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Pretreatment of lignocellulosic biomass for efficient enzymatic saccharification of cellulose  37


              including a partial reduction of esterified acetic acid, ferulic acid, and p-
              coumaric acids as well as a significant cleavage of etherified linkages
              between lignin and hemicelluloses [114]. In fact, almost no significant
              changes in the chemical structure of hemicelluloses might be observed,
              because the oxidation reaction only occurs in the aliphatic part of the
              macromolecule [115].
                 Alkaline peroxide pretreatment has been applied to various biomass
              feedstock including wheat straw [116], softwood [117], sugarcane bagasse
              [118], bamboo [119], corn stover [120], Miscanthus [121], and other her-
              baceous and woody biomass [122]. After alkaline peroxide pretreatment,
              the pretreated wheat straw presents 96.7% enzymatic hydrolysis yield.
              During the pretreatment, no measurable quantities of furfural and HMF
              are produced. The ethanol yield could be 0.46 g/g of available sugars
              (0.29 g/g straw) [123]. Recently, the alkaline peroxide pretreatment at
              low peroxide loadings has been used to enhance the enzymatic hydrolysis
              of softwood [117]. It was found that the presence of H 2 O 2 is essential for
              this pretreatment. In order to achieve a better substrate hydrolyzability, it
              is more effective to maintain a higher alkaline loading than increasing the
              H 2 O 2 loadings. When Douglas-fir was pretreated at 180°C for 30 min
              with a low peroxide loading of 0.10 (mass fraction of H 2 O 2 to biomass), a
              cellulose to glucose yield of 95% could be achieved [117]. The key factor
              is the balance between alkaline and peroxide loadings during the
              pretreatment.

              2.3.4.3 Peracid oxidation
              As powerful oxidants, peracids, such as peroxymonosulfuric acid, peroxy-
              formic acid, and peracetic acid (PAA), also have been used for biomass
              delignification and pretreatment [68]. Among the peracids used, PAA is
              the most promising because it is more stable than performic acid [124]
              and easier to recover and prepare than peroxymonosulfuric acid [125].
              PAA has been found to be very selective to oxidize lignin. It oxidizes the
              hydroxyl groups in lignin side chains to carbonyl groups [126] and cleaves
              β-aryl ether bonds, resulting in the decrease of lignin molecular weight
              and introduction of hydrophilic groups [127]. In addition, PAA oxidation
              increases the water solubility of lignin via several reactions: formation of
              hydroquinones by phenolic rings hydroxylation [128], oxidation of
              hydroquinones to quinones which undergo ring opening to produce
              water-soluble muconic, maleic, and fumaric acid derivatives [129]. The
              main reaction types of PAA with lignin-related structures using lignin
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