Abstract
Hydrothermal processing is an interesting technology for the conversion of lignocellulosic biomass in biofuels and compounds in terms of a biorefinery. This process is based on the selective solubilization and depolymerization of hemicellulose fraction (xylan), producing a liquid phase of hemicellulose rich in oligomers (xylooligosaccharides), monosaccharides (mainly xylose), and degradation compounds (furfural and formic acid). Therefore, this chapter presents an overview of mathematical modeling based on pseudo-first-order kinetics and the operating conditions as temperature and time (“severity factor”) during the hydrothermal processing in order to predict the conversion and the produced compounds with high value-added in terms of biorefinery.
Access this chapter
Tax calculation will be finalised at checkout
Purchases are for personal use only
References
Aguedo M, Ruiz HA, Richel A (2015) Non-alkaline solubilization of arabinoxylans from destarched wheat bran using hydrothermal microwave processing and comparison with the hydrolysis by an endoxylanase. Chem Eng Process Process Intensif 96:72–82
Aguilar-Reynosa A, Romaní A, Rodríguez-Jasso RM, Aguilar CN, Garrote G, Ruiz HA (2017) Microwave heating processing as alternative of pretreatment in second-generation biorefinery: an overview. Energ Conver Manage 136:50–65
Archambault-Leger V, Shao X, Lynd LR (2012) Integrated analysis of hydrothermal flow through pretreatment. Biotechnol Biofuels 5:49
Bajpai P (2013) Products from hemicellulose. In: Bajpai P (ed) Biorefinery in the pulp and paper industry. Academic Press, Elsevier, London, UK, pp 65–98
Bobleter O, Bonn G (1983) The hydrothermolysis of cellobiose and its reaction-product D-glucose. Carbohydr Res 23:185–193
Brennan MA, Wyman CE (2004) Initial evaluation of simple mass transfer models to describe hemicellulose hydrolysis in corn stover. Appl Biochem Biotechnol 113/116:965–976
Bruggeman JP, Bettinger CJ, Langer R (2010) Biodegradable xylitol-based elastomers: in vivo behavior and biocompatibility. J Biomed Mater Res A 95:92–104
Carvalheiro F, Garrote G, Parajó JC, Pereira H, Gírio FM (2005) Kinetic modeling of brewery’s spent grain autohydrolysis. Biotechnol Prog 21:233–243
Carvalho AFA, de Oliva NP, Da Silva DF, Pastore GM (2013) Xylo-oligosaccharides from lignocellulosic materials: chemical structure, health benefits and production by chemical and enzymatic hydrolysis. Food Res Int 51:75–85
Chapla D, Pandit P, Shah A (2012) Production of xylooligosaccharides from corncob xylan by fungal xylanase and their utilization by probiotics. Bioresour Technol 115:215–221
Chornet E, Overend RP (1991) Phenomenological kinetics and reaction engineering aspects of steam/aqueous treatments. In: Focher B, Marzetti A (eds) Steam explosion techniques. Fundamentals and industrial applications. Gordon and Breach Science, Philadelphia, pp 21–58
Christopher L (2012) Adding value prior to pulping: bioproducts from hemicellulose. In: Okia CA (ed) Global perspectives on sustainable forest management. InTech. Doi: 10.5772/36849
Dekker RFH, Wallis AFA (1983) Autohydrolysis-explosion as pretreatment for the enzymic saccharification of sunflower seed hulls. Biotechnol Lett 5:311–316
Edlund U, Ryberg YZ, Albertsson AC (2010) Barrier films from renewable forestry waste. Biomacromolecules 11:2532–2538
Fang H, Deng J, Zhang X (2011) Continuous steam explosion of wheat straw by high pressure mechanical refining system to produce sugars for bioconversion. Bioresources 6:4468–4480
Fogler HS (1999) Elements of chemical reaction engineering, 3rd edn. Prentice Hall, Upper Saddle River, pp 68–123
Garrote G, Domínguez H, Parajó JC (1999a) Hydrothermal processing of lignocellulosic materials. HolzRohWerkst 57:191–202
Garrote G, Domínguez H, Parajó JC (1999b) Mild autohydrolysis: an environmentally friendly technology for xylooligosaccharides production from wood. J Chem Technol Biotechnol 74:1101–1109
