Dilute Acid Hydrolysis of Sugar Cane Bagasse at High Temperatures: A Kinetic Study of Cellulose Saccharification and Glucose Decomposition. Part I: Sulfuric Acid as the Catalyst
Contribuinte(s) |
UNIVERSIDADE DE SÃO PAULO |
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Data(s) |
05/11/2013
05/11/2013
2012
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Resumo |
The kinetics of sugar cane bagasse cellulose saccharification and the decomposition of glucose under extremely low acid (ELA) conditions, (0.07%), 0.14%, and 0.28% H2SO4, and at high temperatures were investigated using batch reactors. The first-order rate constants were obtained by weight loss, remaining glucose, and fitting glucose concentration profiles determined with HPLC using the Saeman model. The maximum glucose yields reached 67.6% (200 degrees C, 0.07% H2SO4, 30 min), 69.8% (210 degrees C, 0.14% H2SO4, 10 min), and 67.3% (210 degrees C, 0.28% H2SO4, 6 min). ELA conditions produced remarkable glucose yields when applied to bagasse cellulose. The first-order rate constants were used to calculate activation energies and extrathermodynamic parameters to elucidate the reaction mechanism under ELA conditions. The effect of acid concentration on cellulose hydrolysis and glucose decomposition was also investigated. The observed activation energies and reaction orders with respect to hydronium ion for cellulose hydrolysis and glucose decomposition were 184.9 and 124.5 kJ/mol and 1.27 and 0.75, respectively. Conselho Nacional de Pesquisa e Desenvolvimento (CNPq) Conselho Nacional de Pesquisa e Desenvolvimento (CNPq) Fundacao de Amparo a Pesquisa do Estado de Sao Paulo (FAPESP) Fundacao de Amparo a Pesquisa do Estado de Sao Paulo (FAPESP) Oxiteno Oxiteno |
Identificador |
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, WASHINGTON, v. 51, n. 3, supl. 4, Part 1-2, pp. 1173-1185, 45658, 2012 0888-5885 http://www.producao.usp.br/handle/BDPI/40932 10.1021/ie2025739 |
Idioma(s) |
eng |
Publicador |
AMER CHEMICAL SOC WASHINGTON |
Relação |
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH |
Direitos |
restrictedAccess Copyright AMER CHEMICAL SOC |
Palavras-Chave | #ETHANOL #BIOMASS #REACTOR #ENERGY #ENGINEERING, CHEMICAL |
Tipo |
article original article publishedVersion |