디메틸카보네이트제조용무기체담지촉매,그제조방법및이에의한디메틸카보네이트의제조방법
    53.
    发明授权
    디메틸카보네이트제조용무기체담지촉매,그제조방법및이에의한디메틸카보네이트의제조방법 失效
    碳酸二甲酯的制备催化剂及其制备方法及其用途

    公开(公告)号:KR1019930005305B1

    公开(公告)日:1993-06-17

    申请号:KR1019910005562

    申请日:1991-04-08

    Inventor: 박대철 이미연

    Abstract: A catalyst supported on an inorganic substance is given formula MaS [M is CuCl2 2H2O; S is an inorganic support such as γ-alumina, TiO2 and kisselbuhr; a is the wt.% of the metal . In the production, M and S are added to distilled water and heated to 80-90 deg.C, after deposition, it is dried at 110 deg.C. The production of dimethylcarbonater of formula (II) is also claimed. Methanol, carbon monoxide, oxygen are reacted in the presence of the catalyst at 100-140 deg.C and under 1-5 kg/cm2.

    Abstract translation: 负载在无机物质上的催化剂给出式为MaS [M为CuCl 2·2H 2 O; S是无机载体,如γ-氧化铝,TiO2和亲水; a是金属的重量%。 在生产中,将M和S加入到蒸馏水中,加热至80-90℃,沉积后在110℃下干燥。 还要求生产式(II)的二甲基碳酸酯。 在催化剂存在下,甲醇,一氧化碳,氧气在100-140℃和1-5kg / cm2下反应。

    에틸리덴 디 아세테이트 제조용 고체촉매, 그의 제조방법 및 이를 이용한 연속식, 공정에 의한 에틸리덴 디 아세테이트의 제조방법
    54.
    发明授权
    에틸리덴 디 아세테이트 제조용 고체촉매, 그의 제조방법 및 이를 이용한 연속식, 공정에 의한 에틸리덴 디 아세테이트의 제조방법 失效
    用于生产亚乙基二乙酸酯的固体催化剂,其生产方法,使用其的连续方法以及通过方法生产亚乙基二乙酸酯的方法

    公开(公告)号:KR1019930003649B1

    公开(公告)日:1993-05-08

    申请号:KR1019900015830

    申请日:1990-10-05

    Inventor: 박대철 조성윤

    CPC classification number: C07C67/29 Y02P20/582 C07C69/16

    Abstract: A soild catalyst is given the formula MaPbS. In formula, M is (CH3CO2)2Pd or RhCl(CO) [P(C6H5)3 2; P is selected from triphenylphosphin, nicotinamide and nicotinic acid; S is a support chosen from kisselguhr, γ-alumina, silica, TiO2, and acitive carbon; a is mole number of M; and b is mole ratio of an accelerating agent. The manufacturing method comprises; (A) dissolving M and P in dichloromethane and adding kisselguhr; (B) after deposition, refluxing at 30-50 deg.C; (C) distillation under diminished pressure; and (D) vacuum drying. In the production of ethylidene diacetate of formula (I), methyl acetate, 20-70 wt.% methyl iodide, hydrogen, CO are reacted in the presence of catalyst (I) and an accelerating agent at 90-250 deg.C, under 20-70 atms.

    Abstract translation: 给出了催化剂式MaPbS。 在式中,M为(CH 3 CO 2)2 Pd或RhCl(CO)[P(C 6 H 5)3 2; P选自三苯基膦,烟酰胺和烟酸; S是选自亲胶,γ-氧化铝,二氧化硅,二氧化钛和游离碳的载体; a是M的摩尔数; b是加速剂的摩尔比。 制造方法包括: (A)将M和P溶解在二氯甲烷中并加入kisselguhr; (B)沉积后,在30-50℃回流; (C)减压蒸馏; 和(D)真空干燥。 在制备式(I)的亚乙基二乙酸酯时,乙酸甲酯,20-70重量%甲基碘,氢,CO在催化剂(I)和促进剂存在下在90-250℃, 20-70公斤。

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