Page 107 - Lignocellulosic Biomass to Liquid Biofuels
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Bioconversion of lignocellulosic biomass to bioethanol and biobutanol  83


              3.3.2 Traditional downstream purification
              Aqueous ethanol that is produced after conventional fermentation process
              is yet to be accepted as fuel ethanol. Ethanol and water form azeotropic
              mixture and make it difficult to get fuel-grade ethanol. Thus new research
              directs to initiate reducing high-energy demanding and industrially
              acceptable distillation process to break the azeotrope nature for achieving
              almost pure ethanol. Since many years azeotropic and extractive distilla-
              tion processes are used widely for this purpose [183].
                 Distillation is separating liquid mixtures based on their boiling point
              by evaporation followed by condensation. Gill et al. designed the use of
              glycerol in extractive distillation processes to dehydrate ethanol. The rea-
              son is that glycerol has high availability, relatively low cost, and enhanced
              relative volatility, which impart a positive effect on azeotropic mixture.
              The study of the impact of this entrainer on feed stage, feed temperature,
              reflux ratio, feed molar ratio has been done to get the most appropriate
              design for minimizing the requirement of energy [184].
                 A novel approach of extractive dividing-wall columns (DWC), which
              combines with solvent recovery system, and preconcentration column in
              a single distillation unit, is efficient to separate 99.8 wt.% bioethanol. This
              ethanol dehydration configuration can be applied in large-scale bioethanol
              production anywhere in this world [185]. While using ethylene glycol
              and n-pentane as mass separating agent, DWC in extractive and azeotro-
              pic distillation can separate highly pure, that is, 99.8% ethanol, and also
              saves 10% 20% of overall energy [186]. Using ionic liquid as mass sepa-
              rating agent during extractive distillation lowers energy consumption for
              ethanol purification. This process can achieve 0.995 (in mass) ethanol
              purity and 99.9 wt.% ethanol recovery [187].


              3.3.3 Possibilities of application of membrane
              in bioethanol production
              Membrane, a permeable barrier when placed between two mediums and
              applying required driving force, allows the selectively transfer of one or
              more constituent from one phase to another. Membranes that are mostly
              used in bioseparation processes are generally porous in nature. The consti-
              tuents that pass through the pores of the membrane and collected in other
              side are called permeate, whereas the components that retain are called
              retentate. Most useful pressure-driven membrane-based separation com-
              monly used methods include microfiltration (MF), NF, ultrafiltration
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