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               lactic acid was still found as the major soluble metabolite products of all operational conditions.
               Which  is  consistent  with  our  previous  research  in  batch  assay  that  used  the  enriched  and
               acclimated hydrogen producing bacteria obtained from H 2-CSTR reactor was operated under the
               volumetric mixing ratio of SLS to POME at 1:1 under HRT of 4.50 days. The result shows that
               lactic  acid  was  the  main  soluble  metabolite  products  in  a  relatively  high  concentration  of  all
               treatment. Reactions (4.1) and (4.2) shows metabolic pathway produced lactic acid by lactic acid
               bacteria  (LAB),  which  distinguished  between  homofermentative  LAB  (Reaction  4.1)  and
               heterofermentative LAB (Reaction 4.2) (Mariakakis et al., 2011). Although lactic acid could be
               transformed to acetic, propionic (Reaction 4.3) and butyric acids (Reaction 4.4) by Clostridium
               propionicum  and  Clostridium  tyrobutyricum  to  generates  hydrogen  (Noike  et  al.,  2002).
               Nevertheless, hydrogen could be generated by secondary fermentation (Reactions 4.3 and 4.4)
               which provides the biological reaction rate slower than that generated by primary reaction rate.
               Moreover, a study from Noike et al. (2002) found that the hydrogen production yield gradually
               decreased and ceased since high concentration of lactic acid was detected.

                                                         C 6H 12O 6                2 CH 3CH(OH)COOH                                         (4.1)

                                                         C 6H 12O 6               CH 3CH(OH)COOH + CH 3COOH + CO 2           (4.2)

                          3 CH 3CH(OH)COOH             2 CH 3CH 2COOH + CH 3COOH + CO 2 + H 2O                (4.3)


               CH 3CH(OH)COOH + 0.4 CH 3COOH       0.7 CH 3(CH 2) 2COOH + CO 2 + 0.4 H 2O + 0.6 H 2  (4.4)



                       Furthermore, the other possible reason for still lower of hydrogen was generated of all
               operational condition is that the growing of sulfate reducing bacteria in the H 2-CSTR reactor
               which could potentially consume hydrogen generated (Reactions 4.5 and 4.6) (Schink, 1997).

                                                2-
                                                                2-
                                                     4H 2 + SO 4                      S  + 4H 2O                                                    (4.5)
                                               0
                                                         H 2 + S                            H 2S                                                            (4.6)
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