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首页> 外文期刊>Polish journal of chemical technology >Catalytic hydrogenation in the process of 2-((1-benzylpiperidin-4-yl) methyl)-5,6-dimethoxy-2,3-dihydroinden-1-one hydrochloride synthesis I. Catalyst screening and finding the optimal reaction conditions
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Catalytic hydrogenation in the process of 2-((1-benzylpiperidin-4-yl) methyl)-5,6-dimethoxy-2,3-dihydroinden-1-one hydrochloride synthesis I. Catalyst screening and finding the optimal reaction conditions

机译:2-((1-苄基哌啶-4-基)甲基)-5,6-二甲氧基-2,3-二氢茚-1-酮盐酸盐合成过程中的催化加氢反应I.催化剂的筛选及最佳反应条件的确定

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1Catalytic hydrogenation of 2-((1-benzyl-1,2,3,6-tetrahydropyridin-4-yl)methylene)-5,6-dimethoxy-2,3-dihydroinden- 1-one hydrochloride () to 2-((1-benzylpiperidin-4-yl)methyl)-5,6-dimethoxy-2,3-dihydroinden- 1-one hydrochloride (2) was investigated in the batch-slurry reactor. The 5% Pt/C catalyst was chosen to search the optimal reaction conditions because of its higher catalytic activity compared to other catalysts used in the work. To investigate the catalyst activity, selectivity and stability, the effect of agitation speed, catalyst loading, solvent, temperature, hydrogen pressure and catalyst reuse were studied.The initial rate of hydrogenation increases with the increase of catalyst loading, with the temperature and solvent polarity, if alcohols were used as solvents. The hydrogenation rate decreases with higher hydrogen pressure and that was explained by competitive adsorption of both reactants.The results also indicate that 5% Pt/C is a promising catalyst for 1 hydrogenation because at relatively mild reaction conditions selectivity towards main product was high (98%) and catalyst maintains its activity during successive runs.
机译:1将2-((1-苄基-1,2,3,6-四氢吡啶-4-基)亚甲基)-5,6-二甲氧基-2,3-二氢茚-1-酮盐酸盐(1)催化加氢成2-(在间歇淤浆反应器中研究了(1-苄基哌啶-4-基)甲基)-5,6-二甲氧基-2,3-二氢茚-1-酮盐酸盐(2)。选择5%Pt / C催化剂以寻找最佳反应条件是因为与工作中使用的其他催化剂相比,它具有更高的催化活性。为了研究催化剂的活性,选择性和稳定性,研究了搅拌速度,催化剂负载量,溶剂,温度,氢气压力和催化剂再利用的影响。随着催化剂负载量的增加,温度和溶剂极性的增加,氢化的起始速率也随之增加。 ,如果将酒精用作溶剂。氢化速率随氢气压力的升高而降低,这可以通过两种反应物的竞争性吸附来解释。结果还表明,5%Pt / C是一种有希望的1加氢催化剂,因为在相对温和的反应条件下,对主产物的选择性很高(98 %),并且催化剂在连续运行期间保持其活性。

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