Waste sugarcane bagasse-derived nanocatalyst for microwave-assisted transesterification: Thermal, kinetic and optimization study

被引:28
|
作者
Nazir, Muhammad H. [1 ]
Ayoub, Muhammad [1 ]
Zahid, Imtisal [1 ]
Shamsuddin, Rashid B. [1 ]
Zulqarnain [1 ]
Ameen, Mariam [1 ]
Sher, Farooq [2 ]
Farrukh, Sarah [3 ]
机构
[1] Univ Teknol Petronas, Inst Self Sustainable Bldg, Dept Chem Engn, HICoE Ctr Biofuel & Biochem Res CBBR, Bandar Seri Iskandar 32610, Perak, Malaysia
[2] Nottingham Trent Univ, Sch Sci & Technol, Dept Engn, Nottingham NG11 8NS, England
[3] Natl Univ Sci & Technol, Sch Chem & Mat Engn, Dept Chem Engn, Islamabad, Pakistan
来源
关键词
renewable energy; biodiesel synthesis; process optimization; biofuels; waste cooking oil and sugarcane bagasse; SOLID ACID CATALYST; TEXTILE DYEING SLUDGE; BIODIESEL PRODUCTION; HETEROGENEOUS CATALYST; OLEIC-ACID; COOKING OIL; PALM OIL; KERNEL SHELL; FATTY-ACIDS; FRYING OIL;
D O I
10.1002/bbb.2264
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
The production of biodiesel has increased globally during the last decade to overcome the problems of increasing prices of petro-diesel and the depletion of fossil fuels. The present study aimed to utilize agro-waste sugarcane bagasse (SCB) to synthesize a heterogeneous acid catalyst for biodiesel production using waste cooking oil. Waste sugarcane bagasse was converted into biochar through partial carbonization and activated via sulfonation by using acid solutions of different concentration i.e., 1M, 3M, 5M and concentrated sulfuric acid at a sulfonation temperature of 180 degrees C for 5 h. The prepared catalysts were characterized by using Fourier transform infrared spectroscopy (FTIR), thermogravimetric analysis (TGA), scanning electron microscopy (SEM), the Brunauer-Emmett-Teller (BET) technique, X-ray diffraction (XRD), and the Carbon, Hydrogen, Nitrogen and Sulfur (CHNS) analyzer. The prepared catalyst exhibited an excellent surface area of 20.78 m(2) g(-1) and a total acid density of 3.94 mmol g(-1). The biodiesel production process was optimized by varying reaction temperature from (40-70 degrees C), methanol to oil molar ratio (5:1-20:1), catalyst loading (1-7 wt.%) and reaction time (5-25 min) by using a microwave reactor. The maximum conversion of 95.45% and yield of 92.12% was obtained under optimum conditions: catalyst loading 5 wt%, methanol-to-oil molar ratio (15:1), temperature (60 degrees C) after 15 min. The results of the experiments were validated by using response surface methodology, which validated the predicted model. The kinetic study of experiments showed that the use of sulfonated catalysts lowered the activation energy (10.5 kJ mol(-1)) and reactants attained an equilibrium point after a short interval under microwave heating. Reusability of catalyst up to seven cycles with 77.34% yield of biodiesel using low-grade feedstock showed that the catalyst is stable and can be used for sustainable biodiesel production. The utilization of wastes for catalyst synthesis and for biodiesel production can help to minimize the overall production cost of biodiesel. (c) 2021 Society of Chemical Industry and John Wiley & Sons, Ltd
引用
收藏
页码:122 / 141
页数:20
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