TW201219112A - Catalyst for the oxidation of o-xylene and/or naphthalene to phthalic anhydride - Google Patents
Catalyst for the oxidation of o-xylene and/or naphthalene to phthalic anhydride Download PDFInfo
- Publication number
- TW201219112A TW201219112A TW100127132A TW100127132A TW201219112A TW 201219112 A TW201219112 A TW 201219112A TW 100127132 A TW100127132 A TW 100127132A TW 100127132 A TW100127132 A TW 100127132A TW 201219112 A TW201219112 A TW 201219112A
- Authority
- TW
- Taiwan
- Prior art keywords
- catalyst
- oxidation
- naphthalene
- content
- xylene
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 56
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 27
- 230000003647 oxidation Effects 0.000 title claims abstract description 26
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 title claims abstract description 22
- LGRFSURHDFAFJT-UHFFFAOYSA-N Phthalic anhydride Natural products C1=CC=C2C(=O)OC(=O)C2=C1 LGRFSURHDFAFJT-UHFFFAOYSA-N 0.000 title claims abstract description 14
- JHIWVOJDXOSYLW-UHFFFAOYSA-N butyl 2,2-difluorocyclopropane-1-carboxylate Chemical compound CCCCOC(=O)C1CC1(F)F JHIWVOJDXOSYLW-UHFFFAOYSA-N 0.000 title claims abstract description 14
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical group CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 title abstract description 29
- 229940078552 o-xylene Drugs 0.000 title abstract description 12
- ADCOVFLJGNWWNZ-UHFFFAOYSA-N antimony trioxide Inorganic materials O=[Sb]O[Sb]=O ADCOVFLJGNWWNZ-UHFFFAOYSA-N 0.000 claims abstract description 30
- 239000007789 gas Substances 0.000 claims abstract description 17
- 238000000034 method Methods 0.000 claims abstract description 8
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 6
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 6
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 6
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims abstract description 5
- 229910001882 dioxygen Inorganic materials 0.000 claims abstract description 5
- 239000000126 substance Substances 0.000 claims description 13
- OIAQMFOKAXHPNH-UHFFFAOYSA-N 1,2-diphenylbenzene Chemical compound C1=CC=CC=C1C1=CC=CC=C1C1=CC=CC=C1 OIAQMFOKAXHPNH-UHFFFAOYSA-N 0.000 claims description 5
- 238000000634 powder X-ray diffraction Methods 0.000 claims description 5
- 239000000843 powder Substances 0.000 claims description 4
- YXFVVABEGXRONW-UHFFFAOYSA-N toluene Substances CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 4
- 238000006243 chemical reaction Methods 0.000 abstract description 4
- GHPGOEFPKIHBNM-UHFFFAOYSA-N antimony(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Sb+3].[Sb+3] GHPGOEFPKIHBNM-UHFFFAOYSA-N 0.000 abstract 4
- 239000000203 mixture Substances 0.000 description 40
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 37
- 239000000725 suspension Substances 0.000 description 12
- 239000004408 titanium dioxide Substances 0.000 description 12
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 9
- 229910052797 bismuth Inorganic materials 0.000 description 9
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 description 9
- 150000003839 salts Chemical class 0.000 description 9
- 238000004519 manufacturing process Methods 0.000 description 8
- 239000000454 talc Substances 0.000 description 8
- 229910052623 talc Inorganic materials 0.000 description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 7
- 230000003197 catalytic effect Effects 0.000 description 7
- GNTDGMZSJNCJKK-UHFFFAOYSA-N divanadium pentaoxide Chemical compound O=[V](=O)O[V](=O)=O GNTDGMZSJNCJKK-UHFFFAOYSA-N 0.000 description 7
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 5
