TY - JOUR
T1 - Mesoporous acidic catalysts synthesis from dual-stage and rising co-current gasification char
T2 - Application for fame production from waste cooking oil
AU - Ahmad, Junaid
AU - Rashid, Umer
AU - Patuzzi, Francesco
AU - Alamoodi, Nahla
AU - Choong, Thomas Shean Yaw
AU - Soltani, Soroush
AU - Ngamcharussrivichai, Chawalit
AU - Nehdi, Imededdine Arbi
AU - Baratieri, Marco
N1 - Funding Information:
This research was funded by a Putra IPB grant to the University Putra Malaysia (UPM) Serdang, through GP-IPB/2016/9490400 research grant vote number. The authors acknowledge King Saud University (Riyadh, Saudi Arabia) for the funding of this research through the Researchers Supporting Project number (RSP-2019/80).
Publisher Copyright:
© 2020 by the authors.
PY - 2020/2/1
Y1 - 2020/2/1
N2 - The main purpose of this work is to investigate the application options of the char produced from gasification plants. Two promising mesoporous acidic catalysts were synthesized using char as a support material. Two char samples were collected from either a dual-stage or a rising co-current biomass gasification plant. The catalysts produced from both gasification char samples were characterized for their physiochemical and morphological properties using N2 physorption measurement, total acidity evaluation through TPD-NH3, functional groups analysis by FT-IR, and morphology determination via FESEM. Results revealed that the dual-stage char-derived mesoporous catalyst (DSC-SO4) with higher specific surface area and acidic properties provided higher catalytic activity for fatty acid methyl esters (FAME) production from waste cooking oil (WCO) than the mesoporous catalyst obtained from char produced by rising co-current gasification (RCC-SO4). Furthermore, the effects of methanol/oil molar ratio (3:1-15:1), catalyst concentration (1-5 wt.% of oil), and reaction time (30-150 min) were studied while keeping the transesterification temperature constant at 65 °C. The optimal reaction conditions for the transesterification ofWCOwere 4 wt.% catalyst concentration, 12:1 methanol/oil molar ratio, and 90 min operating time. The optimized reaction conditions resulted in FAME conversions of 97% and 83% over DSC-SO4 and RCC-SO4 catalysts, respectively. The char-based catalysts show excellent reusability, since they could be reused six times without any modification.
AB - The main purpose of this work is to investigate the application options of the char produced from gasification plants. Two promising mesoporous acidic catalysts were synthesized using char as a support material. Two char samples were collected from either a dual-stage or a rising co-current biomass gasification plant. The catalysts produced from both gasification char samples were characterized for their physiochemical and morphological properties using N2 physorption measurement, total acidity evaluation through TPD-NH3, functional groups analysis by FT-IR, and morphology determination via FESEM. Results revealed that the dual-stage char-derived mesoporous catalyst (DSC-SO4) with higher specific surface area and acidic properties provided higher catalytic activity for fatty acid methyl esters (FAME) production from waste cooking oil (WCO) than the mesoporous catalyst obtained from char produced by rising co-current gasification (RCC-SO4). Furthermore, the effects of methanol/oil molar ratio (3:1-15:1), catalyst concentration (1-5 wt.% of oil), and reaction time (30-150 min) were studied while keeping the transesterification temperature constant at 65 °C. The optimal reaction conditions for the transesterification ofWCOwere 4 wt.% catalyst concentration, 12:1 methanol/oil molar ratio, and 90 min operating time. The optimized reaction conditions resulted in FAME conversions of 97% and 83% over DSC-SO4 and RCC-SO4 catalysts, respectively. The char-based catalysts show excellent reusability, since they could be reused six times without any modification.
KW - Biodiesel
KW - Characterization
KW - Dual-stage gasification char
KW - Post-sulfonation
KW - Rising co-current gasification char
KW - Transesterification
UR - http://www.scopus.com/inward/record.url?scp=85082166683&partnerID=8YFLogxK
U2 - 10.3390/ma13040871
DO - 10.3390/ma13040871
M3 - Article
AN - SCOPUS:85082166683
SN - 1996-1944
VL - 13
JO - Materials
JF - Materials
IS - 4
M1 - 871
ER -