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Transesterification of Mixture of Castor Oil and Sunflower Oil in Millichannel Reactor: FAME Yield and Flow Behaviour

机译:米西克克料反应器中蓖麻油和葵花籽油混合物的酯交换:名称产量和流动行为

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Transesterification of castor oil, sunflower oil and mixture of both oils were conducted in a millichannel reactor with 1.6 mm internal diameter. The flow behavior of the sample in millichannel reactor was observed. Both of the oil was mixed from 100 mL of castor oil until 20 mL of castor oil with total amount of 100 mL solution before used in the reaction. The alkali catalyst was mixed together with methanol before entering the reactor. In this study, the behavior of the flow pattern inside the millichannel reactor was observed under fixed parameters which are 21:1 methanol-to-oil molar ratio, 5.4 wt% of KOH concentration in methanol, 180 s of residence time and 60 °C of temperature. The FFA value of both the oils was less than 2 mg-KOH/g-oil. The viscosity and density of the oils were determined before and after mixing the oils. The flow behaviour of the castor oil formed parallel flow throughout the reactor while sunflower oil formed slug flow in the reactor. When the volume of castor oil is reduced from 100 mL to 20 mL, the flow behaviours of the mixture oil were changed from slug flow at upstream to parallel flow at downstream. The formation of slug flow in the reactor improved the biodiesel yield: 88.4% of FAME yield.
机译:蓖麻油,向日葵油和两种油的混合物的酯交换反应是在一反应器millichannel 1.6内径进行。没有观察到反应器millichannel样品的流动行为。两个油的从100毫升蓖麻油的混合,直到20毫升的蓖麻油与在反应中使用之前100mL的溶液总量。碱催化剂在进入反应器之前用甲醇混合在一起。 1甲醇与油的摩尔比,在甲醇中的KOH浓度为5.4%(重量),180秒的停留时间和60℃下:在该研究中,根据固定的参数,其是21观察到的millichannel反应器内的流动模式的行为的温度。两个油的FFA值小于2毫克KOH /克的油。油的粘度和密度之前和混合油后进行了测定。而向日葵油反应器中形成段塞流的蓖麻油的流动行为形成整个反应器中的平行流。当蓖麻油的容积从100毫升降低到20毫升,将混合物油的流动行为进行从弹状流改变在上游到下游在平行流动。在反应器段塞流的形成改进的生物柴油产率:产率FAME的88.4%。

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