About

Log in?

DTU users get better search results including licensed content and discounts on order fees.

Anyone can log in and get personalized features such as favorites, tags and feeds.

Log in as DTU user Log in as non-DTU user No thanks

DTU Findit

Journal article

A Mathematical Model for Simultaneous Saccharification and Co-fermentation (SSCF) of C6 and C5 Sugars

From

Computer Aided Process Engineering Center, Department of Chemical and Biochemical Engineering, Technical University of Denmark1

Department of Chemical and Biochemical Engineering, Technical University of Denmark2

Center for BioProcess Engineering, Department of Chemical and Biochemical Engineering, Technical University of Denmark3

Reliable production of biofuels and specifically bioethanol has attracted a significant amount of research recently. Within this context, this study deals with dynamic simulation of bioethanol production processes and in particular aims at developing a mathematical model for describing simultaneous saccharification and co-fermentation (SSCF) of C6 and C5 sugars.

The model is constructed by combining existing mathematical models for enzymatic hydrolysis and co-fermentation. An inhibition of ethanol on cellulose conversion is introduced in order to increase the reliability. The mathematical model for the SSCF is verified by comparing the model predictions with experimental data obtained from the ethanol production based on kraft paper mill sludge.

When fitting the model to the data, only the yield coefficients for glucose and xylose metabolism were fine-tuned, which were found to be 0.43 g·g−1 (ethanol/glucose) and 0.35 g·g−1 (ethanol/xylose) respectively. These promising validation results encourage further model application to evaluate different process configurations for lignocellulosic bioethanol technology.

Language: English
Year: 2011
Pages: 185-191
ISSN: 2210321x , 08920370 and 10049541
Types: Journal article
DOI: 10.1016/S1004-9541(11)60152-3
ORCIDs: Gernaey, Krist , Meyer, Anne S. and Sin, Gürkan

DTU users get better search results including licensed content and discounts on order fees.

Log in as DTU user

Access

Analysis