Empty fruit bunch was considered as substrate for second generation of bioethanol because it consists of lignin, cellulose, and hemicelluloses. For lignocelluloses materials, it usually needs pretreatment and hydrolysis to convert cellulose into glucose. Two methods of enzymatic hydrolysis, Separated Hydrolysis and Fermentation (SHF) and Simultaneous Saccharification and Fermentation (SSF) were carried out in this study. The performance of both SHF and SSF was concerned to evaluate the effect of hydrolysis methods and enzyme concentration for producing ethanol. Pretreatment was conducted in a reactor using 10% sodium hydroxide at temperature 150°C during 30 minutes. Two kinds of enzyme, Cellic® CTec2 and Cellic® HTec2 from novozyme were added in 15% (gr/ml) of pretreated EFB at pH 4.8. Four concentration of enzyme Cellic® CTec2, 10, 20, 30, 40 FPU per gram biomass were performed in SHF and SSF processes respectively, while Cellic® HTec2 was added 20% from Cellic® CTec2. Contents of glucose, xylose, and ethanol were recorded every 24 hours. Using 40 FPU of concentration enzyme, it could be produce 4.74% of ethanol in 72 hours fermentation by SHF process and 6.05% of ethanol in 24 hours by SSF process. From this study, the SSF method was considered as a better process than SHF due to rapidly ethanol production and the highest concentration of produced ethanol.

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The transesterification of ethylene carbonate (EC) with methanol to co-generate dimethyl carbonate (DMC) and ethylene glycol over the MgO, CeO 2 and mixed oxide thereof was studied using a fixed-bed isothermal tube reactor. In all mixed oxide, the presence of cerium led to a decrease of BET surface area and pore volume as compared to pure magnesia. X-ray diffraction (XRD) revealed that no mixed phases were observed, but MgO (periclase) and CeO 2 (cerianite) phases. The catalytic activity intensely depends on the surface basicity and the base strength distribution, but not on the surface area and pore volume. It was found that a high EC conversion of 67% with DMC selectivity of 95% could be obtained by catalyst with cerium content around 25 mol%.

Increasing energy demand and concern about increased greenhouse gas emissions make lignocellulosic biomass increasingly to be recognized as having great potential for biofuel and biomaterial production based on the biorefinery concept. Oil Palm Empty Fruit Bunches (EFBs) is one of the major solid wastes in the palm oil industries as a source of lignocellulosic biomass. Cellulose is the highest component of EFBs that can be converted to ethanol. The aim of this research was to investigate the different strategies for high substrate loading on SSF process of bioethanol production from EFBs. Increasing substrate loading is one of the most important challenges to make bioethanol production more economical. This research used two methods to increase the substrate concentration loading on Simultaneous Saccharification and Fermentation (SSF) i.e: direct variation of substrate concentration loading and substrate loading gradually to obtain a high-concentration substrate. A range of substrate loading was from 15% to 25% (g.mL -1 ). The SSF process was carried out at 32 o C, pH 4.8, and 150 rpm for 72 hours. The result shows that the highest concentration of ethanol can be produced by a high concentration of substrate loading gradually. The highest ethanol concentration was 83.40 g.L -1 (80.21% ethanol yield) by using 25% (g.mL -1 )substrate loading gradually, 18 FPU/g substrate enzyme Cellic® Ctec2 and 20% Cellic® Htec2 (based on volume of Cellic® Ctec2), and 1% (g.mL -1 ) yeast Saccharomyces cereviceae in SSF process. Whereas, 20% (g.mL -1 ) concentration substrate loading by directly or gradually produce almost same ethanol concentration.