塩化物イオンが無くなるまで洗浄を継続した。洗浄されたパラジウム／金／担体組成物を、約１１０℃で４時間乾燥した。
工程４．パラジウム／金／担体組成物に、担体吸水量相当の量の、２ｇの酢酸カリウムを溶解した水溶液を含浸させ、約１１０℃で４時間乾燥した。
Step 3. Water twice as much as the water absorption amount of the carrier was added to the carrier obtained in Step 2-2, and 3.3 ml of a 52% by mass hydrazine hydrate aqueous solution was added, mixed gently, and allowed to stand at room temperature for 4 hours. . This palladium / gold / carrier composition was washed with pure water, and washing was continued until no chloride ions were present in the washing water. The washed palladium / gold / support composition was dried at about 110 ° C. for 4 hours.
Step 4. The palladium / gold / carrier composition was impregnated with an aqueous solution of 2 g of potassium acetate in an amount corresponding to the amount of water absorbed by the carrier, and dried at about 110 ° C. for 4 hours.
実施例４ 触媒Ｇの調製
工程１．において、５６質量％のＮａ２ＰｄＣｌ４水溶液１．１ｇに、さらに０．５ＮのＨＣｌ７．０ｇを加えた、担体吸水量相当の量の水溶液を用いた。
工程２．工程１で得られた担体を、Ｎａ２ＳｉＯ３・９Ｈ２Ｏ２．５ｇおよび１７質量％のＨＡｕＣｌ４水溶液２．９ｇを含む、担体吸水量の２倍の水溶液に浸漬し、２０時間静置した。
これら以外は実施例１の操作を繰り返した。
Example 4 Preparation of Catalyst G Step 1. In Example 1, an aqueous solution having an amount equivalent to the amount of water absorbed by the carrier, in which 7.0 g of 0.5 N HCl was further added to 1.1 g of a 56 mass% Na 2 PdCl 4 aqueous solution.
Step 2. The carrier obtained in step 1 was immersed in an aqueous solution twice as much as the carrier water absorption amount containing 2.5 g of Na 2 SiO 3 .9H 2 O and 2.9 g of a 17% by mass HAuCl 4 aqueous solution, and allowed to stand for 20 hours. .
Except these, the operation of Example 1 was repeated.
［触媒の評価］
金属担持量の測定
担持触媒サンプル３ｇを粉砕し、内径３ｃｍのディスク状にプレスする。このディスクの金属量をフィリップス社製蛍光Ｘ線分析装置ＰＷ２４０４を用いて測定した。
金属表面積の測定
大倉理研株式会社製Ｒ６０１５を用いて、ＣＯパルス吸着法で測定した。
[Evaluation of catalyst]
Measurement of metal loading 3 g of the supported catalyst sample is pulverized and pressed into a disk shape having an inner diameter of 3 cm. The metal amount of the disk was measured using a fluorescent X-ray analyzer PW2404 manufactured by Philips.
Measurement of metal surface area Using a R6015 manufactured by Okura Riken Co., Ltd., measurement was performed by the CO pulse adsorption method.
初期活性評価試験Ａ
触媒３ｃｃをガラスビーズ７５ｃｃで希釈して反応管（ＳＵＳ３１６Ｌ製、内径２２ｍｍ、長さ４８０ｍｍ）に充填する。反応温度１５０℃、反応圧力０．６ＭＰａＧ、ガス組成Ｃ２Ｈ４／Ｏ２／Ｈ２Ｏ／ＨＯＡｃ／Ｎ２＝４７．３／６．１／５．６／２６．３／１４．７（ｍｏｌ％）のガスを流量２０ｎＬ／ｈで流通させ、反応を行った。
反応器出口ガスの分析を、以下の方法を用いて行った。
Initial activity evaluation test A
3 cc of catalyst is diluted with 75 cc of glass beads and filled into a reaction tube (manufactured by SUS316L, inner diameter 22 mm, length 480 mm). Reaction temperature 150 ° C., reaction pressure 0.6 MPaG, gas composition C 2 H 4 / O 2 / H 2 O / HOAc / N 2 = 47.3 / 6.1 / 5.6 / 26.3 / 14.7 ( mol%) gas was allowed to flow at a flow rate of 20 nL / h to carry out the reaction.
