Selection of Biorefinery Routes: The Case of Xylitol and its Integration with an Organosolv Process

Abstract

Lignocellulosic biomass includes agricultural and forest residues, which is a promising source for energy and chemical production when valorized through the biorefinery process. Xylitol is an important co-product in biorefinery. The production of xylitol is achieved either by yeast fermentation or by catalytic hydrogenation of xylose. However these approaches are not viable unless integrated. This paper presents a comparative analysis and the integrating opportunities of two processes for the production of xylitol, assessing the scope for individual integration as well as integration with upstream and parallel processes. The two processes examined are the fermentation of xylose by Candida yeasts (productivity 0.73 kg xylitol crystals/kg xylose), and the catalytic hydrogenation of xylose using a Raney Nickel catalyst (productivity 0.85 kg xylitol crystals/ kg xylose). The heat integration analysis resulted in conservation of 90% for cooling and 18% for heating requirements in the catalytic process. The corresponding results in the biotechnological process were 94 and 65% respectively. The economic evaluation estimated higher total investment and raw materials-utilities cost for the biotechnological process in comparison to the catalytic by 391 and 8% respectively. The economic indexes characterize the catalytic process investment as more secure and profitable.

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Abbreviations

C5:

Pentoses (five carbon sugars)

C6:

Hexoses (six carbon sugars)

CEPCI:

Chemical engineering plant cost index

CIMV:

Compagnie Industrielle de la Matière Végétale (tr. industrial company of vegetative material)

cr:

Crystallized

GCC:

Grand composite curves

LHV:

Lower heating value

MILP:

Mixed integer linear programming

MINLP:

Mixed integer non linear programming

MM:

Million

NPV:

Net present value

PBP:

Payback period

USD:

United states dollar

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Acknowledgements

Financial support from the Consortium of Marie Curie project RENESENG (FP7-607415) is gratefully acknowledged. The authors would also like to thank Marilyn Wiebe and all the people working for the BIOCORE Project (FP7-241566), for their collaboration and excellent communication.

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Correspondence to A. D. Mountraki.

Appendix

Appendix

See Tables 12, 13, 14, 15, 16, 17 and 18.

Table 12 Shortcut calculations
Table 13 Cost estimation of the heat exchangers in the catalytic process
Table 14 Total equipment cost estimation of the catalytic process
Table 15 Cost estimation of the heat exchangers in the biochemical process
Table 16 Total equipment cost estimation of the biochemical process
Table 17 Raw materials and utilities cost
Table 18 Calculation of the total fixed investment

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Mountraki, A.D., Koutsospyros, K.R., Mlayah, B.B. et al. Selection of Biorefinery Routes: The Case of Xylitol and its Integration with an Organosolv Process. Waste Biomass Valor 8, 2283–2300 (2017). https://doi.org/10.1007/s12649-016-9814-8

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Keywords

  • Xylitol
  • Process design
  • Cost estimation
  • Integration
  • Biorefinery