Extractive Fermentation With Surfactant To Enchance Butanol Production
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newline Abstract
newlineExtractive butanol fermentation with non-ionic surfactant, a recently explored area, has shown
newlinepromising results with several advantages but is relatively less investigated. Non-ionic
newlinesurfactants (L62 and L62D) were selected for the extractive fermentation to enhance butanol
newlineproduction using butanol producing strain Clostridium beijerinckii MCMB 581 and
newlineClostridium sporogenes. Biocompatibility studies with both the surfactants showed bacterial
newlinegrowth. Higher concentrations of surfactant (gt5%) affected the cell count. Effect of mixing
newlinewas studied and it was found that mixing does not improve butanol production. Further, the
newlinestudy was undertaken in order to investigate effect of diverse parameters such as fermentation
newlinemedia, pH, initial concentration of biomass and various substrate on increasing butanol and
newlinetotal solvent production. Cheng s fermentation media was successfully tested and perceived
newlineto increase final solvents concentration. Controlled pH at 12th and 24th hours had negative
newlineeffect on butanol enhancement; however, it resulted in more butyric acid production which
newlineremained accumulated. Ten percent (v/v) biomass was evaluated to increase final solvents
newlineconcentration and hence butanol yield compared to 20% and 30% (v/v) of initial biomass
newlineconcentrations. Glucose was found to be the best substrate among the studied substrates. Effect
newlineof surfactant concentration (3 20%) was studied on butanol production and it was found that
newline6% (v/v) L62 resulted in 49% higher final butanol concentration compared to control. Effect
newlineof different concentrations of glucose was also studied, 60 g/L was found to be best for butanol
newlinefermentation. Earlier studies had shown improved butanol production with non-ionic
newlinesurfactant and immobilized cells independently. Thus, combined effect of extractive
newlinefermentation and immobilized cells on butanol production was studied. Different matrices
newline(brick, bamboo, cotton fiber, flannel cloth, and polyurethane foam) were tested for
newlinesimultaneous immobilization and extractive fermentation. Immobilized biomass was used in
newlinean extractive fermentation study with non-ionic surfactantL62. Biomass immobilized on
newlinepolyurethane foam (PF) doubled the butanol production in presence of 6% (v/v) L62 with
newlinerespect to control (free cells without surfactant). Immobilized cells on PF were successfully
newlinereused for 4 cycles.
newlineFurther work investigates microemulsion based butanol extraction from simulated and
newlinemicrobial fermentation broth. Alkanes C5-C7 (pentane, hexane and heptane) were used for
newlineextraction of butanol from fermentation broth using microemulsion technique. Conditions for
newlineii
newlineWinsor microemulsion with C5, C6 and C7 alkanes were established. Hexane and heptane
newlineformed Winsor-III microemulsion at 45-50°C. Hexane based microemulsion resulted into
newlineorganic phase (Om) containing more butanol (62% w/w) than pentane (12.4% w/w) and
newlineheptane (57.3% w/w). Bi-continuous phase (i.e. the surfactant phase or BC) had negligible
newlineamount of butanol. Surfactant was retained in bi-continuous and water phase (Wm). Thus,
newlinehexane was found to be a better microemulsion extractant than other two alkanes. Studies with
newlinetwo step approach i.e. coacervation followed by back-extraction resulted in less extraction
newlineefficiency of butanol. However, the single stage approach with hexane not only reduced a step
newlinebut also yielded into 4 times more extraction than two stage approach.
newlineKeywords: Butanol, ABE, Non-ionic surfactant, Extractive fermentation, Immobilization,