Zobrazeno 1 - 8
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pro vyhledávání: '"Fon Yee Han"'
Publikováno v:
Materials Today: Proceedings. 5:22118-22122
Single-phase transesterification of palm oil with methanol catalyzed by homogeneous alkaline catalyst was carried out in a laboratory scale batch reactor at 298, 308 and 323 K in the presence of methylethylketone (MEK) as a co-solvent. Most of the pr
Publikováno v:
Materials Today: Proceedings. 5:22123-22127
This paper aims to formulate a model describing the overall transesterification rate of vegetable oil with methanol catalyzed by homogeneous catalyst. Transesterification of palm oil with methanol catalyzed by KOH was carried out in a laboratory scal
Publikováno v:
Biomass and Bioenergy. 143:105834
Biodiesel production from microalgae requires energy-intensive dewatering before lipid extraction and transesterification. In order to avoid this energy penalty, one-path direct transesterification of wet microalgae (Chlorella vulgaris) using supercr
Autor:
Chung Yiin Wong, Man Kee Lam, Wan Nadiah Amalina Kadir, Suzana Yusup, Kunlanan Kiatkittipong, Siti-Suhailah Rosli, Jun Wei Lim, Fon Yee Han, Worapon Kiatkittipong, Anwar Usman
Publikováno v:
Renewable and Sustainable Energy Reviews. 134:110306
The suspended microalgal cultivation systems targeting the production of lipid for biodiesel is still unable to meet the commercial and economic feasibility due to high energy and cost inputs during the harvesting process. Currently, the attached mic
Publikováno v:
Journal of the Japan Institute of Energy. 96:307-309
Publikováno v:
The Journal of Supercritical Fluids. 157:104704
Microalgae are promising feedstock for the production of biofuel due to their high productivity and low interference with food production for their cultivation and usage. Owing to their aquatic production environment, however, energy-intensive dewate
Publikováno v:
AIP Conference Proceedings.
The effect of heterogeneous catalyst in the supercritical methanol reaction of wet microalgae (64 wt% moisture content), Chlorella vulgaris, was examined in a batch operation system at 385 °C for 60 minutes. The reaction products were separated into
Publikováno v:
AIP Conference Proceedings; 2018, Vol. 2016 Issue 1, p1-4, 4p, 1 Chart, 2 Graphs