TY - JOUR
T1 - Design of portable biodiesel plant from waste cooking oil
AU - Samad, Alan Try Putra
AU - Putri, Dwini Normayulisa
AU - Perdani, Meka Saima
AU - Utami, Tania Surya
AU - Arbianti, Rita
AU - Hermansyah, Heri
N1 - Funding Information:
The authors would like to thank for the support provided by Universitas Indonesia, Ministry of Research, Technology and Higher Education Republic of Indonesia, and for the publication support provided by the United States Agency for International Development (USAID) through the Sustainable Higher Education Research Alliance (SHERA) Program for Unievrs dIeonniass’ Scientiic Mof ,gdelin pp,licatioAn eseaRrch dan Tinrgain orf itCy - centered Innovation and Technology #IIE-00000078-UI-1.
Publisher Copyright:
© 2018 The Authors. Published by Elsevier Ltd.
PY - 2018
Y1 - 2018
N2 - The design of portable biodiesel plant from waste cooking oil has been done simultaneously based on biodiesel standard of SNI 7182: 2012. Design of biodiesel production involves several processes including esterification, transesterification, decantation, vacuum evaporation, and ultra-filtration. Production of biodiesel has been simulated using several software packages. Based on the simulation conducted, the esterification process was able to convert 92.8% of FFA into FAME by using sulfuric acid as the catalyst with 10% w/w of FFA. Transesterification showed the biodiesel yield of 90% by using NaOH as the catalyst with 1% w/w of triglyceride. Evaporation on vacuum system was able to obtain biodiesel with methanol content less than 0.5% with lower energy consumption. Purification of biodiesel using ultra-filtration requires considerable energy but it was able to produce the purity rate of biodiesel up to 99.8% with relatively shorter time.
AB - The design of portable biodiesel plant from waste cooking oil has been done simultaneously based on biodiesel standard of SNI 7182: 2012. Design of biodiesel production involves several processes including esterification, transesterification, decantation, vacuum evaporation, and ultra-filtration. Production of biodiesel has been simulated using several software packages. Based on the simulation conducted, the esterification process was able to convert 92.8% of FFA into FAME by using sulfuric acid as the catalyst with 10% w/w of FFA. Transesterification showed the biodiesel yield of 90% by using NaOH as the catalyst with 1% w/w of triglyceride. Evaporation on vacuum system was able to obtain biodiesel with methanol content less than 0.5% with lower energy consumption. Purification of biodiesel using ultra-filtration requires considerable energy but it was able to produce the purity rate of biodiesel up to 99.8% with relatively shorter time.
KW - Biodiesel
KW - Portable biodiesel plant
KW - Waste cooking oil
UR - http://www.scopus.com/inward/record.url?scp=85057433463&partnerID=8YFLogxK
U2 - 10.1016/j.egypro.2018.10.062
DO - 10.1016/j.egypro.2018.10.062
M3 - Conference article
AN - SCOPUS:85057433463
SN - 1876-6102
VL - 153
SP - 263
EP - 268
JO - Energy Procedia
JF - Energy Procedia
T2 - 5th International Conference on Energy and Environment Research, ICEER 2018
Y2 - 23 July 2018 through 27 July 2018
ER -