Page 79 - Lignocellulosic Biomass to Liquid Biofuels
P. 79

is    to
                       sugars  pressure  usually  and  explosion  and  The  single-  the  in  high

                       of  High  is  biomass  satisfying  so  CO 2  biomass  recovery  formed  well  increased.  the  exit  also  alkaline
                       decomposition  inhibitors.  explosion  Steam  grass  not  but  biomass.  dry  to  chemical  sulfur-containing  the  if  not  is  is complexity  in encountered  pretreatment  and  acid  Relatively  costs




               Disadvantages  Significant  form  to  needed.  for effective  hardwood,  softwood  effective  not  is  of  cost  High  of  effluent  wastewater  lignosulfonate  recovered  Process  issues  stage  subsequent  pretreatment.  operation







                              size                               hexose  single
                          low   impact            other  Low  of        well
                       cellulose  relatively  consumption,  particle  big  woody  to  of formation  with  pretreatments.  digestibility.  adsorption  lignin  on  both  for  with  pretreatment.  is  enzymes



                       improve  with  energy  for  suitable  environmental  effective  Less  compared  cellulose  enzyme  recovery  compared  alkaline  digestibility  less  with


               Advantages  to Efficient  digestibility  low  cost,  being  low  and  Particularly  biomass.  inhibitors  thermochemical  High  nonproductive  cellulase  sugar  High  pentose  and  or  acid  Cellulose  enhanced  required





                       high-  duration   (for     of    make

               to      with   is  explosive  cell  and  chips  a  with  part  with  to  wall  accessibility  respectively
               mechanisms  digestibility  heated  or  steam  short  a  for  pressure  causing  deconstruct  significant  structure  lignin  wood  reduction  considerable  removed  Lignin  modified  Cell  deconstructed  cellulose  alkaline  and  remove  lignin




               and     are  saturated  CO 2 the  then  to  with  hemicelluloses  of  soften  size  A  is  delignification.  greatly  hydrophilic.  greatly  in  acid  of  to  and  process
               action  cellulose  substrates  and  reduced  decompression  structure  of  explosion)  to  sulfite  by  milling.  hemicelluloses  is  is  increase  hemicelluloses  multistage

               of         pressure  supercritical  time  swiftly  removal  modification  stem  followed  partial  structure  more  structure  with  Combination  pretreatment  a
               Mode  improve  Biomass  of  wall  Using  disk  it        in

           (Continued)  pretreatment  CO 2  etc.)                acid




           2.2  Pretreatment  Physicochemical  pretreatment  (steam  explosion,  explosion,  Subsequent  alkaline  pretreatment
           Table  methods  Combined          SPROL                 and
   74   75   76   77   78   79   80   81   82   83   84