TY - GEN
T1 - Utilization of Oil Recovery Process on Spent Bleaching Earth into Non-Hazardous Waste
AU - Tetrisyanda, Rizky
AU - Wibawa, Gede
N1 - Publisher Copyright:
© 2024 Trans Tech Publications Ltd, Switzerland.
PY - 2024
Y1 - 2024
N2 - Crude palm oil purifying process is an important process in refining vegetable and animal oils to remove the impurities. This process produces spent bleaching earth (SBE) waste which needs to be reprocessed before being released into the environment because it contains 20-30% of oil. However, based on Government Regulation Number 22/2021, SBE was removed from the list of hazardous waste on condition the oil contained is under 3%. In this study, the oil content in SBE was extracted using maceration process. The aim of this study was to measure the remain oil content in de-oiled bleaching earth (de-OBE) using various solvent. The solvents used are n-hexane, acetone, and ethanol with SBE to solvent ration. The highest yield obtained was 22% using n-hexane as a solvent. To determine the quality of the recovered oil, water and free fatty acid contained were analyzed. After being extracted, the remaining oil content in the de-OBE was measured. The remaining oil content in de-OBE for n-hexane and acetone as solvent was under 3% but for ethanol the oil content in de-OBE was high up to 15%.
AB - Crude palm oil purifying process is an important process in refining vegetable and animal oils to remove the impurities. This process produces spent bleaching earth (SBE) waste which needs to be reprocessed before being released into the environment because it contains 20-30% of oil. However, based on Government Regulation Number 22/2021, SBE was removed from the list of hazardous waste on condition the oil contained is under 3%. In this study, the oil content in SBE was extracted using maceration process. The aim of this study was to measure the remain oil content in de-oiled bleaching earth (de-OBE) using various solvent. The solvents used are n-hexane, acetone, and ethanol with SBE to solvent ration. The highest yield obtained was 22% using n-hexane as a solvent. To determine the quality of the recovered oil, water and free fatty acid contained were analyzed. After being extracted, the remaining oil content in the de-OBE was measured. The remaining oil content in de-OBE for n-hexane and acetone as solvent was under 3% but for ethanol the oil content in de-OBE was high up to 15%.
KW - maceration
KW - oil recovery
KW - spent bleaching earth
UR - http://www.scopus.com/inward/record.url?scp=85186700959&partnerID=8YFLogxK
U2 - 10.4028/p-GkR8k7
DO - 10.4028/p-GkR8k7
M3 - Conference contribution
AN - SCOPUS:85186700959
SN - 9783036414959
T3 - Advances in Science and Technology
SP - 21
EP - 25
BT - 4th International Seminar on Fundamental and Application of Chemical Engineering, ISFAChE 2022
A2 - Ni'mah, Hikmatun
A2 - Wiguno, Annas
A2 - Tetrisyanda, Rizky
A2 - Degreve, Jan
A2 - Shimada, Manabu
A2 - Ju, Yi-Hsu
A2 - Ahmad, Arshad
A2 - Anugraha, Rendra Panca
A2 - Fahmi, Fahmi
A2 - Meka, Wahyu
A2 - Rozy, Mohammad Irwan Fatkhur
PB - Trans Tech Publications Ltd
T2 - 4th International Seminar on Fundamental and Application of Chemical Engineering, ISFAChE 2022
Y2 - 26 October 2022 through 27 October 2022
ER -
