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. 2019 Jun 11;9(7):264. doi: 10.1007/s13205-019-1788-3

Table 3.

Effect of inorganic salts and their mass fractions on the [C2mim]Cl/water/salt pretreatment and [C2mim]Cl recovery

Inorganic salt Mass fraction (%) Solvent pH Lignin removal (%) Sugar yield (%)a IL recovery (%)
KCl 2 4.31 2.02 (± 0.04) 17.13 (± 0.47)
K2SO4 2 5.36 2.44 (± 0.13) 18.91 (± 1.11)
KH2PO4 2 5.88 2.20 (± 0.06) 19.55 (± 0.54)
K2HPO4 2 9.91 13.94 (± 1.18) 27.96 (± 0.98) 71.25 (± 1.24)
K3PO4 2 13.60 45.76 (± 2.25) 64.33 (± 2.64) 98.14 (± 0.77)
K2CO3 2 12.86 72.38 (± 1.67) 84.99 (± 0.51) 88.53 (± 0.69)
K2CO3 1 12.16 70.49 (± 1.40) 75.17 (± 2.20) 95.95 (± 1.23)
K2CO3 3 12.97 78.94 (± 0.78) 88.67 (± 1.28) 96.28 (± 2.51)
K2CO3 5 13.22 81.45 (± 1.29) 80.32 (± 1.37) 92.67 (± 0.40)
K2CO3 7 13.46 93.70 (± 2.43) 92.07 (± 1.66) 94.32 (± 0.44)
K2CO3 9 13.69 85.39 (± 1.55) 90.61 (± 0.72) 94.54 (± 2.10)

Mass fraction of [C2mim]Cl was 40%, pretreatment temperature was 110 °C, and pretreatment time was 1 h

aEnzymatic hydrolysis time was 72 h