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                                                    LIST OF TABLES

                                                                                                        Page

               Table 2.1 Physical and chemical characteristics of skim latex serum                        8

               Table 2.2 Physical and chemical characteristics of palm oil mill effluent                  9

               Table 2.3 Hydrogen and methane production from anaerobic digestion                         10

                         of POME under mesophilic and thermophilic conditions

               Table 3.1 Physical and chemical characteristics of skim latex serum and                    29

                         palm oil mill effluent

               Table 3.2 Experimental variables and concentration levels investigated by using central    26
                         composite design
               Table 3.3 Central composite experimental design matrix defining NaHCO 3,                   27

                         Na 2HPO 4.12H 2O and EFB ash concentrations on hydrogen production yield

               Table 3.4 Analysis of variance (ANOVA) for the regression model                            35
               Table 3.5 Model coefficients estimated by multiples linear regression                      35

                         (significance of regression coefficients), where X 1 =NaHCO 3 concentration  (g/L),

                         X 2 =Na 2HPO 4.12H 2O concentration (mg/L) and X 3 = EFB ash concentration (g/L)

               Table 3.6 pH and results on hydrogen production yield achieved from buffer and macro-      36

                         nutrient optimization stage.

               Table 3.7 Soluble metabolites obtained from different mixing ratio of SLS to POME          39

                         with initial organic loading of 7 g-VS added/L

               Table 3.8 Soluble metabolites obtained from different mixing ratio of SLS to POME          41

                         with initial organic loading of 21 g-VS added/L

               Table 3.9 Soluble metabolite products and COD balance obtained from different              43

                          mixing ratio of SLS to POME with initial organic loading of 7 g-VS added/L

                         at the end of fermentation

               Table 3.10 Soluble metabolite products achieved from methane production in                 45

                         batch experiment
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