Esterification of oleic acid to biodiesel using biowaste-based solid acid catalyst under microwave irradiation

被引:16
作者
Kushwaha, Tribhuvan [1 ]
Ao, Supongsenla [1 ]
Ngaosuwan, Kanokwan [2 ]
Assabumrungrat, Suttichai [3 ,4 ]
Gurunathan, Baskar [5 ]
Rokhum, Samuel Lalthazuala [1 ,6 ]
机构
[1] Natl Inst Technol Silchar, Dept Chem, Silchar, India
[2] Rajamangala Univ Technol Krungthep, Fac Engn, Chem Engn Div, Bangkok, Thailand
[3] Chulalongkorn Univ, Fac Engn, Ctr Excellence Catalysis & Catalyt React Engn, Dept Chem Engn, Bangkok, Thailand
[4] Chulalongkorn Univ, Fac Engn, Biocircular Green econ Technol & Engn Ctr BCGeTEC, Bangkok, Thailand
[5] St Josephs Coll Engn, Dept Biotechnol, Chennai, India
[6] Natl Inst Technol Silchar, Dept Chem, Silchar 788010, Assam, India
关键词
biodiesel; renewable energy; sustainability; waste management; BIOCHAR-BASED CATALYST; HETEROGENEOUS CATALYST; OIL; TRANSESTERIFICATION; OPTIMIZATION; PERFORMANCE; STABILITY; TRENDS; OXIDES; MG;
D O I
10.1002/ep.14170
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A novel carbon-based solid catalyst was synthesized from waste biomass of watermelon peel (Citrullus lanatus) by one pot carbonization and functionalization with H2SO4 for biodiesel production. Oleic acid was utilized as a test substrate in this study given that it is a key component for majority of feedstocks used for biodiesel production. Synthesized catalyst was extensively characterized by X-ray diffraction, Fourier transform infrared, thermogravimetric analysis, X-ray photoelectron spectroscopy, scanning electron microscopy-EDX and Brunauer-Emmett Teller analysis. The catalyst revealed aromatic structure, hydrophilic -OH and -COOH groups as well as a high density of -SO3H active centres with a total acidity of 3.6 mmol g(-1). Using the optimized reaction condition (MeOH: oleic acid molar ratio 20:1, catalyst loading 8 wt.%, temperature 100 degrees C and reaction time of 60 min) under microwave irradiation (50 W, 100 psi) a conversion as high as 94.36 +/- 0.3% of oleic acid to biodiesel was reported. Activation energy of the esterification was found to be 38.16 kJ mol(-1). Catalyst recovery was probed to over five reaction cycles, with a modest loss in activity (81.73 +/- 0.4% conversion in the fifth cycle) resulting from limited active site leaching.
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页数:13
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