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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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