- 229910000420 cerium oxide Inorganic materials 0.000 description 5
- -1 oxidizing planers Chemical class 0.000 description 5
- BMMGVYCKOGBVEV-UHFFFAOYSA-N oxo(oxoceriooxy)cerium Chemical compound [Ce]=O.O=[Ce]=O BMMGVYCKOGBVEV-UHFFFAOYSA-N 0.000 description 5
- 239000011230 binding agent Substances 0.000 description 4
- 239000011248 coating agent Substances 0.000 description 4
- 238000000576 coating method Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 229910052698 phosphorus Inorganic materials 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 229910052787 antimony Inorganic materials 0.000 description 3
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 3
- 238000001354 calcination Methods 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- XNGIFLGASWRNHJ-UHFFFAOYSA-N o-dicarboxybenzene Natural products OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- 239000011574 phosphorus Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical compound O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 description 3
- UYPYRKYUKCHHIB-UHFFFAOYSA-N trimethylamine N-oxide Chemical compound C[N+](C)(C)[O-] UYPYRKYUKCHHIB-UHFFFAOYSA-N 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 2
- 235000011054 acetic acid Nutrition 0.000 description 2
- 239000013543 active substance Substances 0.000 description 2
- MWPLVEDNUUSJAV-UHFFFAOYSA-N anthracene Chemical compound C1=CC=CC2=CC3=CC=CC=C3C=C21 MWPLVEDNUUSJAV-UHFFFAOYSA-N 0.000 description 2
- LJCFOYOSGPHIOO-UHFFFAOYSA-N antimony pentoxide Chemical compound O=[Sb](=O)O[Sb](=O)=O LJCFOYOSGPHIOO-UHFFFAOYSA-N 0.000 description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 2
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 description 2
- 229910000416 bismuth oxide Inorganic materials 0.000 description 2
- 150000001244 carboxylic acid anhydrides Chemical class 0.000 description 2
- 150000001735 carboxylic acids Chemical class 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- TYIXMATWDRGMPF-UHFFFAOYSA-N dibismuth;oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Bi+3].[Bi+3] TYIXMATWDRGMPF-UHFFFAOYSA-N 0.000 description 2
- AXTYOFUMVKNMLR-UHFFFAOYSA-N dioxobismuth Chemical compound O=[Bi]=O AXTYOFUMVKNMLR-UHFFFAOYSA-N 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 229930004069 diterpene Natural products 0.000 description 2
- 150000004141 diterpene derivatives Chemical class 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 150000004679 hydroxides Chemical class 0.000 description 2
- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 239000004337 magnesium citrate Substances 0.000 description 2
- 229960005336 magnesium citrate Drugs 0.000 description 2
- 235000002538 magnesium citrate Nutrition 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-L phthalate(2-) Chemical compound [O-]C(=O)C1=CC=CC=C1C([O-])=O XNGIFLGASWRNHJ-UHFFFAOYSA-L 0.000 description 2
- 229910052707 ruthenium Inorganic materials 0.000 description 2
- WOCIAKWEIIZHES-UHFFFAOYSA-N ruthenium(iv) oxide Chemical compound O=[Ru]=O WOCIAKWEIIZHES-UHFFFAOYSA-N 0.000 description 2
- 239000001117 sulphuric acid Substances 0.000 description 2
- 235000011149 sulphuric acid Nutrition 0.000 description 2
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 2
- PLSARIKBYIPYPF-UHFFFAOYSA-H trimagnesium dicitrate Chemical compound [Mg+2].[Mg+2].[Mg+2].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O.[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O PLSARIKBYIPYPF-UHFFFAOYSA-H 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 229910052720 vanadium Inorganic materials 0.000 description 2
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 2
- 239000000052 vinegar Substances 0.000 description 2