The reactor outlet gas was analyzed using the following method.
１．酸素
絶対検量線法を用い、流出ガスを５０ｍｌ採取し、ガスクロマトグラフィーに付属する１ｍｌのガスサンプラーに全量流し、以下の条件で分析を行った。
ガスクロマトグラフィー：島津ガスクロマトグラフ用ガスサンプラ−（ＭＧＳ−４：計量管１ｍｌ）付ガスクロマトグラフィー（島津製作所製ＧＣ−１４（Ｂ）
カラム：ＭＳ−５Ａ ＩＳ ６０／８０ｍｅｓｈ（３ｍｍΦ×３ｍ）
キャリアーガス：ヘリウム（流量２０ｍｌ／ｍｉｎ．）
温度条件：検出器温度、気化室温度が１１０℃、カラム温度は７０℃一定
検出器：ＴＣＤ（Ｈｅ圧７０ｋＰａＧ、Ｃｕｒｒｅｎｔ１００ｍ（Ａ）
1. Using an oxygen absolute calibration curve method, 50 ml of the effluent gas was sampled, and the entire amount was flowed to a 1 ml gas sampler attached to gas chromatography, and analysis was performed under the following conditions.
Gas chromatography: Shimadzu gas chromatograph gas sampler (MGS-4: measuring tube 1 ml) with gas chromatography (Shimadzu GC-14 (B)
Column: MS-5A IS 60/80 mesh (3 mmΦ × 3 m)
Carrier gas: helium (flow rate 20 ml / min.)
Temperature conditions: Detector temperature, vaporization chamber temperature is 110 ° C., column temperature is constant 70 ° C. Detector: TCD (He pressure 70 kPaG, Current 100 m (A)
２．酢酸
内部標準法を用い、反応液１０ｍｌに対し、内部標準として１，４−ジオキサンを１ｍｌ添加したものを分析液として、そのうちの０．２μｌを注入して以下の条件で分析を行った。
ガスクロマトグラフィー：島津製作所製ＧＣ−１４Ｂ
カラム：パックドカラムＴｈｅｒｍｏｎ ３０００（長さ３ｍ、内径０．３ｍｍ）
キャリアーガス：窒素（流量２０ｍｌ／ｍｉｎ．）
温度条件：検出器温度、気化室温度が１８０℃、カラム温度は分析開始から６分間は５０℃保持、その後１０℃／ｍｉｎの昇温速度で１５０℃まで昇温し、１５０℃で１０分間保持
検出器：ＦＩＤ（Ｈ2圧４０ｋＰａＧ、空気圧１００ｋＰａＧ）
2. The acetic acid internal standard method was used, and 10 ml of the reaction solution was added with 1 ml of 1,4-dioxane as an internal standard, and 0.2 μl was injected as an analysis solution, and analysis was performed under the following conditions.
Gas chromatography: Shimadzu GC-14B
Column: Packed column Thermon 3000 (length 3 m, inner diameter 0.3 mm)
Carrier gas: Nitrogen (flow rate 20 ml / min.)
