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               the  mixtures  was  increased.  The  biohydrogen  production  yield  obtained  from  the  optimum
               mixing ratio of SLS and POME was 4 times greater than that of individual fermentation of SLS.
               Subsequently, it was further transferred into the BMP test in the second stage.

                       In  the  Fig.  3.1  shows  that  cumulative  hydrogen  production  achieved  from  sole
                                                                        st
                                                                                  nd
               fermentation of POME is dramatically increase from the 1  to the 2  days of fermentation. The
               possible  reasons  is  that  the  microorganisms  can  be  easily  broken  down  the  complex  organic
               contained  in  the  POME  such  as  carbohydrates  to  generate  biohydrogen.  Subsequently,
                                                                                                   th
                                                                                       nd
               cumulative  hydrogen  production  is  gradually  increased  during  the  2   to  the  4   days  of
               fermentation. The possible cause for gradually increased of biohydrogen was generated due to
               the microorganisms are broken down lipid contained in POME was slow, this is due to lipid is a
               large  molecules  which  makes  it  difficult  to  degrade.  At  the  end  of  fermentation,  cumulative
               hydrogen  production  is  dramatically  increased  possibly  correlates  to  reduced  products  which
               expected mostly achieved from lipid hydrolysis was utilized to generate biohydrogen. Similarly
               to co-digestion of SLS and POME with a relatively high proportion of POME in the mixture
               such as SLS: POME mixing ratio of 50:50 %v/v as shown in Fig. 3.1.

                       On the other hand, the lowest cumulative hydrogen production achieved from individual
               fermentation  of  POME  with  initial  organic  concentration  of  21  g-VS added/L  due  to  it  is  a
               concentrated  substrate  with  high  lipid  content  which  could  potentially  inhibit  or  overload  the
               process  and  lead  to  decrease  in  biodegradability.  At  the  same  time,  cumulative  hydrogen
               production achieved from sole fermentation of SLS around 17 times greater than that achieved
               from sole fermentation of POME. The possible reason is that the complex organics contained in
               SLS would be easily broken down as compared with POME. In the Fig. 3.2 shows that when the
               proportion of POME was increased in the mixture, resulting in increase in cumulative hydrogen
               production was obtained. Nevertheless, when the proportion of POME in the mixture was higher
               than 40%, cumulative hydrogen production is gradually decreased as previously mentioned.
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