- 235000021419 vinegar Nutrition 0.000 description 2
- 239000008096 xylene Substances 0.000 description 2
- WOAHJDHKFWSLKE-UHFFFAOYSA-N 1,2-benzoquinone Chemical compound O=C1C=CC=CC1=O WOAHJDHKFWSLKE-UHFFFAOYSA-N 0.000 description 1
- AHBGXHAWSHTPOM-UHFFFAOYSA-N 1,3,2$l^{4},4$l^{4}-dioxadistibetane 2,4-dioxide Chemical compound O=[Sb]O[Sb](=O)=O AHBGXHAWSHTPOM-UHFFFAOYSA-N 0.000 description 1
- XDJWZONZDVNKDU-UHFFFAOYSA-N 1314-24-5 Chemical compound O=POP=O XDJWZONZDVNKDU-UHFFFAOYSA-N 0.000 description 1
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- KKMOSYLWYLMHAL-UHFFFAOYSA-N 2-bromo-6-nitroaniline Chemical compound NC1=C(Br)C=CC=C1[N+]([O-])=O KKMOSYLWYLMHAL-UHFFFAOYSA-N 0.000 description 1
- ZUGAOYSWHHGDJY-UHFFFAOYSA-K 5-hydroxy-2,8,9-trioxa-1-aluminabicyclo[3.3.2]decane-3,7,10-trione Chemical compound [Al+3].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O ZUGAOYSWHHGDJY-UHFFFAOYSA-K 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 239000004254 Ammonium phosphate Substances 0.000 description 1
- 239000005711 Benzoic acid Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 229910052684 Cerium Inorganic materials 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 241000270295 Serpentes Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- LMAYBWHOGIBOSQ-UHFFFAOYSA-N [Ce+5] Chemical class [Ce+5] LMAYBWHOGIBOSQ-UHFFFAOYSA-N 0.000 description 1
- XHCLAFWTIXFWPH-UHFFFAOYSA-N [O-2].[O-2].[O-2].[O-2].[O-2].[V+5].[V+5] Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[V+5].[V+5] XHCLAFWTIXFWPH-UHFFFAOYSA-N 0.000 description 1
- 150000001242 acetic acid derivatives Chemical class 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 229910000148 ammonium phosphate Inorganic materials 0.000 description 1
- 235000019289 ammonium phosphates Nutrition 0.000 description 1
- 150000008064 anhydrides Chemical class 0.000 description 1
- 229910000411 antimony tetroxide Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- UNTBPXHCXVWYOI-UHFFFAOYSA-O azanium;oxido(dioxo)vanadium Chemical compound [NH4+].[O-][V](=O)=O UNTBPXHCXVWYOI-UHFFFAOYSA-O 0.000 description 1
- 235000010233 benzoic acid Nutrition 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- DJIGQKWBFJTLNH-UHFFFAOYSA-H bis(1,5-dioxo-2,4,3-benzodioxabismepin-3-yl) benzene-1,2-dicarboxylate Chemical compound [Bi+3].[Bi+3].[O-]C(=O)c1ccccc1C([O-])=O.[O-]C(=O)c1ccccc1C([O-])=O.[O-]C(=O)c1ccccc1C([O-])=O DJIGQKWBFJTLNH-UHFFFAOYSA-H 0.000 description 1
- WMWLMWRWZQELOS-UHFFFAOYSA-N bismuth(III) oxide Inorganic materials O=[Bi]O[Bi]=O WMWLMWRWZQELOS-UHFFFAOYSA-N 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 229910052792 caesium Inorganic materials 0.000 description 1
- TVFDJXOCXUVLDH-UHFFFAOYSA-N caesium atom Chemical compound [Cs] TVFDJXOCXUVLDH-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical class OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- GWXLDORMOJMVQZ-UHFFFAOYSA-N cerium Chemical compound [Ce] GWXLDORMOJMVQZ-UHFFFAOYSA-N 0.000 description 1
- 150000001785 cerium compounds Chemical class 0.000 description 1
- ITZXULOAYIAYNU-UHFFFAOYSA-N cerium(4+) Chemical compound [Ce+4] ITZXULOAYIAYNU-UHFFFAOYSA-N 0.000 description 1
- 229910000423 chromium oxide Inorganic materials 0.000 description 1
- 229910000428 cobalt oxide Inorganic materials 0.000 description 1
- IVMYJDGYRUAWML-UHFFFAOYSA-N cobalt(ii) oxide Chemical compound [Co]=O IVMYJDGYRUAWML-UHFFFAOYSA-N 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- GLVVKKSPKXTQRB-UHFFFAOYSA-N ethenyl dodecanoate Chemical compound CCCCCCCCCCCC(=O)OC=C GLVVKKSPKXTQRB-UHFFFAOYSA-N 0.000 description 1
