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                       Thesis Title         Hydrogen and Methane Production by Two-stage Anaerobic
                                            Co-digestion of Palm Oil Mill Effluent and Ceratophyllum
                                            demersum
                       Author               Miss Nikannapas Usmanbaha

                       Major Program        Applied Chemistry
                       Academic Year        2015

                                                          ABSTRACT


                                     The aim of this research project was to utilize palm oil mill effluent (POME)
                       co-digesting  with  Ceratophyllum  demersum  for  hydrogen  and  methane  production  by

                       using  the  two-stage  anaerobic  process  in  both  batch  and  continuous  mode.  In  batch
                       cultivation at the initial organic concentration of 10 g-VS/L, various POME: C. demersum
                       mixing  ratios  (VS  Basis)  of  10:0,  9:1,  8:2,  7:3,  6:4,  5:5,  4:6,  3:7,  2:8,  1:9  and  0:10  were

                       investigated under thermophilic (55°C) and mesophilic (35°C) conditions for the first stage
                       and  the  second  stage,  respectively.  Highest  hydrogen  production  yield  of  65.35±3.37
                       mL-H /g-VS added  was obtained from POME: C. demersumratio of 9:1 (VS basis), which is 19%
                           2
                       and  58%  higher  than  that  from  single  fermentation  of  POME  and  C.  demersum,
                       respectively. Subsequent  methane production  yield of  360.7±18.0  mL-CH /g-VS added  was
                                                                                             4
                       achieved from hydrogenogenic effluent from POME: C. demersum ratio of 9:1 (VS basis).
                       The two-stage anaerobic process for continuous hydrogen and methane production was
                       subsequently investigated in the Continuous Stirred Tank Reactor (CSTR) operated under

                       thermophilic (55°C) conditions and Plug Flow Reactor (PFR) operated at ambient condition,
                       respectively.  Specific  hydrogen  yield  of  81±1.2  mL-H /g-VS added  using  10%  of  VS  from
                                                                          2
                       C. demersum concentration in a mixed-substrate was obtained by operating at hydraulic
                       retention  time  (HRT)  of  2  days  and  methane  yield  of 424±4.6  mL-CH /g-VS added  was
                                                                                             4
                       obtained  by  operating  PFR  at  a  hydraulic  retention  time  (HRT)  of  30  days.  Dominant
                       hydrogen-producing bacteria in CSTR were Clostridium sp. and Enterobacter sp. Existance
                       of Weissella sp., Leuconostoc sp. and Lactobacillus sp. could possibly cause lowering
                       hydrogen  production.  Meanwhile,  PFR  broth  was  dominated  with  methanogens  of

                       Methanocorpusculum  sp.,  Methanothrix  sp.  and  Methanoregula  sp.  Hydrogen  and
                       methane yields of 4.13 L-H / L substrate  and 23.15 L-CH /L   satisfactory obtained from
                                                2
                                                                         4 substrate
                       the continuous two-stage anaerobic process could be enable potentially for scale-up this
                       two-stage process to the industrial scale. This research work thus demonstrated a novel

                       and  feasible  approach  for  co-digesting  POME  with  C.  demersumto  generate  valuable
                       gaseous biofuel, mixed hydrogen-methane gas, efficiently.
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