Optimization, kinetic and thermodynamic studies on sustainable biodiesel production from waste cooking oil: An Indian perspective

被引:114
作者
Pugazhendhi, Arivalagan [1 ]
Alagumalai, Avinash [2 ]
Mathimani, Thangavel [3 ]
Atabani, A. E. [4 ]
机构
[1] Ton Duc Thang Univ, Fac Environm & Labour Safety, Innovat Green Prod Synth & Renewable Environm Dev, Ho Chi Minh City, Vietnam
[2] GMR Inst Technol, Dept Mech Engn, Rajam 532127, Andhra Pradesh, India
[3] Natl Inst Technol, Dept Energy & Environm, Tiruchirappalli 620015, Tamil Nadu, India
[4] Erciyes Univ, AFRL, Energy Div, Dept Mech Engn,Fac Engn, TR-38039 Kayseri, Turkey
关键词
Waste cooking oil; Transesterification; Biodiesel; Optimization; Kinetics; Thermodynamic analysis; EMISSION CHARACTERISTICS; ENGINE PERFORMANCE; TRANSESTERIFICATION; EXTRACTION; JATROPHA; FUEL;
D O I
10.1016/j.fuel.2020.117725
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In India, the biodiesel industry is promising and growing at a rapid rate. Several attempts have been made using non edible feedstock to develop the commercial and sustainable biodiesel industry. In this perspective, this study has aimed to optimize four main factors; catalyst quantity, methanol: waste cooking oil molar ratio, mixing intensity and reaction time, which would influence the conversion of waste cooking oil to biodiesel. Response surface methodology integrated with desirability function approach was used to determine the best operative conditions. The optimal reaction parameters for maximum biodiesel yield (90 +/- 0.25%) were identified as 0.6%w/w catalyst loading, 10.6:1 methanol to waste cooking ratio, 559 rpm mixing intensity and 63 min reaction time. The study of reaction kinetics revealed that the experimental data followed the first order reaction kinetics and the energy required to activate the molecules to undergo chemical transformation was calculated as 57.82 kJ/mol. The important thermodynamic parameters such as enthalpy (Delta H), entropy (Delta S), and the Gibbs free energy (Delta G) were estimated to assess the characteristics of the transesterification process. The values of the thermodynamic parameters were found to be Delta H = 55.09 kJ/mol, Delta S =-0.103 kJ/mol K and Delta G = 89.90 kJ/mol, respectively.
引用
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页数:8
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