- VXNZUUAINFGPBY-UHFFFAOYSA-N ethyl ethylene Natural products CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 238000010574 gas phase reaction Methods 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 229910052732 germanium Inorganic materials 0.000 description 1
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 239000013029 homogenous suspension Substances 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 1
- 150000002690 malonic acid derivatives Chemical class 0.000 description 1
- NFFIWVVINABMKP-UHFFFAOYSA-N methylidynetantalum Chemical compound [Ta]#C NFFIWVVINABMKP-UHFFFAOYSA-N 0.000 description 1
- 229910000476 molybdenum oxide Inorganic materials 0.000 description 1
- 229910000480 nickel oxide Inorganic materials 0.000 description 1
- 229910052758 niobium Inorganic materials 0.000 description 1
- 239000010955 niobium Substances 0.000 description 1
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 description 1
- QGLKJKCYBOYXKC-UHFFFAOYSA-N nonaoxidotritungsten Chemical compound O=[W]1(=O)O[W](=O)(=O)O[W](=O)(=O)O1 QGLKJKCYBOYXKC-UHFFFAOYSA-N 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 150000003891 oxalate salts Chemical class 0.000 description 1
- PQQKPALAQIIWST-UHFFFAOYSA-N oxomolybdenum Chemical compound [Mo]=O PQQKPALAQIIWST-UHFFFAOYSA-N 0.000 description 1
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- ACVYVLVWPXVTIT-UHFFFAOYSA-N phosphinic acid Chemical compound O[PH2]=O ACVYVLVWPXVTIT-UHFFFAOYSA-N 0.000 description 1
- VSAISIQCTGDGPU-UHFFFAOYSA-N phosphorus trioxide Inorganic materials O1P(O2)OP3OP1OP2O3 VSAISIQCTGDGPU-UHFFFAOYSA-N 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 239000012041 precatalyst Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 229910052712 strontium Inorganic materials 0.000 description 1
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 229910003468 tantalcarbide Inorganic materials 0.000 description 1
- 150000003892 tartrate salts Chemical class 0.000 description 1
- ISIJQEHRDSCQIU-UHFFFAOYSA-N tert-butyl 2,7-diazaspiro[4.5]decane-7-carboxylate Chemical compound C1N(C(=O)OC(C)(C)C)CCCC11CNCC1 ISIJQEHRDSCQIU-UHFFFAOYSA-N 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 229910001887 tin oxide Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- 229910001930 tungsten oxide Inorganic materials 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
- 229910001935 vanadium oxide Inorganic materials 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/20—Vanadium, niobium or tantalum
- B01J23/22—Vanadium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/18—Arsenic, antimony or bismuth
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0215—Coating
- B01J37/0219—Coating the coating containing organic compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0215—Coating
- B01J37/0221—Coating of particles
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/255—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting
- C07C51/265—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting having alkyl side chains which are oxidised to carboxyl groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D307/00—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
- C07D307/77—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom ortho- or peri-condensed with carbocyclic rings or ring systems
- C07D307/87—Benzo [c] furans; Hydrogenated benzo [c] furans
- C07D307/89—Benzo [c] furans; Hydrogenated benzo [c] furans with two oxygen atoms directly attached in positions 1 and 3
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/063—Titanium; Oxides or hydroxides thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Catalysts (AREA)
- Furan Compounds (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