Garrote G, Domínguez H, Parajó JC (2001) Kinetics modelling of corncob autohydrolysis. Process Biochem 36:571–578
Goli JK, Panda SH, Linga VR (2012) Molecular mechanism of D-xylitol production in yeasts: focus on molecular transportation, catabolic sensing and stress response. In: da Silva SS, Kumar CA (eds) D-Xylitol. Springer, Berlin, pp 85–107
González-Figueredo C, Sánchez A, Díaz G, Rodríguez F, Flores R, Ceballos MA, Ruiz HA (2015) Dynamic modelling and experimental validation of a pilot-Scale tubular continuous reactor for the autohydrolysis of lignocellulosic materials. In: Gernay KV, Huusom JK, Gani R (eds) 12th International symposium on process systems engineering and 25th European symposium on computer aided process engineering. Elsevier, pp 431–436
Gonçalves FA, Ruiz HA, Dos-Santos ES, Teixeira JA, de Macedo GR (2015) Bioethanol production from coconuts and cactus pretreated by autohydrolysis. Ind Crop Prod 77:1–12
Gonçalves FA, Ruiz HA, dos Santos ES, Teixeira JA, de Macedo GR (2016) Bioethanol production by Saccharomyces cerevisiae, Pichia stipitis and Zymomonas mobilis from delignified coconut fibre mature and lignin extraction according to biorefinery concept. Renew Energy 94:353–365
González-Muñoz MJ, Rivas S, Santos V, Parajó JC (2013) Aqueous processing of Pinus pinaster wood: kinetics of polysaccharides. Chem Eng J 231:380–387
Gullón P, Romaní A, Vila C, Garrote G, Parajó JC (2012) Potential of hydrothermal treatments in lignocellulose biorefineries. Biofuels Bioprod Biorefin 6:219–232
Hansen NM, Plackett D (2008) Sustainable films and coatings from hemicelluloses: a review. Biomacromolecules 9:1493–1505
IEA. IEA bioenergy Task 42. http://www.iea-bioenergy.task42-biorefineries.com/en/ieabiorefinery/Factsheets.htm. Accessed 16 Jun 2016
INBICON – DONG Energy. http://www.inbicon.com/en. Accessed 29 Jun 2016
Jacobsen SE, Wyman CE (2002) Xylose monomer and oligomer yields for uncatalyzed hydrolysis of sugarcane bagasse hemicellulose at varying solids concentration. Ind Eng Chem Res 41:1454–1461
Kim Y, Hendrickson R, Mosier N, Ladisch MR (2005) Plug-flow reactor for continuous hydrolysis of glucans and xylans from pretreated corn fiber. Energy Fuel 19:2189–2200
Kabel MA, Warard P, Schols HA, Voragen AGJ (2003) Location of O-acetyl substituents in xylo-oligosaccharides obtained from hydrothermally treated Eucalyptus wood. Carbohydr Res 338:69–77
Lima DU, Oliveira RC, Buckeridge MS (2003) Seed storage hemicelluloses as wet-end additives in papermaking. Carbohydr Polym 52:367–373
Liang X, Montoya A, Haynes BS (2016) Mechanistic insights and kinetic modeling of cellobiose decomposition in hot compressed water. Energy Fuels. In press Doi: 10.1021/acs.energyfuels.6b02187
Liu Z, Fatehi P, Sadeghi S, Ni Y (2011) Application of hemicelluloses precipitated via ethanol treatment of pre-hydrolysis liquor in high-yield pulp. Bioresour Technol 102:9613–9618
Lora JH, Wayman M (1980) Autohydrolysis of aspen milled wood lignin. Can J Chem 58:669–676
Marinova M, Mateos-Espejel E, Jemaa N, Paris J (2009) Addressing the increased energy demand of a Kraft mill biorefinery: the hemicellulose extraction case. Chem Eng Res Des 87:1269–1275
Michelin M, Ruiz HA, Silva DP, Ruzene DS, Teixeira JA, Polizeli MD (2015) Cellulose from lignocellulosic waste. In: Ramawat KG, Mérillon JM (eds) Polysaccharides: bioactivity and biotechnology. Springer, Switzerland, pp 475–511
Mittal A, Chatterjee SG, Scott GM, Amidon TE (2009a) Modeling xylan solubilization during autohydrolysis of sugar maple wood meal: reaction kinetics. Holzforschung 63:307–314
Mittal A, Chatterjee SG, Scott GM, Amidon TE (2009b) Modeling xylan solubilization during autohydrolysis of sugar maple and aspen wood chips: Reaction kinetics and mass transfer. Chem Eng Sci 64:3031–3041
