Page 354 - Refining Biomass Residues for Sustainable Energy and Bioproducts
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(2018)  (2018)  (2018)  (2018)  (2016)
                     Amin  (2016)  (2016)  (2015)  (2016)  (2016)  (2016)  (2016)  (2013)  (2017)
                   (2015)  and  al.  (2014b)  (2018)  Yu  (2014b)  al.  (2014a)  (2017)  (2018)  al.  al.  al.  al.  (2016)  Kim  Kim  Kim  Kim  al.  (2017)  al.  al.  et

                   al.  Omar  et  al.  et  al.  et  and  al.  et  et  al.  et  al.  al.  et  et  et  et  al.  and  and  and  and  et  al.  et  et
                   et  (2016)          et  et  Elumalai  Elumalai  Elumalai  Elumalai  et  Pulidindi  Pulidindi  Pulidindi  Pulidindi  Bevilaqua  Rackemann
            Ref.   Chin  Wan  Medina  Ramli  Gozan  Kang  Ramli  Noparat  Ramli  Jeong  Jeong  Ma  Lopes  Schmidt


            (%)
            yield  (21.5)  0.11 g/L b                                   B75.0 c,e (19.0)
            LA     53.9 a  14.3  31.6  52.1 c  25.8  39.5  2.53 b  25.3  16.5  4.6 d  21.0  8.0  13.0  13.0  25.2  50.4 c  56.0 c  53.3 c  53.6 c  59.4  55.0 a  53.1 c,e

               (h)
               Time  3.27  1.0  0.17  0.74  1.5  5.0  0.74  0.67  3.0  0.17  3.0  2.0  2.0  2.0  2.0  0.25  5.0  5.0  5.0  5.0  1.0  1.25  0.75  0.67


               (   C)
            production  Temp.  186.0  180.0  195.0  165.5  170.0  170.0  165.5  180.0  170.0  200.0  190.0  180.0  180.0  180.0  180.0  200.0  150.0  150.0  150.0  150.0  170.0  170.0  180.0  180.0



            LA
            on
        biomass.  condition          zeolite  NaOH-zeolite  H 2 SO 4 1 p-hydroxyanisole


        lignocellulosic  Reaction  Catalyst  H 2 SO 4  H 2 SO 4     H 2 SO 4  H 2 SO 4  H 2 SO 4  H 2 SO 4     Fe/HY  H 2 SO 4  (aq.)  HCl  (aq.)  HCl  (aq.)  HCl  (aq.)  HCl  HCl  HCl  HCl  HCl  HCl  H 2 SO 4  MSA  MSA





        pretreated  Solvent  H 2 O  H 2 O     H 2 O  H 2 O  H 2 O  H 2 O     H 2 O  H 2 O  H 2 O  DMSO-THF  DMSO-THF  DMSO-THF  DMSO-THF  H 2 O  H 2 O  H 2 O  H 2 O  H 2 O  H 2 O  H 2 O  H 2 O  H 2 O



        from                 (aq.)                                extraction EFB, Empty fruit bunch; MSA, methanesulfonic acid; OPF, oil palm frond; OPMF, oil palm mesocarp fiber; OPT, oil palm trunk.
        production  step  explosion  ammonia  H 2 SO 4  explosion enzymatic  aqueous



        (LA)  Pretreatment  milling  Ozone  Steam  [EMIM][Cl]  in  Soaking  (aq.)  H 2 SO 4  [EMIM][Cl]  Diluted  [BMIM][Br]  (aq.)  H 2 SO 4  (aq.)  H 2 SO 4  Thermo-H 2 SO 4  Thermo-NaOH  Thermo-NaCIO 2  Thermo-NaCIO  Steam  Na 2 CO 3 1 Na 2 S  Na 2 CO 3 1 Na 2 S  Na 2 CO 3 1 Na 2 S  Na 2 CO 3 1 Na 2 S  Soxhlet  H 2 SO 4 1 NaOH  Thermal-enz

        acid       Ball                                                     a Calculated based on cellulose percentage of biomass feedstock.
        Levulinic  feedstocks  wood                                 bagasse  bagasse  bagasse  c Calculated based on C6/C5 sugar concentration.



        14.4                               straw  straw  straw  straw  straw  straw  stover  sorghum  bagasse  husk  b Product from pretreatment process. d LA from biomass hydrolysate. e Product in mol.%.
        Table  Biomass  EFB  EFB  EFB  EFB  EFB  Eucalyptus  Kenaf  OPT  OPF  Oak  Oak  Rice  Rice  Rice  Rice  Rice  Rice  Corn  Miscanthus  Sweet  Rice  Sugarcane  Sugarcane  Sugarcane
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