201219112 六、發明說明: 【發明所屬之技術領域】 本發明係關於一種用於鄰二曱苯及/或萘氧化成鄰笨二 甲酸酐之觸媒,其具有複數個串聯配置於反應管内之觸媒 ' 區’且其採用含相當大比例之錄華的三氧化二銻來產製。 - 本發明進一步係關於一種用於氣相氧化之方法,其中含有 至少一種烴及分子氧之氣流穿過採用含相當大比例之銻華 的三氧化二銻產製之觸媒。 【先前技術】 很多羧酸及/或羧酸酐工業上藉由在固定床反應器中催 化氣相氧化烴類物質(諸如苯、二甲苯、萘、曱苯或莊)製 備。以此方法,可得到(例如)苯甲酸、順丁烯二酸酐、鄰 苯二曱酸酑、間苯二曱酸、對苯二甲酸或笨均四酸酐^ — 般而cr 3氧亂體及待氧化之起始物質之混合物通過存在 觸媒床1。爲了調節溫度,該我管為傳熱介質(例如 鹽熔融體)所環繞。 經塗佈觸媒(其中催化活性組合物已以殼的形式施加於 惰性撑體物質,諸如,塊滑石)已發現可作爲用於該等氧 化反應之觸媒。一般而言,該等觸媒具有活性組合物層, 其基本上具有均勻化學組成且以殼的形式施加。另,活性 * 組合物之兩種或更多種不同層可連續施加於撐體。此等稱 爲兩層或多層觸媒(參見,例如,DE 19839〇〇ι Μ)。 冉 乍爲。亥等、經塗佈觸媒之催化活性組合物之觸媒活性成 刀使用一般由二氧化鈦及五氧化二釩組成者。另,少量 157378.doc 201219112 的許多其他作爲促進劑以影響觸媒活性及選擇性之氧化化 合物(包括氧化鉋、三氧化二磷及氧化銻)可存在於催化活 性組合物中。 依據EP 1636161,當設定專門ν2〇5/%2〇3比及三氧化二 録具有—限定平均粒徑時,可獲得提供特別高PAn產率之 觸媒。 銻氧化物的存在使得PAn選擇性提高,其效果被視為是 釩位置之分離。 該等觸媒之活性組合物中採用的氧化銻可為各種銻 (ΠΙ)、銻(IV)及銻(V)化合物:通常採用三氧化二銻或五氧 化一銻》EP 522871係描述五氧化二銻的應用,us 2〇〇9/ 306409及EP 1636161係揭示三氧化二銻的應用。 相較四氧化二銻及五氧化二銻,三氧化二銻可更好遍佈 於二氧化鈦之上,從而獲得明顯改善之觸媒分佈。三氧化 二録一般作爲純方銻礦相使用(比照Schubert,u._a.等人,
Topics in Catalysis,2001,15(2-4)卷,195 至 200頁)。除立 方銻礦外’亦存在三氧化二銻之斜方晶變體,稱爲銻華 (Golunski,S. E.等人.,Appl. Catal.,1989,48卷,123至 135 頁)。 氣相氧化過程持續需要觸媒,此過程中觸媒在高選擇性 基礎上實現相當高轉化率。 【發明内容】 本發明目的之一是開發用於鄰二曱苯及/或萘氧化成鄰 苯二甲酸酐之觸媒,該觸媒使得在低鹽浴溫度中由低含量 157378.doc 201219112 鄰二甲苯及鄰苯二甲内酯可獲得高產率之鄰苯二〒酸酐。 此目的藉由一種用於鄰二甲苯及/或萘氧化成鄰苯二甲 酸酐之觸媒實現,此觸媒採用含有相當大比例之銻華的三 氧化二銻產製。 本發明目的之一係提供用於鄰二甲苯及/或萘氧化成鄰 苯二甲酸酐之觸媒,其採用三氧化二銻產製,#中其又光 粉末繞射圖中在2_θ=28.4。之信號高度與在2_θ=27 7。及 28.4之彳§號尚度總和的比至少為0.02。 在2-θ_27.7。之信號係方銻礦的特徵(對照ASTM Index,
No· 5-0534/7)且在2-θ=28.4。之信號為銻華(對照ASTM
Index,No. U_689)。信號高度藉由各自信號之最大強度與 所測定背景之不同來給出。 【實施方式】 在本發明之一較佳實例中,該觸媒採用三氧化二銻產 製,其中其X光粉末繞射圖中在2Θ=28 4。之信號高度與在 2-θ-27·7及28·4°之信冑高度總和的比至少為〇 〇3,尤佳至 少 0.05。 待依據本發明使用之具有相當高的銻華含量之三氧化二 録可用於產生—個或更多個觸媒區。在本發明之—較佳實 例中:該觸媒具有3、4或5個區,其中使用具有相當高録 華含Β二氧化二銻産生至少一個區。 本發明之觸媒亦可用於與合適之上游及/或下游床結合 及亦和中間區-起結合,以(例如)避免高熱點溫度,其中 該等上游及/或下游床及中間區—般可包括觸媒非活性或 157378.doc 201219112 活性較低物質。 本發明之觸媒一般為經塗佈觸媒,其中觸媒活性組合物 係以殼的形式施加至惰性撐體物質。 關於惰性樓體物質,實際上可採料有利地用於製造將 芳香烴氧化成醛、羧酸及/或羧酸酐之經塗佈觸媒的先前 技術之全部撐體物質,例如石英(Si〇2)、瓷、氧化鎂、二 氧化錫、碳化矽、金紅石、礬土(ΑΙΑ3)、矽酸鋁、塊滑石 (矽酸鎂)、矽酸鍅、矽酸鈽或該等撐體物質之混合物。該 等觸媒撐體可(例如)以球體、環、丸劑、螺旋形物、管、 擠出物或壓碎物質形式使用。此等觸媒撐體的尺寸係對應 於通常用於製造芳香烴之氣相反應的經塗佈觸媒之觸媒撐 體的尺寸。較佳採用呈具有3至6 mm直徑之球形形式或具 有5至9 mm外徑及3至8 mm長度及1至2 mm壁厚度之環形形 式的塊滑石。 本發明之觸媒包括催化活性組合物,其至少包括氧化鈒 及二氧化鈦且可以一層或多層施加於撐體物質。在此情況 下’不同層的化學組成可不同。 該催化活性組合物較佳包括,以催化活性組合物總量 計,1至40重量。/。之氧化釩(以ν:ί〇5計算),及6〇至99重量% 之一氧化鈦(以Ti〇2計算)。在較佳實施例中,此催化活性 組合物可另外包括至多達1重量%之铯化合物(以Cs計算)、 至多達1重量%之磷化合物(以P計算)、及至多達1〇重量0/〇 之氧化録(以St>2〇3計算)。關於催化活性組合物之化學組成 的王。卩數據係以後者的锻燒態為基準,例如,於將觸媒在 157378.doc 201219112 450°C下煅燒1小時後。 二氧化鈦通常係以銳鈦礦形式用於催化活性組合物。此 二氧化鈦較佳具有自15至60 m2/g之BET表面積,特定言之 自15至45 m2/g,特佳係自13至28 m2/g。所用二氧化鈦可 為個別二氧化鈦或二氧化鈦之混合物。在後者情況下,該 BET表面積之加權平均值決定個別二氧化鈦之貢獻。所用 二氧化鈦(例如)可有利地為具有5至15 m2/g之BET表面積的 Ti〇2及具有15至50 m2/g之BET表面積的Ti02的混合物。 合適釩源為(特定言之)五氧化二釩或偏釩酸銨。合適銻 源為各種具有相當大銻華含量之三氧化二銻。可能的磷源 為(特定言之)磷酸、亞磷酸、次磷酸、磷酸銨或磷酸酯且 尤其是填酸二氫銨。合適鉋源為氧化物或氫氧化物或可熱 轉化成氧化物之鹽’例如叛酸鹽,特定言之乙酸鹽、丙二 酸鹽或草酸鹽、碳酸鹽、碳酸氫鹽、硫酸鹽或硝酸鹽。 除視需要添加鉋及磷外,此催化活性組合物可包括少量 之許多其他作爲促進劑以影響觸媒之活性及選擇性(例 如,降低或提高其活性)的氧化化合物。此類促進劑之實 例為鹼金屬,特定言之,除上述鉋之外的鋰、鉀及铷(其 通常以其等之氧化物或氫氧化物形式使用)、氧化蛇⑴、 氧化銘、氧化錯·、氣化榻备 礼化鐵氡化鎳、氧化鈷、氧化錳、氧 化錫、乳化銀、乳化鋼、氧化鉻、氧化鉬、氧化鎢、氧化 鈒、氧化组、氧化起、氧化石申、四氧化二録、五氧化二錄 及氧化飾。 另’在上述促進劑中,更㈣以含量爲催化活性組合物 157378.doc 201219112 之〇·〇1至〇.50重量%的銳及鎢的氧化物作為添加劑。 該⑷經塗佈觸媒層之施加較有利係藉由將Ti〇2及Μ 之懸浮液(其視需要可包括上述促進劑成分源)嗔淋於流體 化擇體之上而進行。在塗佈之前,較佳將該懸浮液檀掉充 分長時間’例如’ 2至30小時’特定言之以”小時以 打碎懸浮固體之凝聚物而獲得均句懸浮液。此懸浮液—般 具有20至50重量%之固體含量。此懸浮介質一般為水性, 例如:水本身或含有水可混溶有機溶劑諸如甲醇、乙醇、 異丙醇、甲醯胺及其類似物的水性混合物。 一般而言’有機黏合劑,較佳共聚物,較有利係以丙婦 酸-順丁稀二酸、乙酸乙祕月桂酸乙稀醋、乙酸乙稀醋_ 丙烯酸醋、苯乙烯·丙烯酸§旨及乙酸乙稀•乙稀之水性分 散液㈣式添加到懸浮液中。可購得固體含量為(例如)35 量之水丨生刀散液的該等黏合劑。該等黏合劑分散 :之用量-般佔懸浮液重量之2至45重量%,較佳5至㈣ 量%,尤佳7至20重量%。 字〆樓體在(例如)流體化床裝置或移動床裝置中,於上 升氣流(特疋5之’空氣)中流體化。該裝置通常包括一圓 錐形或球形容器,將流體化氣體經由一沉管自下方或自上 方引入其中。該懸浮液經過噴嘴自上方、自侧邊、或下方 喷淋入流體化床。升流管以中心或同心環繞沉管配置使用 較爲有利。在升流管中向上運輸樓體粒子之較高氣流速度 *勢在外蜋中,氣流速度僅稍高於鬆動速度。因此, /等粒子以j衣狀方式垂直移動。