Montané D, Overend RP, Chornet E (1998) Kinetic models for non-homogeneous complex system with a time-dependent rate constant. Can J Chem Eng 76:58–68
Mosier N, Wyman C, Dale B, Elander R, Lee YY, Holtzapple M et al (2005) Features of promising technologies for pretreatment of lignocellulosic biomass. Bioresour Technol 96:673–686
Mosier NS (2013) Fundamentals of aqueous pretreatment of biomass. In: Wyman CE (ed) Aqueous pretreatment of plant biomass for biological and chemical conversion to fuels and chemicals. Wiley, Chichester, pp 129–143
Moure A, Gullón P, Domínguez H, Parajó JC (2006) Advances in the manufacture, purification and applications of xylo-oligosaccharides as food additives and nutraceuticals. Process Biochem 41:1913–1923
Nabarlatz D, Farriol X, Montané D (2004) Kinetic modeling of the autohydrolysis of lignocellulosic biomass for the production of hemicellulose-derived oligosaccharides. Ind Eng Chem Res 43:4124–4131
Nabarlatz D, Farriol X, Montané D (2005) Autohydrolysis of almond shells for the production of xylo-oligosaccharides: product characteristics and reaction kinetics. Ind Eng Chem Res 44:7746–7755
Otieno DO, Ahring BK (2012) The potential for oligosaccharide production from the hemicellulose fraction of biomasses through pretreatment processes: xylooligosaccharides (XOS), arabinooligosaccharides (AOS), and mannooligosaccharides (MOS). Carbohydr Res 360:84–92
Overend RP, Chornet E (1987) Fractionation of lignocellulosic by steam-aqueous pretreatments. Philos Trans R Soc Lond A 321:523–536
Parajó JC, Garrote G, Cruz JM, Dominguez H (2004) Production of xylooligosaccharides by autohydrolysis of lignocellulosic materials. Trends Food Sci Technol 15:115–120
Pereira FB, Romaní A, Ruiz HA, Teixeira JA, Domingues L (2014) Industrial robust yeast isolates with great potential for fermentation of lignocellulosic biomass. Bioresour Technol 161:192–199
Pronyk C, Mazza G (2010) Kinetic modeling of hemicellulose hydrolysis from triticale straw in a pressurized low polarity water flow-through reactor. Ind Eng Chem Res 49:6367–6375
Rocha MSRS, Pratto B, Júnior RS, Almeida RMRG, Cruz AJG (2017) A kinetic model for hydrothermal pretreatment of sugarcane straw. Bioresour Technol 228:176–185
Romaní A, Ruiz HA, Pereira FB, Domingues L, Teixeira JA (2014) Effect of hemicellulose liquid phase on the enzymatic hydrolysis of autohydrolyzed Eucalyptus globulus wood. Biomass Conv Biorefin 4:77–86
Romaní A, Ruiz HA, Teixeira JA, Domingues L (2016) Valorization of Eucalyptus wood by glycerol-organosolv pretreatment within the biorefinery concept: an integrated and intensified approach. Renew Energy 95:1–9
Ruiz HA, Ruzene DS, Silva DP, Quintas MAC, Vicente AA, Teixeira JA (2011a) Evaluation of a hydrothermal process for pretreatment of wheat straw – effect of particle size and process conditions. J Chem Technol Biotechnol 86:88–94
Ruiz HA, Ruzene DS, Silva DP, da Silva FFM, Vicente AA, Teixeira JA (2011b) Development and characterization of an environmentally friendly process sequence (autohydrolysis and organosolv) for wheat straw delignification. Appl Biochem Biotechnol 164:629–641
Ruiz HA, Vicente AA, Teixeira JA (2012) Kinetic modeling of enzymatic saccharification using wheat straw under autohydrolysis and organosolv process. Ind Crop Prod 36:100–107
Ruiz HA, Rodríguez-Jasso RM, Fernandes BD, Vicente AA, Teixeira JA (2013a) Hydrothermal processing, as an alternative for upgrading agriculture residues and marine biomass according to the biorefinery concept: a review. Renew Sustain Energy Rev 21:35–51
Ruiz HA, Cerqueira MA, Silva HD, Rodríguez-Jasso RM, Vicente AA, Teixeira JA (2013b) Biorefinery valorization of autohydrolysis wheat straw hemicellulose to be applied in a polymer-blend film. Carbohydr Polym 92:2154–2162
