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    • 2. 发明授权
    • Continuous process for the extraction and esterification of carboxylic
acid
    • 连续提取和酯化羧酸的方法
    • US4458088A
    • 1984-07-03
    • US364387
    • 1982-04-01
    • Harley F. HardmanJohn G. Frye, Jr.Terry J. Mazanec
    • Harley F. HardmanJohn G. Frye, Jr.Terry J. Mazanec
    • C07C67/10
    • C07C67/08C07C67/10Y02P20/582
    • A continuous process for the production of alkyl esters from carboxylic acids wherein an aqueous stream containing a first carboxylic acid, RCO.sub.2 H, is contacted with an organic stream comprising a carboxylic acid ester, R"CO.sub.2 R', so that the organic stream is enriched with RCO.sub.2 H. The RCO.sub.2 H enriched organic stream is separated from the aqueous stream and is contacted with a catalyst to obtain a second carboxylic acid, R"CO.sub.2 H, and a product carboxylic acid ester, RCO.sub.2 R'. The product ester, RCO.sub.2 R', is separated from the second acid, R"CO.sub.2 H, the reactant ester, R"CO.sub.2 R', and the first acid, RCO.sub.2 H, and the second acid, R"CO.sub.2 H, is esterified to obtain the reactant ester, R"CO.sub.2 R', which is recycled to the initial part of the process. In this process R is aliphatic or aromatic, R' is alkyl and R" is aliphatic with at least about 4 carbon atoms. When the reactant ester is a bifunctional polymer having both sulfonic acid and R' carboxylic acid ester pendant functional groups, this process may be performed in the absence of a catalyst.
    • 用于从羧酸生产烷基酯的连续方法,其中含有第一羧酸RCO 2 H的水流与包含羧酸酯R'CO 2 R'的有机物流接触,使得有机物流富含 RCO2H。 将富含RCO 2 H的有机物流与水流分离,并与催化剂接触,得到第二种羧酸R'CO 2 H和产物羧酸酯RCO 2 R'。 将产物酯RCO 2 R'与第二酸R'CO 2 H,反应物酯R'CO 2 R'和第一酸RCO 2 H和第二酸R'CO 2 H分离,得到 反应物酯R'CO 2 R',其被再循环到该方法的初始部分。 在该方法中,R为脂族或芳族,R'为烷基,R“为具有至少约4个碳原子的脂族基。 当反应物酯是具有磺酸和R'羧酸酯侧链官能团的双功能聚合物时,该方法可以在不存在催化剂的情况下进行。
    • 4. 发明授权
    • Catalyst composition for the preparation of alcohols
    • 用于制备醇的催化剂组合物
    • US4657887A
    • 1987-04-14
    • US754879
    • 1985-07-15
    • Harley F. HardmanTerry J. MazanecJohn G. Frye, Jr.
    • Harley F. HardmanTerry J. MazanecJohn G. Frye, Jr.
    • B01J23/78B01J23/83B01J23/84B01J23/89B01J35/10B01J37/03C07C29/154C07C29/156B01J21/04B01J23/02B01J23/12B01J23/72
    • B01J23/83B01J23/78B01J23/84B01J23/894C07C29/154C07C29/156B01J35/1014B01J37/03Y02P20/52
    • A catalyst composition containing alkali metal or alkaline earth metal uranate suitable for the conversion of mixtures of carbon monoxide and hydrogen has the formulaCu.sub.a U M.sub.b A.sub.c O.sub.xwhere M is one or more metals selected from the group consisting of Th, Pd, Mn, Cr, Fe, Co, Zn, Ce, V, Ru, Rh, Al, Re, Os, Pt, Ir, Ag, Ti, La and Zr, A is an alkaline or alkali earth metal anda is from 0.01 to 5.0;b is from 0 to 5.0 with the proviso that when M is Th the value of b is less than 1;c is a number up to 5.0 selected so that the catalyst composition contains more than 2 percent by weight of Metal A;x is a number such that the valence requirements of the other elements for oxygen are satisfied.The catalyst composition can be used to prepare an alcohol composition containing at least 30 percent by weight of methanol, the remainder of said composition comprising higher alcohols, the distribution of which on a methanol-free basis isC.sub.2 -10 to 90 weight percentC.sub.3 -15 to 60 weight percentC.sub.4 -0.5 to 35 weight percentC.sub.5 -0 to 15 weight percentC.sub.6 -0 to 15 weight percentand wherein the percent of C.sub.3 is at least 1.25 times the percent of C.sub.4.
    • 适用于转化一氧化碳和氢的混合物的碱金属或碱土金属的尿素的催化剂组合物具有式CuaUMbAcOx,其中M是选自Th,Pd,Mn,Cr,Fe,Co中的一种或多种金属 ,Zn,Ce,V,Ru,Rh,Al,Re,Os,Pt,Ir,Ag,Ti,La和Zr,A为碱金属或碱土金属,a为0.01〜5.0; b为0至5.0,条件是当M为Th时,b的值小于1; c是至多选择5.0的数量,使得催化剂组合物含有超过2重量%的金属A; x是满足氧气的其他元素的化合价要求的数字。 催化剂组合物可用于制备含有至少30重量%甲醇的醇组合物,所述组合物的其余部分包含高级醇,其在不含甲醇的基础上的分布为C2-10-90重量%C3- 15至60重量%的C 4 -0.5至35重量%的C 5至15重量%C 6至15重量%,并且其中C 3的百分比为C 4的至少1.25倍。