合適之流體化床裝置係於 157378.doc 201219112 例如DE-A 4006935中描述。 在以催化活性組合物塗佈觸媒撐體中一般採用20至 500 C之塗佈溫度,其中塗佈可在大氣壓或減壓下進行。 一般而言,塗佈在0艽至2〇〇七進行,較佳汕至丨“它,特 定言之60至120°C。 催化活性組合物之層厚度—般自〇 〇2至〇 2 mm,較佳自 0.05至0.15 mm。觸媒中活性組和物之比例一般為5至25重 量% ’大部分為7至1 5重量%。 在溫度自大於20(TC至50(rc熱處理以此方式得到之觸媒 前體(precataiyst)導致黏合劑由於熱分解及/或燃燒而自該 施加層中放出。該熱處理較佳於氣相氧化反應器中在原位 進行。 本發明進一步提供氣相氧化之方法,其中包括至少一種 烃及刀子氧之氣流穿過採用三氧化二銻產製之觸媒,其中 X光粉末繞射圖中在2_θ=28.4。之信號高度與在2_0=27 7。及 28.4°之彳§號向度總和的比至少為〇 。 本發明之一較佳實施例爲一用於將鄰二曱苯及/或萘氣 相氧化成鄰苯二曱酸酐之方法’其中包括鄰二曱苯及/或 萘及分子氧之氣流穿過採用三氧化二銻產製之觸媒,其中 X光粉末繞射圖中在2_θ=28.4。之信號高度與在2_θ=27 7〇 及28.4。之仏號高度總和的比至少為0.02。 實施例 二氧化二銻中銻華含量及方礦銻含量之測定: 此測疋藉由X光粉末繞射術進行。出於此目的,該三氧 157378.doc 201219112 化二銻粉末係採用購自Siemens之“D5000 Θ/Θ”Χ光粉末繞 射計測量。該測量參數如下: 直徑 435 mm X-輻射 · (:ιιΚ-α(λ=1.54· 10_10m) 管電壓 40 kV 管電流 30 mA 孔徑 變量V20 散射輻射孔 變量V20 二次單色器 石墨 單色器孔徑 0.1 mm 閃爍計數器 探測器孔徑 0.6 mm 步長 0.02° 2Θ 步進模式 連續 測量時間 2.4 s/步 測量速率 0.5° 20/min 信號高度藉由各自信號之最大強度與所決定背景之間的 不同給出。為測定銻華含量,採用於2-θ=27.7° (方銻礦, 信號高度a)及28.4°(銻華,信號高度b)之信號。該銻華含 量為b/(a+b),且該方礦録含量為a/(a+b)。 實例1(依據本發明): 觸媒區CZ1 : 將3·38 g碳酸鉋,459.3 g二氧化鈦(Fuji TA 100C,銳鈦 礦,BET表面積 20 m2/g),196.9 g二氧化鈦(Fuji TA 100, 157378.doc •10· 201219112 銳鈦礦’ BET表面積7 m2/g)及51.4 g五氧化二飢及13.2 g 二氧化二銻(Merck Selectipur 7835,錄華含量=〇.i8,方錄 礦含量=0.82,99.5% Sb2〇3含量,以重量計300 ppm之 As ’以重量計5〇〇 ppm之Pb,以重量計50 ppm之Fe,平 均粒徑2 μηι)懸浮於1869 g去離子水中且攪拌18小時以獲 得均勻分布》將78.4 g包含乙酸乙烯酯及月桂酸乙烯酯之 共聚物的有機黏合劑以50重量%濃度之水性分散液形式添 加到此懸浮液中。在流體化床裝置中,將82〇 g此懸浮液 喷淋到2 kg呈7 mmx7 mmx4 mm尺寸的環形形式之塊滑石 (矽酸鎂)上並予以乾燥。在450。(:磁燒該觸媒1小時後,施 加於塊滑石環的活性組合物量為9.1 %。該活性組合物之分 析化學組成為7.1%之V205,1.8%之Sb203,0.38%之Cs, 其餘為Ti〇2。 觸媒區CZ2 : 製造方法類似CZ1,其中該懸浮液之化學組成變化。在 450°C煅燒該觸媒1小時後,施加於塊滑石環的活性組合物 量為8.5% ^該活性組合物之分析化學組成包括7 95%之 ▽2〇5,2.7%之8152〇3,0.31%之〇3,其餘為平均8丑1'表面積 1 8 m2/g之 Ti〇2 〇 觸媒區CZ3 : 製造方法類似CZ1,其中該懸浮液之化學組成變化。在 450°C煅燒該觸媒1小時後,施加於塊滑石環的活性組合物 量為8.5%。該活性組合物之分析化學組成包括7 1%之 V205 ’ 2.4%之Sb2〇3,0·10%之&,其餘為平均BET表面積 157378.doc • 11 - 201219112 17 m2/g之 Ti02。 觸媒區CZ4 : 製造方法類似CZ1,其中該懸浮液之化學組成變化且採
用 Fuji TA 100CT(銳鈦礦,bet 表面積 27 m2/g)代替 Fuji TA 100C。在450°C煅燒該觸媒【小時後,施加於塊滑石環的活 性組合物量為9· 1 %。該活性組合物之分析化學組成包括 20%之V205 ’ 0.38%之P,其餘為平均BET表面積23 一化之 Ti02。 實例2(非依據本發明): 觸媒區CZ5 : 製造方法類似CZ1,但採用一具有減少銻華含量之三氧 化二錄級(例如,白色Triox,購自Antraco,綈華含量 =0.015,方銻礦含量=0.985,99.3% Sb203 含量,0.3 重量 %2As203 ’ 0.18重量%2PbO,0.02重量%之氧化鐵,平均 粒徑 1.5 μηι)。 觸媒區CZ6 : 製造方法類似CZ2但採用一具有減少銻華含量之三氧化 二銻級(例如,白色Triox,購自Antraco,録華含量 = 0.015 ’ 方銻礦含量=0.985,99.3% Sb203含量,〇.3重量% 之As2〇3 ’ 0· 18重量%之PbO ’ 0.02重量%之氧化鐵,平均 粒徑 1.5 μηι)。 觸媒區CZ7 : 製造方法類似CZ3但採用一具有減少銻華含量之三氧化 157378.doc 12 201219112 二銻級(例如,白色Triox,購自Antraco,銻華含量 =0.015,方銻礦含量=0.985,99.3% Sb203 含量,0.3 重量 % 之As203,0.18重量。/。之PbO,0.02重量%之氧化鐵,平均 粒徑 1 ·5 μπι)。 實例3(依據本發明,鄰二甲苯以模型管規模氧化成鄰苯二 甲酸酐): 鄰二甲苯之催化氧化成鄰苯二甲酸酐在具有25 mm之管 内徑的鹽浴冷卻管式反應器中進行《自反應器進口至反應 器出口,130 cm之 CZ1、70 cm之 CZ2、60 cm之 CZ3及 60 cm之CZ4被引入到具有3.5 m之長度及25 mm之内徑的鐵管 中。該鐵管為一用以調節溫度之鹽熔融體,一具有4 mm外 徑的外勒及一用以測量催化溫度之内建可抽出元件的熱電 偶所環繞。 載荷自30至1〇〇克/標準立方米之99.2重量%濃度的鄰二 曱苯之4.0標準立方米/小時的氣體自頂端向下穿過管。此 結果在表1中總結給出(“PAn產率”係以1〇〇%強度鄰二曱苯 計’獲得的鄰笨二曱酸酐量的重量百分比)。 實例4(非依據本發明’鄰二甲苯以模型管規模氧化成鄰苯 二曱酸酐): 參見實例3’但具有一觸媒床包括(自反應器進口至反應 器出口)130 cm之 CZ5、70 cm之 CZ6、60 cm之 CZ7 及 60 cm之 CZ4 〇 157378.doc •13· 201219112 表1 模型管結果 實例3(依據本發明) 實例4(非依據本發明) 氣體量[標準m3/h] i荷[g/標準m3] 4.0 4.0 4.0 4.0 70 82 72 81 運行時間[天] 33 40 21 29 鹽浴溫度[°0] 352.0 347.0 357.0 352.0 ΡΑη產率[重量。/0] 112.5 113.0 111.5 112.5 鄰二曱苯含量[重量%] 0.03 0.08 0.03 0.07 鄰苯二甲内g旨含量[重量%1 ----— 0.05 0.09 0.06 0.10 表1中實例3及4之比較顯示實例3之觸媒催化活性高於實 例4貫例3中β玄鹽浴溫度(依據本發明)由於此原因可進一 步降低,且具有低鄰二甲苯及鄰苯二甲内酯含量之ρΑη產 率顯著高於實例4(非依據本發明)^ 實例5(依據本發明,鄰二甲苯以工業規模氧化成鄰苯二甲 酸酐): 鄰二甲苯之催化氧化成鄰苯二甲酸酐係在具有15 1〇5支 25 mm之管内徑的管之鹽浴冷卻管式反應器中進行。自反 應器進口至反應器出口 ’引入13〇 Cm之CZ1、90 cm之 CZ2、60 cm之CZ3及60 cm之CZ4。為記錄溫度曲線,一些 反應官配備有熱電偶。具有0至1〇〇克/標準立方米之鄰二 甲苯載荷(純度達99重量%)的4.0標準立方米/小時氣體穿過 該管。該ΡΑη產率在反應器出口氣體中·測量且於表2中以 100%濃度之鄰二甲苯計,以重量%記錄(每千克反應鄰二 157378.doc -14- 201219112 甲苯之PAn千克)。 實例6(非依據本發明,鄰二甲苯以工業規模氧化成鄰苯二 甲酸酐): 參見實例5,但具有一觸媒床包括(自反應器進口至反應 • 器出口)130 cm之 CZ5、90 cm之 CZ6、60 cm之 CZ7 及 60 - cm之 CZ4。 表2 工業規模 實例5(依據本發明) 實例6(非依據本發明) 氣體量[標準m3/h] 4.0 4.0 載荷[g/標準m3] 95 95 運行時間[天] 79 76 鹽浴溫度[°(:] 343.4 346.2 PAn產率[重量%] 114.5 112.9 鄰二曱苯含量[重量%] 0.08 0.06 鄰苯二曱内酯含量[重量%] 0.01 0.01 表2中實例5及6之比較顯示實例5之觸媒催化活性高於實 例6。實例5中該鹽浴溫度(依據本發明)由於此原因進一步 降低,且具有低鄰二甲苯及鄰苯二甲内酯含量之PAn產率 顯著高於實例6(非依據本發明)。 157378.doc -15-
