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Hydrolysis of sugarcane bagasse in subcritical water
Affiliation:1. Department of Chemical Engineering and Centro de Química Estrutural, Instituto Superior Técnico, Universidade de Lisboa, Lisboa, Portugal;2. Department of Health Sciences, Luleå University of Technology, Luleå, Sweden;1. High Pressure Processes Group, Department of Chemical Engineering and Environmental Technology, University of Valladolid, C/Dr Mergelina s/n, 47011, Valladolid, Spain;2. Department of Applied and Industrial Chemistry, Faculty of Exact, Physical and Natural Sciences, National University of Córdoba, Av. Velez Sarsfield 1611, 5000 Córdoba, Argentina;1. School of Food Engineering, University of Campinas (UNICAMP), Rua Monteiro Lobato, n. 80, 13083-862 Campinas, SP, Brazil;2. Department of Chemical Engineering, Worcester Polytechnic Institute, 100 Institute Road, Goddard Hall 123, Worcester, MA 01609, United States;3. School of Applied Sciences, University of Campinas (UNICAMP), Rua Pedro Zaccaria, n. 1300, 13484-350 Limeira, SP, Brazil
Abstract:In this work, a subcritical water process was used for the hydrolysis of sugarcane bagasse with the aim of producing fermentable sugars. Hydrolysis kinetics was determined using a semi-batch unit equipped with a 50 mL reactor. Different sample loads (2 and 11 g), flow-rates (11, 22, 33, 44 and 55 mL/min) and temperatures (213, 251 and 290 °C) were evaluated, while maintaining constant pressure (20 MPa). The liquefaction degree of the sugarcane bagasse was not affected by water flow rate and increased with temperature; the maximum liquefaction degree was 95% for hydrolysis at 251 °C and 33 mL/min. The total reducing sugars recovered increased with flow rate up to 23%. The hydrolysis process was completed faster at higher temperatures, requiring 16 min. Maximum monosaccharides + cellobiose + cellotriose yield was 5.6% at 213 °C and 33 mL/min. Approximately 60% of the sugars recovered were in the oligomeric form.
Keywords:Subcritical water hydrolysis  Sugarcane bagasse  Sugars
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