Temperature conditions: Detector temperature, vaporization chamber temperature is 180 ° C, column temperature is kept at 50 ° C for 6 minutes from the start of analysis, then raised to 150 ° C at a rate of 10 ° C / min, and kept at 150 ° C for 10 minutes. Detector: FID (H 2 pressure 40 kPaG, air pressure 100 kPaG)
３．酢酸ビニル
内部標準法を用い、反応液６ｇに対し、内部標準として酢酸ｎ−プロピルを１ｇ添加したものを分析液として、そのうちの０．３μｌを注入して以下の条件で分析した。
ガスクロマトグラフィー：島津製作所製ＧＣ−９Ａ
カラム：キャピラリーカラムＴＣ−ＷＡＸ（長さ３０ｍ、内径０．２５ｍｍ、膜厚０．５μｍ）
キャリアーガス：窒素（流量３０ｍｌ／ｍｉｎ．）
温度条件：検出器温度、気化室温度が２００℃、カラム温度は分析開始から２分間は４５℃保持、その後４℃／ｍｉｎの昇温速度で１３０℃まで昇温し、１３０℃で１５分間保持し、その後２５℃／ｍｉｎの昇温速度で２００℃まで昇温し、２００℃で１０分間保持
検出器：ＦＩＤ（Ｈ2圧６０ｋＰａＧ、空気圧１００ｋＰａＧ）
触媒の初期活性評価結果を表１に示す。
3. Using vinyl acetate internal standard method, 0.3 μl of the resultant was added with 1 g of n-propyl acetate as an internal standard to 6 g of the reaction liquid, and analyzed under the following conditions.
Gas chromatography: Shimadzu GC-9A
Column: Capillary column TC-WAX (length 30 m, inner diameter 0.25 mm, film thickness 0.5 μm)
Carrier gas: Nitrogen (flow rate 30 ml / min.)
Temperature conditions: Detector temperature, vaporization chamber temperature is 200 ° C, column temperature is maintained at 45 ° C for 2 minutes from the start of analysis, then heated to 130 ° C at a temperature increase rate of 4 ° C / min, and maintained at 130 ° C for 15 minutes. Then, the temperature is increased to 200 ° C. at a temperature increase rate of 25 ° C./min and held at 200 ° C. for 10 minutes. Detector: FID (H 2 pressure 60 kPaG, air pressure 100 kPaG)
The initial activity evaluation results of the catalyst are shown in Table 1.
実施例１と比較例１については、酢酸ビニル活性の繰り返し実験誤差は５％であり、７００ｇ／Ｌ−ｃａｔ・ｈに対する絶対値は約３７ｇ／Ｌ−ｃａｔ・ｈとなり、実施例１と比較例１の酢酸ビニル活性は同等とみなすことができる。一方、選択率の実験誤差は絶対値で０．２％程度である。そこで、実施例１を比較例１と比較すると、実施例１は酢酸ビニル活性がほぼ同等で、選択率が高いことから、触媒性能が高いといえる。
実施例２では、工程１において塩酸を添加することにより、実施例１よりも酢酸ビニル活性が向上した。
実施例３と比較例２については、選択率の実験誤差は絶対値で０．２％である。実施例３と比較例２の選択率はおおよそ同等とみなすことができる。比較例２と比較すると、実施例３は酢酸ビニル選択率がほぼ同等で、活性が明らかに高いことから、触媒性能が高いといえる。
比較例３の触媒は、従来技術（特許文献２）の方法で製造された触媒である。担持された成分の質と量が等しい実施例２の触媒と比較すると、酢酸ビニル選択率は同程度であるが、酢酸ビニル活性は大きく劣っていることがわかる。
For Example 1 and Comparative Example 1, the repeated experimental error of vinyl acetate activity is 5%, and the absolute value for 700 g / L-cat · h is about 37 g / L-cat · h. Example 1 and Comparative Example A vinyl acetate activity of 1 can be considered equivalent. On the other hand, the experimental error in selectivity is about 0.2% in absolute value. Therefore, when Example 1 is compared with Comparative Example 1, it can be said that Example 1 has high catalytic performance because it has almost the same vinyl acetate activity and high selectivity.
In Example 2, vinyl acetate activity was improved as compared with Example 1 by adding hydrochloric acid in Step 1.