Claims (1)
- 201219112 ' 七、申請專利範圍: 種用於鄰—甲苯及/或萘氧化成鄰苯二甲酸酐之觸媒, 其係採用三氧化二銻產製,其中χ光粉末繞射圖中在2_ θ-28,4之信號高度與在2_θ=27 7。及28 4。之信號高度總 ‘ 和的比至少為0.02。 ,2· 一種氣相氧化方法,其中使包括至少一種烴及分子氧之 氣流穿過採用三氧化二銻產製之觸媒,其中X光粉末繞 射圖中在2-θ=28.40之信號高度與在2_θ=27 7〇及28 4。之 仏號咼度總和的比至少為〇 〇2。 3.如明求項2之方法,其中該烴為鄰二曱苯及/或萘。 157378.doc 201219112 四、指定代表圖: (一) 本案指定代表圖為:(無) (二) 本代表圖之元件符號簡單說明: 五、本案若有化學式時,請揭示最能顯示發明特徵的化學式: (無) 157378.doc
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP10171381 | 2010-07-30 |
Publications (1)
Publication Number | Publication Date |
---|---|
TW201219112A true TW201219112A (en) | 2012-05-16 |
Family
ID=45529478
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW100127132A TW201219112A (en) | 2010-07-30 | 2011-07-29 | Catalyst for the oxidation of o-xylene and/or naphthalene to phthalic anhydride |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP2598238A4 (zh) |
JP (1) | JP5973436B2 (zh) |
KR (1) | KR20130131306A (zh) |
CN (1) | CN103025424B (zh) |
BR (1) | BR112013001388A2 (zh) |
TW (1) | TW201219112A (zh) |
WO (1) | WO2012014154A1 (zh) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWI660775B (zh) * | 2017-02-14 | 2019-06-01 | 瑞士商克萊瑞特國際股份有限公司 | 具經銻摻雜二氧化鈦之用於氧化烴之催化劑材料 |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9029289B2 (en) | 2012-07-16 | 2015-05-12 | Basf Se | Catalyst for preparing carboxylic acids and/or carboxylic anhydrides |
JP2015530228A (ja) * | 2012-07-16 | 2015-10-15 | ビーエーエスエフ ソシエタス・ヨーロピアBasf Se | カルボン酸および/またはカルボン酸無水物を製造するための触媒 |
US9656983B2 (en) * | 2013-06-26 | 2017-05-23 | Basf Se | Process for starting up a gas phase oxidation reactor |
JP6563410B2 (ja) * | 2014-02-17 | 2019-08-21 | ビーエーエスエフ ソシエタス・ヨーロピアBasf Se | o−キシロールおよび/またはナフタレンをフタル酸無水物に酸化する触媒系 |
US9914716B2 (en) * | 2014-02-17 | 2018-03-13 | Basf Se | Catalyst system for oxidation of o-xylene and/or naphthalene to phthalic anhydride |
EP2987552A1 (en) * | 2014-08-22 | 2016-02-24 | Basf Se | Catalyst system for oxidation of o-xylene and/or naphthalene to phthalic anhydride |
DE102014203725A1 (de) | 2014-02-28 | 2015-09-03 | Basf Se | Oxidationskatalysator mit sattelförmigem Trägerformkörper |
EP3047904A1 (en) * | 2015-01-22 | 2016-07-27 | Basf Se | Catalyst system for oxidation of o-xylene and/or naphthalene to phthalic anhydride |
CA3070416C (en) | 2017-07-18 | 2022-05-24 | Ha-International, Llc | Compositions and methods for refractory coatings with ester carriers |
CN112642454A (zh) * | 2019-10-12 | 2021-04-13 | 中国石油化工股份有限公司 | 一种邻二甲苯氧化制苯酐的催化剂及其制备方法 |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60137438A (ja) * | 1983-09-28 | 1985-07-22 | Nitto Chem Ind Co Ltd | アンチモン含有金属酸化物触媒の製法 |
DE4006935A1 (de) | 1990-03-06 | 1991-09-12 | Wacker Chemie Gmbh | Fliessbettapparatur zum mischen, trocknen und beschichten von pulvrigem, koernigem und geformtem schuettgut |
US5235071A (en) * | 1991-07-10 | 1993-08-10 | Nippon Shokubai Co., Ltd. | Catalyst for producing phthalic anhydride and process by using the same |
DE19823275A1 (de) * | 1998-05-26 | 1999-12-02 | Basf Ag | Verfahren zur Herstellung von Phthalsäureanhydrid durch katalytische Gasphasenoxidation von x-Xylol-/-Naphthalin-Gemischen |
DE19839001A1 (de) | 1998-08-27 | 2000-03-02 | Basf Ag | Schalenkatalysatoren für die katalytische Gasphasenoxidation von aromatischen Kohlenwasserstoffen |
