In this study, co-gasification of palm kernel shell (PKS) and low-rank Malaysian coal (MB) was carried out in a fixed bed reactor. For the pretreated samples, PKS was torrefied at 270C (PKSTo) and MB was preheated at 250C (MBPr) for 1 h, respectively, prior to co-gasification at 767C, with a biomass blending ratio of 52% and a steam flow rate of 55 mL/min. The effect of different blending combinations was investigated towards product yields, namely gas, tar, char and gases composition. The co-gasification on both pretreated (PKSTo/MBPr) and catalyst-pretreated (Cat-PKSTo/MBPr) produced a greater gas yield, with lesser tar and char yield than both untreated PKS and MB (PKSUn/MBUn) and pretreated PKS and untreated MB (PKSTo/MBUn). The PKSTo/MBPr was found to enhance the H2 production by 63.9% and 41% than PKSUn/MBUn and PKSTo/MBUn, respectively, at 45 min of reaction time. Thus, the pretreatment on both samples had a significant impact on the distribution and composition of product yields during co-gasification. As a conclusion, the pretreated sample, which has been upgraded on characteristics such as higher carbon and lower oxygen content than the untreated sample was revealed to enhance gas yield and H2 production during co-gasification.

Abstract. In-situ supercritical methanol transesterification for production of biodiesel from Jatropha curcas L. (JCL) seeds was successfully being carried out via batch-wise reactor system, under varying temperatures of 180 -300 °C, pressures of 6 -18 MPa, reaction time of 5 -35 min and seeds-to-methanol ratio of 1:15 -1:45 (w/v). In this study, the extracted oil obtained showed the presence of FAME referring as biodiesel, indicating that transesterification reaction had occurred during the extraction process. The results showed that the biodiesel yield was obtained at optimum conditions of 280 °C, 12 MPa, 30 min and 1:40 (w/v) were 97.9%.

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