For Example 3 and Comparative Example 2, the experimental error in selectivity is 0.2% in absolute value. The selectivity of Example 3 and Comparative Example 2 can be regarded as approximately equivalent. Compared to Comparative Example 2, it can be said that Example 3 has high catalytic performance because Example 3 has almost the same vinyl acetate selectivity and clearly high activity.
The catalyst of Comparative Example 3 is a catalyst produced by the method of the prior art (Patent Document 2). Compared to the catalyst of Example 2 where the quality and quantity of the supported components are equal, it can be seen that the vinyl acetate selectivity is similar but the vinyl acetate activity is greatly inferior.
本発明は、初期活性および選択性に優れる酢酸アルケニル製造用触媒を提供することができ、産業上有用である。 INDUSTRIAL APPLICABILITY The present invention can provide a catalyst for producing alkenyl acetate having excellent initial activity and selectivity, and is industrially useful.
Claims (8)
工程１．担体にパラジウムまたは白金を含む化合物の溶液Ａを接触含浸させる工程
工程２．担体に少なくとも第１１族元素を含む化合物およびアルカリ性化合物の溶液Ｂを接触含浸させる工程
工程３．還元処理を行う工程および
工程４．担体に酢酸塩を担持する工程
を含み、工程１と工程２とを連続して行うことを特徴とする、少なくとも（ａ）担体、（ｂ）パラジウムまたは白金、（ｃ）第１１族元素および（ｄ）酢酸塩からなる酢酸アルケニル製造用触媒の製造方法。 At least the following process steps 1. 1. Step of impregnating a carrier with a solution A of a compound containing palladium or platinum. 2. Step of impregnating a carrier with a solution B of an alkaline compound and a compound containing at least a Group 11 element Step of performing reduction treatment and step 4. Including a step of supporting acetate on a carrier, and performing Step 1 and Step 2 in succession, comprising at least (a) a carrier, (b) palladium or platinum, (c) a Group 11 element and ( d) A process for producing a catalyst for producing alkenyl acetate comprising an acetate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2008043176A JP4964170B2 (en) | 2007-04-09 | 2008-02-25 | Method for producing catalyst for producing alkenyl acetate |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2007101765 | 2007-04-09 | ||
| JP2007101765 | 2007-04-09 | ||
| JP2008043176A JP4964170B2 (en) | 2007-04-09 | 2008-02-25 | Method for producing catalyst for producing alkenyl acetate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2008279432A true JP2008279432A (en) | 2008-11-20 |
| JP4964170B2 JP4964170B2 (en) | 2012-06-27 |
Family
ID=40140708
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2008043176A Active JP4964170B2 (en) | 2007-04-09 | 2008-02-25 | Method for producing catalyst for producing alkenyl acetate |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP4964170B2 (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0291045A (en) * | 1988-09-29 | 1990-03-30 | Showa Denko Kk | Production of allyl acetate |
| JPH07308576A (en) * | 1993-11-19 | 1995-11-28 | Bp Chem Internatl Ltd | Preparation of catalyst for use in manufacture of vinyl acetate |
| JP2001521817A (en) * | 1997-10-30 | 2001-11-13 | セラニーズ・インターナショナル・コーポレーション | Method for preparing vinyl acetate utilizing a catalyst comprising palladium, gold, and a certain third metal |
| JP2002503545A (en) * | 1998-02-20 | 2002-02-05 | セラニーズ・インターナショナル・コーポレーション | Production method of vinyl acetate catalyst |
| JP2003513788A (en) * | 1999-11-17 | 2003-04-15 | セラニーズ・インターナショナル・コーポレーション | Vinyl acetate catalyst containing palladium metal and gold prepared using sonication |
| JP2003525723A (en) * | 1997-10-28 | 2003-09-02 | セラニーズ・インターナショナル・コーポレーション | Catalyst for vinyl acetate containing metallic palladium and gold and copper acetate |
| JP2004339195A (en) * | 2003-03-07 | 2004-12-02 | Showa Denko Kk | Method for producing lower aliphatic alkenyl carboxylate and alkenyl alcohol and lower aliphatic alkenyl carboxylate and alkenyl alcohol produced by the same |
-
2008