DE19922156A1 (de) * | 1999-05-12 | 2000-08-10 | Basf Ag | Multimetalloxidmassen, Verfahren zu ihrer Herstellung, sowie Vorrichtungen zur Durchführung des Verfahrens |
DE10323461A1 (de) | 2003-05-23 | 2004-12-09 | Basf Ag | Herstellung von Aldehyden, Carbonsäuren und/oder Carbonsäureanhydriden mittels Vanadiumoxid, Titandioxid und Antimonoxid enthaltender Katalysatoren |
DE10323818A1 (de) * | 2003-05-23 | 2004-12-09 | Basf Ag | Katalysatorsysteme zur Herstellung von Phthalsäureanhydrid |
FR2855516B1 (fr) * | 2003-05-27 | 2005-07-08 | Atofina | Oxydation du propane en acide acrylique par utilisation de catalyseurs en melange de phases cristallines |
JP4442317B2 (ja) * | 2004-05-21 | 2010-03-31 | 三菱化学株式会社 | 複合酸化物触媒の製造方法 |
ZA200708804B (en) | 2005-05-22 | 2009-01-28 | Sued Chemie Ag | Multi-layered catalyst for producing phthalic anhydride |
CN101130535B (zh) * | 2006-08-25 | 2010-10-13 | 中国石油化工股份有限公司 | 一种邻苯二甲酸酐的制备方法 |
JP2009067621A (ja) * | 2007-09-12 | 2009-04-02 | Nippon Shokubai Co Ltd | 酸化物粒子、当該粒子を含む分散体及び当該粒子を用いた触媒 |
DE102008054586A1 (de) * | 2008-12-12 | 2010-06-17 | Basf Se | Verfahren zur kontinuierlichen Herstellung von geometrischen Katalysatorformkörpern K |
-
2011
- 2011-07-26 EP EP11811912.2A patent/EP2598238A4/en not_active Withdrawn
- 2011-07-26 JP JP2013522327A patent/JP5973436B2/ja not_active Expired - Fee Related
- 2011-07-26 BR BR112013001388A patent/BR112013001388A2/pt not_active IP Right Cessation
- 2011-07-26 WO PCT/IB2011/053327 patent/WO2012014154A1/en active Application Filing
- 2011-07-26 CN CN201180035813.9A patent/CN103025424B/zh active Active
- 2011-07-26 KR KR1020137004810A patent/KR20130131306A/ko not_active Application Discontinuation
- 2011-07-29 TW TW100127132A patent/TW201219112A/zh unknown
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWI660775B (zh) * | 2017-02-14 | 2019-06-01 | 瑞士商克萊瑞特國際股份有限公司 | 具經銻摻雜二氧化鈦之用於氧化烴之催化劑材料 |
Also Published As
Publication number | Publication date |
---|---|
BR112013001388A2 (pt) | 2016-05-24 |
WO2012014154A1 (en) | 2012-02-02 |
CN103025424A (zh) | 2013-04-03 |
CN103025424B (zh) | 2016-01-20 |
JP2013539407A (ja) | 2013-10-24 |
JP5973436B2 (ja) | 2016-08-23 |
KR20130131306A (ko) | 2013-12-03 |
EP2598238A4 (en) | 2014-08-20 |
EP2598238A1 (en) | 2013-06-05 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
TW201219112A (en) | Catalyst for the oxidation of o-xylene and/or naphthalene to phthalic anhydride | |
US9029289B2 (en) | Catalyst for preparing carboxylic acids and/or carboxylic anhydrides | |
JP2007534628A (ja) | 酸化バナジウム、二酸化チタンおよび酸化アンチモンを含有する触媒を用いての、アルデヒド、カルボン酸および/またはカルボン酸無水物の製造方法 | |
US8859459B2 (en) | Multilayer catalyst for preparing phthalic anhydride and process for preparing phthalic anhydride | |
JP4499729B2 (ja) | 規定の酸化バナジウムの粒度分布を有する気相酸化触媒 | |
JP2016529219A (ja) | 無水フタル酸を製造するための方法 | |
TW200526321A (en) | Process for producing a catalyst for gas-phase oxidations | |
EP3107653B1 (en) | Catalyst system for oxidation of o-xylene and/or naphthalene to phthalic anhydride | |
US20110230668A1 (en) | Catalyst for gas phase oxidations based on low-sulfur and low-calcium titanium dioxide | |
US9212157B2 (en) | Catalyst for the oxidation of o-xylene and/or naphthalene to phthalic anhydride | |
JP6563410B2 (ja) | o−キシロールおよび/またはナフタレンをフタル酸無水物に酸化する触媒系 | |
US10710054B2 (en) | Multi-zoned catalyst system for oxidation of o-xylene and/or naphthalene to phthalic anhydride | |
TWI641587B (zh) | 用於起動氣相氧化器之方法 | |
KR101828779B1 (ko) | 프탈산 무수물을 제조하기 위한 최적의 표면을 갖는 촉매 컨버터 배열체 | |
JP2015530228A (ja) | カルボン酸および/またはカルボン酸無水物を製造するための触媒 | |
TW201138955A (en) | Catalyst for gas phase oxidations based on low-sulfur and low-calcium titanium dioxide | |
EP2987552A1 (en) | Catalyst system for oxidation of o-xylene and/or naphthalene to phthalic anhydride |