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The Process of Acetonitrile Synthesis over y-Al_2O_3 Promoted by Phosphoric Acid Catalysts

机译:磷酸催化剂促进的乙腈合成乙腈合成的方法

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The influence of principal parameters (reaction temperature, ratio of acetic acid and ammonia, composition of reactionary mixture and promotion of catalysts) on the selectivity and yield of the desired product was studied in the reaction of catalytic acetonitrile synthesis by ammonolysis of acetic acid. The processing of γ-Al_2O_3 by phosphoric acid increases amount of the centers, on which carries out reaction of acetamide dehydration. The kinetic model of a limiting stage of reaction - the acetamide dehydration to acetonitrile was suggested. In the process of ammonolysis of acetic acid it was demonstrated that the use of catalysts promoted by phosphoric acid and ratio NH_3:CH_3COOH=(3-4): 1 at temperatures of a reactor 360-390 °C leads to the increase of acetonitrile productivity to 0.7-0.8 g/cm~3 ·h and allows to minimize formation of by-products.
机译:通过乙酸催化乙腈合成的反应,研究了主参数(反应温度,乙酸和氨,反应性混合物的比例,反动混合物和催化剂的促进)对所需产物的选择性和产率的影响。磷酸的γ-Al_2O_3的处理增加了中心的量,在其上进行乙酰胺脱水的反应。提出了反应阶段的动力学模型 - 提出了对乙腈的乙酰胺脱水。在乙酸的氨解的过程中,证明了使用磷酸和比例促进的催化剂NH_3:CH_3COOH =(3-4):1在反应器360-390℃的温度下导致乙腈生产率的增加至0.7-0.8g / cm〜3·h,并允许最小化副产品的形成。

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