Treatment of acidic crude palm oil using supported benzenesulfonic acid-based deep eutectic solvents in trickle bed reactor

被引:1
作者
Hayyan, Adeeb [1 ,2 ]
Putra, Sharifah Shahira Syed [1 ]
Chow, M. K. [1 ]
Alanazi, Yousef Mohammed [3 ]
Saleh, Jehad [3 ]
Alnashef, Inas M. [4 ,5 ,6 ]
Sen Gupta, Bhaskar [7 ]
机构
[1] Univ Malaya, Fac Engn, Dept Chem Engn, 50603 Kuala Lumpur, Malaysia
[2] Univ Malaya, Fac Engn, Sustainable Proc Engn Ctr SPEC, Kuala Lumpur 50603, Malaysia
[3] King Saud Univ, Coll Engn, Dept Chem Engn, PO 19 Box 800, Riyadh 11421, Saudi Arabia
[4] Khalifa Univ Sci & Technol, Dept Chem Engn, POB 127788, Abu Dhabi, U Arab Emirates
[5] Khalifa Univ, Ctr Membranes & Adv Water Technol CMAT, POB 127788, Abu Dhabi, U Arab Emirates
[6] Khalifa Univ, Res & Innovat Ctr Graphene & Mat 2D RIC2D, POB 127788, Abu Dhabi, U Arab Emirates
[7] Heriot Watt Univ, Water Acad, Sch Energy Geosci Infrastruct & Soc, Edinburgh Campus, Edinburgh EH14 4AS, Scotland
关键词
Biodiesel; Deep eutectic solvent; Esterification; Low grade crude palm oil; Trickle bed reactor; Activated carbon; WASTE COOKING OIL; BIODIESEL PRODUCTION; HETEROGENEOUS CATALYST; TRANSESTERIFICATION; OPTIMIZATION; CARBON;
D O I
10.1016/j.mtsust.2024.101021
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In this study, a deep eutectic solvent (DES) from benzenesulfonic acid and choline chloride (BZSA-ChCl-DES) was prepared for the treatment of high free fatty acids (FFA) in acidic crude palm oil (ACPO). The DES was impregnated into activated carbon (AC-DES) to produce a supported catalyst used in a trickle bed reactor (TBR) for FFA esterification. Under optimal conditions, using 8 g of AC-DES at 60 degrees C, with ACPO and methanol flow rates of 1 mL/min and 4 mL/min, respectively, the TBR successfully treated 3.5 L of ACPO. A batch reactor, used for comparison, showed that the continuous TBR process required less catalyst per gram of treated oil (2.87 mg catalyst/g) which can enhance the recyclability. Moreover, the continuous process could sustain up to five recycle runs that can treat 1.5 L under optimal conditions (3.5 wt% catalyst dosage, 10:1 M ratio, 60 degrees C reaction temperature, and 30 min). This approach presents a promising continuous approach for converting high FFA to fatty acid methyl ester (FAME) for biodiesel production.
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页数:10
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