Page 50 - Lignocellulosic Biomass to Liquid Biofuels
P. 50

Pretreatment of lignocellulosic biomass for efficient enzymatic saccharification of cellulose  29


              nitric acid have been used for dilute acid pretreatment, while sulfuric acid
              is studied the most because it is highly effective and inexpensive [55].
              Phosphoric acid has also been widely used since it is relatively cheap and
              can hydrolyze biomass efficiently. Moreover, using NaOH or ammonia to
              neutralize the phosphoric acid, hydrolyzate produces sodium or ammonia
              phosphate, which could be used as a nutrient for microorganisms in fer-
              mentation step [56].
                 For dilute acid pretreatment of rice straw, a maximal sugar yield of
              83% could be achieved by 1% (w/w) sulfuric acid for a reaction time of
              1 5 min at 160°C or 180°C, followed by enzymatic hydrolysis [57].
              Pretreatment of olive tree with 1.4% sulfuric acid at 210°C resulted in a
              maximum enzymatic hydrolysis yield (76.5%), while the maximum sugar
              yield (36.3 g sugar/100 g raw material) was achieved with 1% sulfuric acid
              at 180°C, representing 75% of all sugars in the raw material [58].
              Compared to dilute sulfuric acid pretreatment of rye straw, dilute nitric
              acid pretreatment was found to give higher glucose concentration [59].
              Nevertheless, it is difficult to remove the by-products from nitric acid pre-
              treatment by washing the pretreated substrates [60]. The applications of
              diluted phosphoric acid for corn stover achieved 85% glucose yield with
              0.5% (v/v) H 3 PO 4 and 10% solid loading at 180°C for 15 min [61].
                 Although dilute acid pretreatment presents the advantage of solubiliz-
              ing hemicelluloses, the acid must be neutralized for the downstream
              enzymatic hydrolysis or fermentation processes. In addition, the formation
              of some sugar degradation compounds, for example, furfural and HMF,
              inhibits the microorganism metabolism [62]. Corrosion caused by dilute
              acid pretreatment also mandates expensive construction material.

              2.3.2.2 Acid catalyzed organosolv pretreatment
              Organosolv pretreatment refers to the biomass pretreatment process with
              organic solvents with or without the addition of catalyst. When no exter-
              nal catalyst is used, organosolv pretreatment usually requires high organic
              solvent concentration ($60%) and high pretreatment temperature
              (160°C 220°C) [63], which is also termed auto-catalyzed organosolv pre-
              treatment. In this process the formed organic acid, such as acetic acid, can
              play as a catalyst. However, to promote the pretreatment efficiency, exter-
              nal catalysts, such as mineral or strong organic acids, are usually used.
              Acid-catalyzed organosolv pretreatment is a composite process involving
              lignin and hemicellulose degradation, solvation, and solubilization of lig-
              nin fragments. The supplementary of acid catalyst could increase the
   45   46   47   48   49   50   51   52   53   54   55