Experimental exergy analysis of transesterification in biodiesel production

被引:39
作者
Khoobbakht, Golmohammad [1 ]
Kheiralipour, Kamran [2 ]
Rasouli, Hamed [3 ]
Rafiee, Mojtaba [4 ]
Hadipour, Mehrdad [5 ,6 ]
Karimi, Mahmoud [4 ]
机构
[1] Payame Noor Univ, Dept Agr Engn, Tehran, Iran
[2] Ilam Univ, Mech Engn Biosyst Dept, Ilam, Iran
[3] Univ Tehran, Coll Abouraihan, Dept Agrotechnol, Tehran, Iran
[4] Arak Univ, Dept Biosyst Engn, Arak 3815688349, Iran
[5] Arak Univ, Fac Agr & Nat Resources, Dept Environm, Arak, Iran
[6] Univ Kharazmi, Fac Biol Sci, Tehran, Iran
关键词
Exergy loss; Biodiesel; Transesterification; Thermodynamic analysis; Conversion; WASTE COOKING OIL; JATROPHA BIODIESEL; BLENDED LEVELS; OPTIMIZATION; ETHANOL; BIOMASS; DIESEL; ENERGY; LIPASE; WATER;
D O I
10.1016/j.energy.2020.117092
中图分类号
O414.1 [热力学];
学科分类号
摘要
Exergy flow analysis is applied to account wastes, determine the exergetic efficiency, compare substitutes and other types of energy sources and also define economic and environmental policies for resource use. The present study focuses on the exergy flow analysis of biodiesel production by esterification and transesterification of waste cooking canola oil to achieve benefits such as reducing material and energy consumptions and improving energy and exergy efficiencies. The input amounts of esterification for all the runs were kept constant, while the runs of transesterification were carried out in a variety of mass and energy input values as the experimental variables. The thermodynamics analysis was applied to determine exergy input and output of the system for the experimental runs. Impacts of experiment variables, including methanol:oil molar ratio, potassium hydroxide concentration and the reaction temperature of transesterification were evaluated on exergy efficiency and exergy loss in the transesterification. The maximum exergy efficiency (91.7%) and the minimum exergy loss (4320 kJ/kg biodiesel) were achieved at methanol:oil molar ratio of 8:1, potassium hydroxide concentration of 1 wt% and the reaction temperature of 55 degrees C. Excessive use of methanol and catalyst reduced the yield and the exergy efficiency through increasing exergy loss by waste materials. (C) 2020 Elsevier Ltd. All rights reserved.
引用
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页数:8
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