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               4.2 Introduction



                       Thailand  is  one  of  the  most  agricultural  areas  in  the  Southeast  Asia  which  is  various
               kinds of agricultural crops such as cassava, sugar cane, corn, palm oil and rubber. Among them,
               rubber  is  the  major  agricultural  crops  cultivated  in  Southern  Thailand,  corresponding  with  a
               mostly of located in rubber plant, whereof mostly are provided to produce concentrated latex.
               There  are  several  methods  available  for  concentration  of  natural  latex  is  comprehensive
               creaming, evaporation, electro-decantation and centrifugation. Among them, centrifugation is the
               most method used to  produce concentrated latex in  Southern Thailand. An annual  production
                                                                                                  6
               capacity of concentrated latex obtained from Southern Thailand was around 1.3 x 10  metric ton
                                                                                              3
               which is produced in 2013 (Kongjan et al., 2014). In this process about 580 m  of skim latex
               serum was generated and approximately of 405 ton of concentrated latex was produced. Skim
               latex  serum  is  a  concentrated  with  a  relatively  high  organic  content  in  the  macronutrients  in
               carbon, nitrogen and phosphorus which are the crucial on microbial growing. Thus, skim latex
               serum  generated  cannot  be  discharged  into  environmental  directly,  thank  to  it  could  cause
               seriously environmental pollutions.

                       There are several biological ways to treat this organic waste generated such as aerobic
               and  anaerobic  system.  Among  this  option,  anaerobic  system  is  a  suitable  approach  and  great
               interest since there are several advantages over aerobic system such as higher organic loading
               rate, lower operating cost, gave less excess biomass and produced biogas as a usable product.
               Although skim latex serum contains high nutrients content as previously mentioned, but it’s also
               containing  in  a  relatively  high  inhibitants  content  such  as  ammonia  (latex  preservation)  and
               sulfate (latex coagulation) which is important to microbial growing as well as the efficiency of
               biogas formation. Corresponds with a study from Kongjan et al. (2014) used two-stage anaerobic
               digestion process found that a relatively low of hydrogen and methane production yield achieved
               from sole fermentation of skim latex serum. The hydrogen generated in H 2-UASB reactor was
               59.2±2.4  mL  H 2/g-VS,  while  methane  generated  in  CH 4-UASB  reactor  was  168.6±13.8  mL
               CH 4/g-VS, which is just only 11 and 45% of hydrogen and methane theoretical yield (498 mL
               H 2/g-VS  and  373  mL  CH 4/g-VS).  They  were  reported  the  possible  reason  for  having  low
               hydrogen  formation  because  of  the  competition  of  hydrogen  producing  bacteria  and  sulfate
               reducing  bacteria  to  produce  neither  hydrogen  nor  hydrogen  sulfide.  In  additional,  hydrogen
               sulfide (H 2S) has inhibitory effect on methanogenic archaea at even low concentration of 20-30
               mM (Boe, 2006).

                       Thus, to enhance the biogas production potential from skim latex serum fermentation, the
               approach of anaerobic co-fermentation of organic wastes and two stages process was performed
               in  this  work.  Apart  from  rubber,  palm  oil  is  one  of  the  most  agricultural  crops  cultivated  in
               Southern Thailand. A study from O-Thong et al. (2008) found that high hydrogen production
               yield was achieved from sole fermentation of palm oil mill effluent was 84.2 mL H 2/g-COD and
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