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320                     Refining Biomass Residues for Sustainable Energy and Bioproducts


         chemical for the production of other chemicals that include resins, polymers, herbi-
         cides, pharmaceuticals, and flavoring agents, solvents, plasticizers, antifreeze
         agents, and biofuels/oxygenated fuel additives can be derived from the LA
         (Rackemann and Doherty, 2011). Based on the previous studies, LA has been pro-
         duce from various biomass either through one-step reaction process (Ya’aini et al.,
         2012; Ramli and Amin, 2014) or two-step reaction involving pretreatment method
         (Wan Omar and Amin, 2016; Chin et al., 2015; Kang and Yu, 2016; Ramli et al.,
         2014b; Jeong et al., 2017; Elumalai et al., 2016; Ma et al., 2016; Pulidindi and
         Kim, 2018; Bevilaqua et al., 2013; Lopes et al., 2017). Previous works were
         reported that the catalytic reaction of the biomass to LA required the existence of
         both Bronsted and Lewis acid to demonstrate efficient polymerization of biomass
         carbohydrate (Tiong et al., 2018; Ramli and Amin, 2015). The catalytic thermal
         reaction also may involve the application of homogeneous (Ramli et al., 2014b;
         Tiong et al., 2017) and heterogeneous (Ya’aini et al., 2012; Ramli and Amin, 2014)
         catalysts.
           The conversion of the lignocellulosic biomass to LA required pretreatment in
         order to remove the lignin barrier that covers the cellulose and hemicellulose
         structure of biomass. The biomass composition and operating conditions could
         give a different effect on the pretreatments process and product (Hendriks and
         Zeeman, 2009). Through the pretreatment process, the biomass complex structure
         should break down efficiently, remove the lignin, and decrystallize the cellulose
         fibers that can decrease the mass transfer limitation of the reaction for high con-
         centration of sugar generation to convert to HMF and subsequently to LA
         (Hendriks and Zeeman, 2009; Morone et al., 2015). Table 14.4 has shown the LA
         production from the pretreated lignocellulosic biomass. There are various pretreat-
         ment methods that have been applied on various biomasses for conversion to LA.
         This includes ball milling (Chin et al., 2015), ozone (Wan Omar and Amin,
         2016), steam explosion (Medina et al., 2016), ionic liquid (Ramlietal.,2014a,b),
         ammonia soaking (Gozan et al., 2018), H 2 SO 4 (Kang and Yu, 2016; Jeong et al.,
         2017), NaOH (Rackemann et al., 2016), andcombinedmethod(Ma et al., 2016;
         Pulidindi and Kim, 2018; Lopes et al., 2017; Schmidt et al., 2017). Ball milling
         pretreatment method provides pretreated biomass for further process such as acid
         hydrolysis to LA. Ball milling can reduce the crystallinity of the cellulose to
         enhance the reaction accessibility of catalysts at cellulose β-1,4-glycosidic bonds
         (Zhao et al., 2006; Avolio et al., 2012). The physical pretreatment of biomass via
         ball milling and steam explosion is presented clean and nontoxic alternative
         method as compared to the chemical treatment via acid and base. Pretreatment or
         one-pot reaction of biomass in ionic liquid becomes one of the suggested methods
         for biomass conversion due to the ability of ionic liquid to depolymerize biomass
         complex structure.
           As for ionic liquid, special chemical properties make it work as dual solvent-
         catalysts for catalytic biomass conversions in one pot such as pretreatment and
         depolymerization (Xu et al., 2016). One-port biomass conversion in ionic liquid
         was conducted as another alternatives to synthesis LA (Tiong et al., 2019; Ramli
         and Amin, 2016). However, the separated pretreated biomass would still give a
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