首页> 外国专利> Methyl tert. alkyl ethers prodn. from tert. olefins - and methanol, by liq. phase reaction over a homogeneous acidic catalyst

Methyl tert. alkyl ethers prodn. from tert. olefins - and methanol, by liq. phase reaction over a homogeneous acidic catalyst

机译:甲基叔丁基烷基醚产品来自叔叔烯烃-和甲醇,按液量计。均相酸性催化剂上的相反应

摘要

Prepn. of ethers (I) comprises liquid phase reaction of a tert. olefin of formula RCH=CR'2 (II) (R = H or alkyl, R' = alkyl) with methanol in the presence of a homogeneous catalyst (III) free from heteropolyacid. (III) has formula HnAaDcOy.xH2O (A is P, B, Si, Ge, Sn, As, Sb, U, Mn, Re, Cu, Ni, Co, Fe, Ce, Th and/or Cr. D is Mo, W and/or V. a = 0.1-10, c = 6-18. n = 1 and is the no. of acidic H atoms in the catalyst. y = 10-70 and x = 0-40). Pref. A is P, Si or Ge, specifically (III) is H4SiMo12O40. - xH2O. Process avoids the corrosion problems associated with strong acid catalysts and minimises the amt. of by-product CH3OCH3 formed. In an example reaction of isobutylene and methanol over the specified catalyst at mole ratio 1:4 gave 81.5% isobutylene conversion and 100% selectivity for methyl tert. butyl ether.
机译:准备醚(I)包括叔酸的液相反应。在没有杂多酸的均相催化剂(III)的存在下,用甲醇将式RCH = CR′2(II)的烯烃(R = H或烷基,R′=烷基)。 (III)的分子式为HnAaDcOy.xH2O(A为P,B,Si,Ge,Sn,As,Sb,U,Mn,Re,Cu,Ni,Co,Fe,Ce,Th和/或Cr.D为Mo ,W和/或V。a= 0.1-10,c =6-18。n= 1,是催化剂中酸性H原子的数目。y= 10-70,x = 0-40。首选A为P,Si或Ge,具体地,(III)为H 4 SiMo 12 O 40。 -xH2O该工艺避免了与强酸催化剂相关的腐蚀问题,并最大程度地减少了不良反应。形成副产物CH 3 OCH 3。在一个实例中,异丁烯和甲醇在指定的催化剂上以摩尔比1∶4反应得到81.5%的异丁烯转化率和100%的甲基叔选择性。丁基醚。

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