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An improvement study of biodiese! production from rice bran via non-catalytic in-situ transesterification using a subcritical water-methanol mixture

机译:生物纤维的改进研究!通过使用亚临界水 - 甲醇混合物的非催化原位酯交换从米糠生产

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A non-catalytic in-situ transesterification of biodiesel production from rice bran using subcritical water-methanol mixture was found to be unaffected by initial moisture and free fatty acids (FFA) contents. The method has been known as environmentally friendly conversion since no catalyst was used. Acid catalyst has an important role in in-situ transesterification due to their ability to accelerate the oil extraction from the bran and the reaction rate. In this study, CO2 as pressurizing gas was added into subcritical water methanol mixture to increased yield and content of biodiesel. Effect of different operation pressure (P = 40-100 bar) at subcritical water methanol mixture (T = 200°C) and reaction time of 180 min on the yield and content of biodiesel were investigated. Rice bran with initial FFA content of 40.42 % has been subjected into hydrothermal reactor together with water methanol mixture to produce rice bran oil (RBO)-based biodiesel. The more CO2 as pressurizing gas was added into the hydrothermal reactor, the more yield and content of biodiesel were obtained. The highest yield and content of biodiesel of 98.00±1.41% and 83.93%, respectively, were produced under P = 100 bar.
机译:发现使用亚临界水 - 甲醇混合物的水稻糠醛的生物柴油生产的非催化原位酯交换不受初始水分和游离脂肪酸(FFA)含量的影响。该方法已被称为环境友好的转化,因为不使用催化剂。由于它们加速来自麸皮的油萃取和反应速率,酸催化剂在原位酯交换中具有重要作用。在该研究中,将CO 2作为加压气体加入到亚临界水甲醇混合物中以增加生物柴油的产率和含量。研究了不同操作压力(P = 40-100巴)在亚临界水甲醇混合物(T = 200℃)和180分钟的反应时间对生物柴油的产率和含量的反应时间。初始FFA含量为40.42%的米糠与水甲醇混合物一起进行水热反应器,以生产米糠油(RBO)的基碘。加入加压气体的二氧化碳越多,得到了生物柴油的产率越多。在P = 100巴下,分别在98.00±1.41%和83.93%的生物柴油的最高收率和83.93%。

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