发明公开
EP1082317A1 VERFAHREN ZUR HERSTELLUNG VON PHTHALSÄUREANHYDRID DURCH KATALYTISCHE GASPHASENOXIDATION VON O-XYLOL/NAPHTHALIN-GEMISCHEN 有权
PROCESS FOR通过邻二甲苯/萘混合物的气相催化氧化反应生产邻苯二甲酸酐

  • 专利标题: VERFAHREN ZUR HERSTELLUNG VON PHTHALSÄUREANHYDRID DURCH KATALYTISCHE GASPHASENOXIDATION VON O-XYLOL/NAPHTHALIN-GEMISCHEN
  • 专利标题(英): Method for producing phthalic anhydride by means of catalytic vapor-phase oxidation of o-xylol/naphthalene mixtures
  • 专利标题(中): PROCESS FOR通过邻二甲苯/萘混合物的气相催化氧化反应生产邻苯二甲酸酐
  • 申请号: EP99924921.2
    申请日: 1999-05-10
  • 公开(公告)号: EP1082317A1
    公开(公告)日: 2001-03-14
  • 发明人: HEIDEMANN, ThomasARNOLD, HeikoHEFELE, GerhardWANJEK, Herbert
  • 申请人: BASF AKTIENGESELLSCHAFT
  • 申请人地址: 67056 Ludwigshafen DE
  • 专利权人: BASF AKTIENGESELLSCHAFT
  • 当前专利权人: BASF AKTIENGESELLSCHAFT
  • 当前专利权人地址: 67056 Ludwigshafen DE
  • 优先权: DE19823275 19980526
  • 国际公布: WO9961434 19991202
  • 主分类号: C07D307/89
  • IPC分类号: C07D307/89 C07C51/31 C07C51/265 C07C63/16
VERFAHREN ZUR HERSTELLUNG VON PHTHALSÄUREANHYDRID DURCH KATALYTISCHE GASPHASENOXIDATION VON O-XYLOL/NAPHTHALIN-GEMISCHEN
摘要:
The invention relates to a method for producing phthalic anhydride by means of catalytic vapor-phase oxidation of o-xylol/naphthalene mixtures with molecular oxygen while using a catalyst (I) situated in a first layer on the gas entry side, said layer amounting to 25 to 75 percentage by volume of the total catalyst volume, containing, each time with regard to the catalytically effective mass, 1 to 10 wt.% vanadium oxide (calculated as V2O5), 1 to 10 wt.% antimony oxide (calculated as Sb2O3) and 80 to 98 wt.% titanium dioxide of the anatase type with a BET surface of 13 to 28 m2/g, and 0.05 to 1 wt.% cesium (calculated as Cs), deposited on a steatite support. In addition, the phthalic anhydride is produced by using a catalyst (II) situated in a second layer, said layer amounting to the remaining 75 to 25 percent by volume of the total catalyst volume, containing, each time with regard to the catalytically effective mass, 1 to 10 wt.% vanadium oxide (calculated as V¿2?O5), 1 to 10 wt.% antimony oxide (calculated as Sb2O3) and 80 to 98 wt.% titanium dioxide of the anatase type with a BET surface of 13 to 28 m?2¿/g, 0.01 to 1 wt.% phosphorous oxide (calculated as P) and 0.01 to 0.2 wt.% cesium (calculated as Cs), deposited on a steatite support. The cesium content of catalyst (II) is less than 15 wt.% of the cesium content of catalyst (I), and catalyst (I) and catalyst (II) are produced without adding compounds of niobium.
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