TY - JOUR
T1 - Treatment of acidic crude palm oil using supported benzenesulfonic acid-based deep eutectic solvents in trickle bed reactor
AU - Hayyan, Adeeb
AU - Syed Putra, Sharifah Shahira
AU - Chow, M. K.
AU - Alanazi, Yousef Mohammed
AU - Saleh, Jehad
AU - AlNashef, Inas M.
AU - Gupta, Bhaskar Sen
N1 - Publisher Copyright:
© 2024
PY - 2024/12
Y1 - 2024/12
N2 - 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 °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 °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.
AB - 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 °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 °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.
KW - Activated carbon
KW - Biodiesel
KW - Deep eutectic solvent
KW - Esterification
KW - Low grade crude palm oil
KW - Trickle bed reactor
UR - http://www.scopus.com/inward/record.url?scp=85208067444&partnerID=8YFLogxK
U2 - 10.1016/j.mtsust.2024.101021
DO - 10.1016/j.mtsust.2024.101021
M3 - Article
AN - SCOPUS:85208067444
VL - 28
JO - Materials Today Sustainability
JF - Materials Today Sustainability
M1 - 101021
ER -