- 2008-02-25 JP JP2008043176A patent/JP4964170B2/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0291045A (en) * | 1988-09-29 | 1990-03-30 | Showa Denko Kk | Production of allyl acetate |
| JPH07308576A (en) * | 1993-11-19 | 1995-11-28 | Bp Chem Internatl Ltd | Preparation of catalyst for use in manufacture of vinyl acetate |
| JP2003525723A (en) * | 1997-10-28 | 2003-09-02 | セラニーズ・インターナショナル・コーポレーション | Catalyst for vinyl acetate containing metallic palladium and gold and copper acetate |
| JP2001521817A (en) * | 1997-10-30 | 2001-11-13 | セラニーズ・インターナショナル・コーポレーション | Method for preparing vinyl acetate utilizing a catalyst comprising palladium, gold, and a certain third metal |
| JP2002503545A (en) * | 1998-02-20 | 2002-02-05 | セラニーズ・インターナショナル・コーポレーション | Production method of vinyl acetate catalyst |
| JP2003513788A (en) * | 1999-11-17 | 2003-04-15 | セラニーズ・インターナショナル・コーポレーション | Vinyl acetate catalyst containing palladium metal and gold prepared using sonication |
| JP2004339195A (en) * | 2003-03-07 | 2004-12-02 | Showa Denko Kk | Method for producing lower aliphatic alkenyl carboxylate and alkenyl alcohol and lower aliphatic alkenyl carboxylate and alkenyl alcohol produced by the same |
Also Published As
| Publication number | Publication date |
|---|---|
| JP4964170B2 (en) | 2012-06-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP4969501B2 (en) | Method for producing a catalyst for the production of allyl acetate | |
| JP6366841B2 (en) | Method for producing allyl acetate | |
| TWI793721B (en) | Method for producing catalyst for producing vinyl acetate and method for producing vinyl acetate | |
| JP4925956B2 (en) | Method for producing catalyst for producing alkenyl acetate | |
| RU2282499C2 (en) | Catalyst preparation process, catalyst, and a method for using this catalyst | |
| KR101017904B1 (en) | Process for production of catalyst for alkenyl acetate production | |
| JP3373472B2 (en) | Catalyst for acyloxylation reaction and its use | |
| JP4551109B2 (en) | Catalyst production method | |
| JP4964170B2 (en) | Method for producing catalyst for producing alkenyl acetate | |
| JP7314712B2 (en) | Method for producing catalyst for producing allyl acetate | |
| JP4963922B2 (en) | Method for producing catalyst for producing alkenyl acetate | |
| TWI845399B (en) | Method for producing catalyst for producing vinyl acetate and method for producing vinyl acetate | |
| JP2010247104A (en) | Method for producing catalyst for producing alkenyl acetate | |
| WO2024057789A1 (en) | Method for producing catalyst for vinyl acetate production and method for producing vinyl acetate | |
| JP2021037429A (en) | Method for selecting catalyst for production of alkenyl acetate | |
| JP2003212824A (en) | Method of producing vinyl acetate and vinyl acetate that is produced through the production process | |
| JP2009220099A (en) | Method for producing catalyst for production of lower aliphatic carboxylic acid |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20101101 |
|
| A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20120217 |
|
| TRDD | Decision of grant or rejection written | ||
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20120228 |
|
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 |
|
| A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20120327 |
|
| R150 | Certificate of patent or registration of utility model |
Ref document number: 4964170 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20150406 Year of fee payment: 3 |
|
| S111 | Request for change of ownership or part of ownership |
Free format text: JAPANESE INTERMEDIATE CODE: R313111 |
|
| R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
| S531 | Written request for registration of change of domicile |
Free format text: JAPANESE INTERMEDIATE CODE: R313531 |
|
| R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |