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Biomass Valorization


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rel="nofollow" href="#ulink_815ad749-f171-59de-a8da-59c4ac1807e2">[57] MCC Er(OTf)3 240 0.5 4 (LevA) 3 90 (LacA) [104] MCC Ga‐doped Zn/H‐nanozeolite Y 280 1 5 (MLev) — 58 (MLac) 13 (MMP) [105] MCC Zr‐SBA‐15 260 6 2 (ELev) — 30 (ELac) 14 (EHB) [106] Scenedesmus Sn‐beta 210 2 0 — 83 (LacA) [107]

      a) We note that this table shows yields of products either in mol% or in wt%; it is recommended to refer to the given references if the accurate evaluation of yields is sought. “—”, not specified; “0”, not detected, or detected in trace amounts; T, reaction temperature; t, reaction time; MCC, microcrystalline cellulose; OTf, trifluoromethanesulfonate; TsOH, p‐toluenesulfonic acid; 2‐NSA, 2‐naphthalenesulfonic acid; LevA, levulinic acid; ForA, formic acid; MLev, methyl levulinate; ELev, ethyl levulinate; LacA, lactic acid; MLac, methyl lactate; MMP, methyl 2‐methoxypropanoate; ELac, ethyl lactate; and EHB, ethyl‐2‐hydroxybutanoate.

      b) Cellulose treated in the DES ChCl/oxalic acid [103].

      c) Cellulose treated in the DES ChCl/oxalic acid/MIBK [57].

      Finally, we turn now to the valorization of cellulosic biomass into α‐hydroxy acids. The formation of these products occurs via Lewis acid‐catalyzed retro–aldol transformation of cellulose‐derived monosaccharides into C2–C4 sugars and sequential retro‐Michael dehydration into pyruvic aldehyde, rehydration, and isomerization into 2‐hydroxy carboxylic acids catalyzed by both Brønsted and Lewis acids (Scheme 2.2) [3,4,7]. LacA is usually the desired product of such transformations; however, other derivatives may also appear. The conversion of sugars into LacA requires hydrothermal conditions and Lewis acidic catalysts that remain stable in water at elevated temperature. Metal triflates are water‐tolerant Lewis acids and so are suitable catalysts for the task of hydrothermal conversion of cellulose into products [7,21]. In a study of a series of lanthanide triflates, it has been established that yields of LacA increase with a reduction of the ionic radius of the metal center La3+ < Ce3+ < Pr3+ < Nd3+ < Dy3+ < Ho3+ < Er3+ and is approximately equal for Er3+ ≈ Yb3+ ≈ Lu3+ [104]. Among these, Er(OTf)3 was found to be the most active catalyst, providing an outstanding yield of 90 mol% yield of LacA during the reaction of MCC (Table 2.2) [104]. Importantly, the catalyst may be recovered by distillation of the product and be reused in the next cycle.