Open Access. Powered by Scholars. Published by Universities.®

Chemical Engineering Commons

Open Access. Powered by Scholars. Published by Universities.®

George W. Huber

Selected Works

2010

Articles 1 - 2 of 2

Full-Text Articles in Chemical Engineering

Kinetics Of Furfural Production By Dehydration Of Xylose In A Biphasic Reactor With Microwave Heating, George W. Huber, R. Weingarten, J. Cho, W. C. Conner Jr. Jan 2010

Kinetics Of Furfural Production By Dehydration Of Xylose In A Biphasic Reactor With Microwave Heating, George W. Huber, R. Weingarten, J. Cho, W. C. Conner Jr.

George W. Huber

In this paper we report a kinetic model for the dehydration of xylose to furfural in a biphasic batch reactor with microwave heating. There are four key steps in our kinetic model: (1) xylose dehydration to form furfural; (2) furfural reaction to form degradation products; (3) furfural reaction with xylose to form degradation products, and (4) mass transfer of furfural from the aqueous phase into the organic phase (methyl isobutyl ketone - MIBK). This kinetic model was used to fit experimental data collected in this study. The apparent activation energy for xylose dehydration is higher than the apparent activation energy …


Production Of Jet And Diesel Fuel Range Alkanes From Waste Hemicellulose-Derived Aqueous Solutions, George W. Huber, R. Xing, A. V. Subrahmanyam, H. Olcay, W. Qi, G. P. Van Walsum, H. P. Pendse Dec 2009

Production Of Jet And Diesel Fuel Range Alkanes From Waste Hemicellulose-Derived Aqueous Solutions, George W. Huber, R. Xing, A. V. Subrahmanyam, H. Olcay, W. Qi, G. P. Van Walsum, H. P. Pendse

George W. Huber

In this paper we report a novel four-step process for the production of jet and diesel fuel range alkanes from hemicellulose extracts derived from northeastern hardwood trees. The extract is representative of a byproduct that could be produced by wood-processing industries such as biomass boilers or pulp mills in the northeastern U.S. The hemicellulose extract tested in this study contained mainly xylose oligomers (21.2 g/l xylose after the acid hydrolysis) as well as 0.31 g/l glucose, 0.91 g/l arabinose, 0.2 g/l lactic acid, 2.39 g/l acetic acid, 0.31 g/l formic acid, and other minor products. The first step in this …