Ruiz HA, Rodríguez-Jasso RM, Aguedo M, Kádár S (2015) Hydrothermal pretreatments of macroalgal biomass for biorefineries. In: Prokop A, Bajpai RK, Zappi ME (eds) Algal biorefineries, vol 2: Products and refinery design. Springer, Switzerland, pp 467–491
Ruiz HA, Martínez A, Vermerris W (2016) Bioenergy potential, energy crops, and biofuel production in Mexico. Bioenergy Res 9:981–984
Sabiha-Hanim S, Siti-Norsafurah AM (2012) Physical properties of hemicellulose films from sugarcane bagasse. Proc Eng 42:1390–1395
Samanta AK, Jayapal N, Jayaram C, Roy S, Kolte AP, Senani S, Sridhar M (2015) Xylooligosaccharides as prebiotics from agricultural by-products: production and applications. Bioact Carbohydr Diet Fibre 5:62–71
Sedlmeyer FB (2011) Xylan as by-product of biorefineries: characteristics and potential use for food applications. Food Hydrocoll 25:1891–1898
Shao X, Lynd L (2013) Kinetic modeling of xylan hydrolysis in co- and countercurrent liquid hot water flow-through pretreatments. Bioresour Technol 130:117–124
Tavast D, Mansoor ZA, Brännvall E (2014) Xylan from agro waste as a strength enhancing chemical in kraft pulping of softwood. Ind Eng Chem Res 53:9738–9742
Téllez-Luis SJ, Ramírez JA, Vázquez M (2002) Mathematical modelling of hemicellulosic sugar production from sorghum straw. Int J Food Eng 52:285–291
Vallejos ME, Felissia FE, Kruyeniski J, Area MC (2015) Kinetic study of the extraction of hemicellulosic carbohydrates from sugarcane bagasse by hot water treatment. Ind Crop Prod 67:1–6
Walch E, Zemann A, Schinner F, Bon G, Bobleter O (1992) Enzymatic saccharification of hemicellulose obtained from hydrothermally pretreated sugar cane bagasse and beech bark. Bioresour Technol 39:173–177
Walsum GPV, Allen SG, Spencer MJ, Laser MS, Antal MJ, Lynd LR (1996) Conversion of lignocellulosics pretreated with liquid hot water to ethanol. Appl Biochem Biotechnol 57(58):157–170
Wyman CE (2013) Introduction. In: Wyman CE (ed) Aqueous pretreatment of plant biomass for biological and chemical conversion to fuels and chemicals. Wiley, Chichester, pp 1–15
Xiao LP, Shi ZJ, Xu F, Sun RC (2013) Hydrothermal treatment and enzymatic hydrolysis of Tamarix ramosissima: evaluation of the process as a conversion method in a biorefinery concept. Bioresour Technol 153:73–81
Yu Y, Wu H (2010) Understanding the primary liquid products of cellulose hydrolysis in hot-compressed water at various reaction temperatures. Energy Fuel 24:1963–1971
Acknowledgments
Financial support from the Energy Sustainability Fund 2014-05 (CONACYT-SENER), Mexican Centre for Innovation in Bioenergy (Cemie-Bio), and Cluster of Bioalcohols (Ref. 249564) is gratefully acknowledged. We also gratefully acknowledge support for this research by the Mexican Science and Technology Council (CONACYT, Mexico) for the infrastructure project—INFR201601 (Ref. 269461) and CB-2015-01 (Ref. 254808). The authors Daniela Aguilar, Anely Lara, and Jesús Velázquez thank the National Council of Science and Technology (CONACYT, Mexico) for their master fellowship grant, and Elisa Zanuso thanks Energy Sustainability Fund 2014-05 (CONACYT-SENER, Ref. 249564) for undergraduate fellowship grant.
Author information
Authors and Affiliations
Corresponding author
Editor information
Editors and Affiliations
Rights and permissions
Copyright information
© 2017 Springer International Publishing AG
About this chapter
Cite this chapter
Zanuso, E. et al. (2017). Kinetic Modeling, Operational Conditions, and Biorefinery Products from Hemicellulose: Depolymerization and Solubilization During Hydrothermal Processing. In: Ruiz, H., Hedegaard Thomsen, M., Trajano, H. (eds) Hydrothermal Processing in Biorefineries. Springer, Cham. https://doi.org/10.1007/978-3-319-56457-9_5
Download citation
DOI: https://doi.org/10.1007/978-3-319-56457-9_5
Published:
Publisher Name: Springer, Cham
Print ISBN: 978-3-319-56456-2
Online ISBN: 978-3-319-56457-9
eBook Packages: EnergyEnergy (R0)