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首页> 外文期刊>Clean technologies and environmental policy >Liquid-liquid-liquid phase-transfer catalysis for cleaner and selective etherification of p-hydroxy-biphenyl with benzyl chloride to 1,1'-biphenyl-4-(phenylmethoxy)
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Liquid-liquid-liquid phase-transfer catalysis for cleaner and selective etherification of p-hydroxy-biphenyl with benzyl chloride to 1,1'-biphenyl-4-(phenylmethoxy)

机译:用于对羟基联苯与苄基氯的更清洁和选择性醚化的液-液-液相转移催化,生成1,1'-联苯-4-(苯基甲氧基)

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摘要

Conversion of bi-liquid phase transfer catalysis (PTC) into a tri-liquid PTC system presents several advantages in terms of enhancement of reaction rates and selectivity. These improvements lead to a minimization of waste, reduction in reactor volume and processing times by orders of magnitude in comparison with a liquid-liquid PTC process. The O-alkylation (etherification) of 4-hy-droxybiphenyl with benzyl chloride to 1,1'-biphenyl-4-(phenylmethoxy) was carried out under L-L-L PTC system with 100% selectivity at 50℃. The resulting product is commercially used in fine chemical industry and to produce novel materials. The catalyst-rich third phase can be recycled many times, thereby leading to profitability and waste minimization. A reaction mechanism and kinetic model are developed and validated against experimental data, which include the effect of different variables on reaction rates and selectivity.
机译:在提高反应速率和选择性方面,双液相转移催化(PTC)转化为三液PTC系统具有多个优点。与液-液PTC方法相比,这些改进导致废物的最小化,反应器体积的减少和处理时间的数量级减少。在L-L-L PTC体系下,在50℃下以100%的选择性,将4-羟基联苯与苄基氯的O-烷基化(醚化)反应为1,1'-联苯-4-(苯基甲氧基)。所得产物可商业用于精细化学工业并生产新型材料。富含催化剂的第三相可以多次循环使用,从而实现收益和废物最小化。建立了反应机理和动力学模型,并针对实验数据进行了验证,其中包括不同变量对反应速率和选择性的影响。

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