发明名称 Fremgangsmate og katalysator for selektiv fremstilling av eddiksyre ved katalytisk oksydasjon av etan og/eller etylen
摘要 A method for the selective production of acetic acid from a gas-phase feed of ethane, ethylene, or mixtures thereof and oxygen at elevated temperatures. The gas-phase feed is brought into contact with a catalyst, containing the elements Mo, Pd, X and Y in the gram atom ratios a:b:c: in combination with oxygen according to formula (I): MO<SUB>a</SUB>Pd<SUB>b</SUB>X<SUB>c</SUB>Y<SUB>d</SUB>. The symbols X and Y have the following meanings: X=one or several elements chosen from the group Cr, Mn, Nb, Ta, Ti, V, Te and W; Y=one or several elements chosen from the group B, Al, Ga, In, Pt, Zn, Cd, Bi, Ce, Co, Rh, Ir, Cu, Ag, Au, Fe, Fu, Os, K, Rb, Cs, Mg, Ca, Sr, Ba, Nb, Zr, Hf, Ni, P, Pb, Sb, Si, Sn, Ti and U: the indices a, b, c, d and x=the gram atom ration for the corresponding elements, where: a=1; b-0.0001 to 0.01; c=0.4 to 1; and d=0.005 to 1, wherein the space-time yield for the above oxidation to yield acetic acid is 470 kg/(hm<SUP>3</SUP>) and the selectivity of the oxidative reaction of ethane and/or ethylene to give acetic acid is, in particular, >=70 mol %. X=preferably Nb and an ammonium salt of niobium is used as niobium source.
申请公布号 NO328001(B1) 申请公布日期 2009.11.09
申请号 NO20020005148 申请日期 2002.10.25
申请人 CELANESE INTERNATIONAL CORP 发明人 DINGERDISSEN UWE;ZEYSS SABINE
分类号 C07C51/215;B01J23/00;B01J23/18;B01J23/20;B01J23/44;B01J23/648;B01J23/652;B01J37/00;C07B61/00;C07C51/25;C07C53/08 主分类号 C07C51/215
代理机构 代理人
主权项
地址