Comprehensive Review on Biodiesel Production from Palm Oil Mill Effluent

被引:19
|
作者
Zulqarnain [1 ]
Yusoff, Mohd Hizami Mohd [1 ]
Ayoub, Muhammad [1 ]
Hamza Nazir, Muhammad [1 ]
Zahid, Imtisal [1 ]
Ameen, Mariam [1 ]
Abbas, Wajahat [2 ]
Shoparwe, Noor Fazliani [3 ]
Abbas, Nadir [4 ]
机构
[1] Univ Teknol PETRONAS, Dept Chem Engn, HICoE Ctr Biofuel & Biochem Res, Inst Self Sustainable Bldg, Seri Iskandar 32610, Perak, Malaysia
[2] Univ Engn & Technol, Dept Environm Engn, Taxila 47080, Pakistan
[3] Univ Malaysia Kelantan, Fac Bioengn & Technol, Jeli Campus, Jeli 17600, Kelantan, Malaysia
[4] Univ Hail, Coll Engn, Dept Chem Engn, Hail 81441, Saudi Arabia
来源
CHEMBIOENG REVIEWS | 2021年 / 8卷 / 05期
关键词
Biodiesel; Palm oil mill effluent; Supercritical biodiesel production; Transesterification; WASTE COOKING OIL; RESPONSE-SURFACE METHODOLOGY; OF-THE-ART; RAPESEED OIL; LIFE-CYCLE; CATALYZED TRANSESTERIFICATION; HETEROGENEOUS CATALYSTS; PROCESS INTENSIFICATION; SUPERCRITICAL METHANOL; ECONOMIC-ASSESSMENT;
D O I
10.1002/cben.202100007
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Biodiesel synthesis processes including pyrolysis, direct blending, transesterification, and advanced technologies such as microwave- and ultrasound-assisted and supercritical processes from palm oil mill effluent (POME) are reviewed to highlight the significance and advances in terms of process sustainability and cost. POME as the most contaminated waste can be effectively utilized for biodiesel production. Supercritical transesterification offers more advantages over the other processes including higher reaction rate, without catalyst constraint, producing pure glycerol, and simple product separation process. The addition of co-solvents like CO2 should be investigated for supercritical biodiesel production from POME. Although POME is an inexpensive source to synthesize biodiesel, innovative processes are needed to maximize the oil recovery from POME. Optimization of transesterification parameters is required for high production yields and sustainable processing.
引用
收藏
页码:439 / 462
页数:24
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