Page 108 - Lignocellulosic Biomass to Liquid Biofuels
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84    Lignocellulosic Biomass to Liquid Biofuels


          (UF), and reverse osmosis. Most of the membrane that is used in different
          chemical processes is made polymer. But nowadays, the use of inorganic
          and hybrid membrane is common comprising inorganic nanoparticle and
          also polymer. The commonly used membrane configurations are hollow-
          fiber module that is currently being used vastly. In bioethanol industry,
          membrane is generally used for downstream purification to concentrate
          the final product. But it can be sufficiently used in cellulase enzyme recy-
          cling, cell recycling, and removal of inhibitory by-products as well.


          3.3.3.1 Membrane-assisted enzymatic hydrolysis
          Fermentation of lignocellulosic biomass to fuel-grade ethanol challenges
          two major difficulties: (1) crystalline structure of cellulose which resists
          enzymatic hydrolysis of cellulose and (2) lignin-cellulose association that
          impedes enzymatic attack on cellulose [188]. Dilute acid catalyzed
          hydrolysis of cellulose uses high pressure and temperature that leads to the
          destruction of monomer glucose to hydroxymethylfurfural (HMF), FA,
          levulinic acid (LA), including side reaction that cause disruption of cellu-
          lose leading to the formation of nonreactive material [189]. On the other
          hand, this chemical process, enzymatic hydrolysis of cellulose, requires
          relatively low energy as well as normal temperature and pressure.
          Cellulolytic enzyme containing CBHs, EG and BGL obtained from dif-
          ferent bacteria or fungi can sufficiently hydrolyze pretreated lignocellulosic
          biomass to fermentable sugar. But the cost of the enzyme constitutes 20%
          of the total ethanol production cost and 50% of the total cost of whole
          hydrolysis process [190].
             One way to reduce the manufacture cost of ethanol from lignocellu-
          losic biomass is to recycle and reuse of enzyme as well as the specific
          activity of enzyme should be recovered, retained. Enzyme recycling is
          predisposed by various reasons such as nature of biomass, process para-
          meters and origin, and activity of enzyme [191]. After hydrolysis, cellulase
          can either appear in solution as free enzyme or can be adsorbed in
          remaining biomass [192]. Recovery and recycling of bound enzyme after
          initial hydrolysis require separation and desorption method [193], but the
          catalytic activity gradually decreases during hydrolysis steps.
             Recovery of filter paper actions decreases from 91% to 22% by this
          method. But the use of alkali or surfactant increases enzyme activity to
          some point. Membrane-based process somehow adequately recovers the
          enzyme from hydrolysis solution, retains its catalytic activity, satisfactorily
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