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Effect of Process Parameters on Yield of Biofuel Production from Waste Virgin Coconut Oil

机译:工艺参数对废椰子油生产生物燃料产量的影响

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This research aimed to determine the influence of process parameters on yields of biofuel production by hydrocracking of waste virgin coconut oil using HZSM-5 zeolite catalyst and to determine statistical relationship of yields of biofuels with the parameters by Pearson’s correlation. The various operating parameters in batch reactor were a reaction temperature (350-400°C), an initial hydrogen pressure (20-40 bar), and a reaction time (1-3 h). The highest yields of gasoline (6.79 wt%) and kerosene (31.38 wt%) were achieved under a temperature at 400°C, initial hydrogen pressure at 40 bar, and a reaction time of 3 h. The highest yield of diesel of 58.62 wt% was achieved at a reaction time of 1 h under temperature 400°C and initial hydrogen pressure 40 bar. The experimental data were analyzed by input-output model with the coefficient of determination (R2) of yield prediction ranging from 0.86 to 0.92. The Pearson’s correlation coefficients show strong dependence of reaction temperature and time on hydrocarbon chains of various length. Yields of shorter hydrocarbon chains such as gasoline and kerosene required higher reaction temperature and longer reaction time and vice versa. Pressure dependence on yields of biofuels was insignificant.
机译:这项研究旨在确定工艺参数对废旧椰子油使用HZSM-5沸石加氢裂化的过程参数对生物燃料产量的影响,并通过皮尔森相关性确定生物燃料产量与参数之间的统计关系。间歇反应器中的各种操作参数是反应温度(350-400℃),初始氢压力(20-40bar)和反应时间(1-3h)。在400°C的温度,40 bar的初始氢气压力和3 h的反应时间下,汽油(6.79 wt%)和煤油(31.38 wt%)的最高收率。在温度为400°C和初始氢气压力为40 bar的条件下,在1小时的反应时间内,柴油的最高收率为58.62 wt%。通过输入-输出模型对实验数据进行分析,产量预测的决定系数(R2)为0.86至0.92。皮尔逊相关系数显示出反应温度和时间对各种长度的烃链的强烈依赖性。较短的烃链(例如汽油和煤油)的产率需要较高的反应温度和较长的反应时间,反之亦然。压力对生物燃料产量的依赖性微不足道。

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