4.6 Article

Integrated Renewable Production of Sorbitol and Xylitol from Switchgrass

Journal

INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH
Volume 60, Issue 15, Pages 5558-5573

Publisher

AMER CHEMICAL SOC
DOI: 10.1021/acs.iecr.1c00397

Keywords

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Funding

  1. European Union's Horizon 2020 research and innovation programme under the Marie Sklodowska-Curie grant [778168]
  2. CADP center at CMU
  3. Spanish MCI

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This study focuses on designing integrated facilities for the production of xylitol and sorbitol from lignocellulosic biomass. Various pretreatments, hydrolysis, fermentation, and catalytic hydrogenation are considered to process different biomass feedstocks into the desired products. An economically optimized system with 3 crystallizers is selected to improve production efficiency and reduce costs for xylitol and sorbitol.
This work deals with the design of integrated facilities for the production of xylitol and sorbitol from lignocellulosic biomass. Xylitol can be obtained from xylose via fermentation or catalytic hydrogenation. Sorbitol is obtained from glucose, but preferably from fructose, and also via fermentation or catalytic hydrogenation. Fructose can be obtained from glucose via isomerization. Thus, a superstructure of alternatives is formulated to process switchgrass, corn stover, miscanthus, and other agricultural and forestry residues. Different pretreatments, such as dilute acid or ammonia fiber explosion (AFEX), for the fractionation of the biomass are evaluated. Next, after hydrolysis, the C5 and C6 sugars are processed separately for which a catalytic or a fermentation stage are considered. Glucose has to be isomerized before it can be processed. Finally, crystallization in a multistage evaporator system is used for purification. The optimization of the system is done by the use of dilute acid and the catalytic system. A system of 3 crystallizers is selected. For a facility that produces 145 kt/yr of xylitol and 157.6 kt/yr of sorbitol, the investment adds up to 120.74 M(sic) for a production cost of 0.28 (sic)/kg products. The inverse engineering of biomass was also performed resulting in a composition of 15% water, 20% cellulose, 40% hemicellulose, 15% lignin, and 5% ash. The closest biomass corresponds to Sargassum (brown algae), which is capable of producing 230.5 kt/yr of xylitol and 116 kt/yr of sorbitol with investment and production costs of 120.5 M(sic) and 0.25 (sic)/kg products, respectively.

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