Page 94 - Lignocellulosic Biomass to Liquid Biofuels
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70    Lignocellulosic Biomass to Liquid Biofuels


          structure of lignin. Finally, an efficient method of removing hemicellulose
          and lignin has been introduced to make the cellulose accessible to hydro-
          lytic enzyme when then can convert it to monosaccharide [12]. There are
          several limitations of conventional pretreatment methods, such as use of
          irradiation, chemical cost, and high electricity consumption. In compari-
          son to this the use of different ionic liquids as pretreatment medium can
          well dissolve cellulose or lignin in it owing to its cationic and anionic
          structure. Finally, it will remove lignin successfully as well as alter the
          crystalline structure of cellulose [13]. The property of the solvent can be
          determined by the way suitable cation and anion is selected; this process
          transforms it as designer solvent before being implemented in the field of
          green synthesis chemistry for its commendable performances [14]. Mai
          et al. [15] summarized different chemical processes, such as distillation
          (distillation of ionic liquid and distillation of volatile solutes/impurities in
          ionic liquid), induced phase separation (salting out, introduction of CO 2 ,
          and changing the temperature), extraction (solvent extraction and CO 2
          extraction), adsorption (adsorption/desorption and chromatography),
          reverse osmosis, pervaporation, magnetic separation, membrane-based
          processes [nanofiltration (NF), electrodialysis] and centrifugation, to
          recover and recycle ionic liquid so that the ionic liquid-based lignin
          recovery can become an industrially suitable procedure. The main stages
          involved in lignin recovery route are mixing of biomass powder with
          ionic liquid in a specific ratio, stirring and heating at high temperature for
          a certain time period which is then followed by the removal of lignin
          from ionic liquid-based lignin solution by precipitation. Some organic
          antisolvents and recycling of ionic liquid are used after evaporation of
          antisolvent for the recovery of final product. Though lignin can be recov-
          ered from poplar wood biomass by only alkaline pretreatment, with cer-
          tain ionic liquid followed by NaOH, it is possible to gradually increases
          lignin yield [16]. Lignin is also recovered from softwood (pine) as well as
          hardwood (Eucalyptus) dissolved in imidazolium-based acetate and chloride
          ionic liquid. Further categorization of recovered lignin showed 31%
          recovery of lignin [17]. Moghaddam et al. [18] isolated and determined
          physicochemical characteristics of sugarcane bagasse lignin using IL 1-
          butyl-3-methylimidazolium  chloride,  [b mim ]Cl,  and  also  1-butyl-
          3 methylimidazolium methyl sulfonate, [b mim ][CH 3 SO 3 ], with HCl as
          catalyst. The differences in the extraction productivity of organic solvents
          are due to the changes in their conductivity as well as dielectric constant.
          NaOH is used to eliminate lignin from carbohydrate-enriched material as
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