The use of pretreated palm oil mill effluent for acetone–butanol–ethanol fermentation by Clostridium saccharoperbutylacetonicum N1-4

Palm oil mill effluent (POME) was used as an acetone–butanol–ethanol (ABE) fermentation medium using Clostridium saccharoperbutylacetonicum N1-4. Various pretreatment methods were applied on POME to increase the amount of fermentable sugars leading to enhanced ABE production. Sulfuric acid-treated POME (SA-POME) method was found to give the highest yield of total reducing sugars (glucose, cellobiose, xylose, and arabinose) as compared to other pretreatment methods. An increment in the concentration of H2SO4 from 1 to 2% resulted in the enhanced release of reducing sugars (18.3, 26.3 g/L, respectively). However, the treatment of POME with 3% H2SO4, decreased the reducing sugars to 21.6 g/L and consequently, the total ABE production was also reduced. The highest yield of ABE was observed from a culture grown with POME treated by 1% H2SO4. The total ABE production from 1, 2, and 3% SA-POME was obtained as 2.2, 0.45, and 0.41 g/L, respectively. Although, enzymatically treated POME (EH-POME) could produce 4.42 g/L glucose, sulfuric acid treatment (1%) was able to liberate only 1.76 g/L glucose, ABE production was higher when 1% SA-POME was used. Low yield of ABE from enzymatically treated POME can be attributed to the production of some inhibitors during hydrolysis of POME. When EH-POME was treated with XAD-4 resin to nullify the inhibitors, the production of ABE was increased to 4.29 g/L, and ABE yield was also increased to 0.29 g/g. In conclusion, enzymatic hydeolysis of POME followed by elution to XAD-4 column can be proposed as the best pretreatment method for highest productivity of ABE. It was found that addition of P2 medium to the POME hydrolysates was able to improve the production of butanol except in raw POME and sulfuric acid hydrolysates.

[1]  Mohd Sahaid Kalil,et al.  Biobutanol production from rice bran and de-oiled rice bran by Clostridium saccharoperbutylacetonicum N1-4 , 2012, Bioprocess and Biosystems Engineering.

[2]  Bärbel Hahn-Hägerdal,et al.  Fermentation of lignocellulosic hydrolysates. II: inhibitors and mechanisms of inhibition. , 2000 .

[3]  Mu'taz Al-Alawi Biohydrogen Production by Anaerobic Biological Fermentation of Agriculture Waste , 2007 .

[4]  Hubert Bahl,et al.  Parameters Affecting Solvent Production by Clostridium pasteurianum , 1992, Applied and environmental microbiology.

[5]  T. Ezeji,et al.  Butanol production from agricultural residues: Impact of degradation products on Clostridium beijerinckii growth and butanol fermentation , 2007, Biotechnology and bioengineering.

[6]  H. Blaschek,et al.  Regulation and localization of amylolytic enzymes in Clostridium acetobutylicum ATCC 824 , 1990, Applied and environmental microbiology.

[7]  E. Ali,et al.  Bioconversion of Butyric Acid to Butanol by Clostridium saccharoperbutylacetonicum N1-4 (ATCC 13564) in a Limited Nutrient Medium , 2012, BioEnergy Research.

[8]  Jay J. Cheng,et al.  HYDROLYSIS OF LIGNOCELLULOSIC MATERIALS FOR ETHANOL PRODUCTION , 2002 .

[9]  Ye Sun,et al.  Hydrolysis of lignocellulosic materials for ethanol production: a review. , 2002, Bioresource technology.

[10]  Nasib Qureshi,et al.  Removal of fermentation inhibitors from alkaline peroxide pretreated and enzymatically hydrolyzed wheat straw: Production of butanol from hydrolysate using Clostridium beijerinckii in batch reactors , 2008 .

[11]  L. Häggström Acetone-butanol fermentation and its variants. , 1985, Biotechnology advances.

[12]  Jay J. Cheng,et al.  Dilute acid pretreatment of rye straw and bermudagrass for ethanol production. , 2005, Bioresource technology.

[13]  N. Qureshi,et al.  Production of acetone-butanol-ethanol from concentrated substrates using Clostridium acetobutylicum in an integrated fermentation-product removal process , 1995 .

[14]  Siwa Msangi,et al.  Biofuels and the global food balance: bioenergy and agriculture promises and challenges , 2006 .

[15]  Nasib Qureshi,et al.  Butanol production by Clostridium beijerinckii. Part I: use of acid and enzyme hydrolyzed corn fiber. , 2008, Bioresource technology.

[16]  Michael R. Ladisch,et al.  Removal of Fermentation Inhibitors Formed during Pretreatment of Biomass by Polymeric Adsorbents , 2002 .

[17]  D. T. Jones,et al.  Acetone-butanol fermentation revisited. , 1986, Microbiological reviews.

[18]  W. Yusoff,et al.  Direct Fermentation of Palm Oil Mill Effluent to Acetone-butanol-ethanol by Solvent Producing Clostridia , 2003 .

[19]  G. Zacchi,et al.  The generation of fermentation inhibitors during dilute acid hydrolysis of softwood , 1999 .

[20]  L. Nielsen,et al.  Fermentative butanol production by clostridia , 2008, Biotechnology and bioengineering.

[21]  Continuous production of butanol from starch-based packing peanuts. , 2003, Applied biochemistry and biotechnology.

[22]  G. L. Miller Use of Dinitrosalicylic Acid Reagent for Determination of Reducing Sugar , 1959 .

[23]  B. Soni,et al.  Bioconversion of agro-wastes into acetone butanol , 2004, Biotechnology Letters.

[24]  J. Engasser,et al.  The role of acids on the production of acetone and butanol by Clostridium acetobutylicum , 1985, Applied Microbiology and Biotechnology.

[25]  H. Blaschek,et al.  Enhanced Butanol Production by Clostridium beijerinckii BA101 Grown in Semidefined P2 Medium Containing 6 Percent Maltodextrin or Glucose , 1997, Applied and environmental microbiology.

[26]  Genta Kobayashi,et al.  Production of Acetone–Butanol–Ethanol (ABE) in Direct Fermentation of Cassava by Clostridium saccharoperbutylacetonicum N1-4 , 2010, Applied biochemistry and biotechnology.

[27]  Mark W. Rosegrant Bioenergy and the Global Food Balance , 2006 .

[28]  Parameters affecting solvent production by Clostridium acetobutylicum in continuous culture , 1984 .

[29]  P. Dürre Biobutanol: An attractive biofuel , 2007, Biotechnology journal.

[30]  J. Giallo,et al.  Clostridium cellulolyticum sp. nov., a cellulolytic, mesophilic species from decayed grass , 1984 .