TY - JOUR
T1 - Process integration for the conversion of glucose to 2,5-furandicarboxylic acid
AU - Boisen, A.
AU - Christensen, T.B.
AU - Fu, Wenjing
AU - Gorbanev, Yury
AU - Hansen, T.S.
AU - Jensen, J.S.
AU - Kegnæs, Søren
AU - Pedersen, S.
AU - Riisager, Anders
AU - Ståhlberg, Tim
AU - Woodley, John
PY - 2009
Y1 - 2009
N2 - The development of biorefineries means that a key feedstock for many new processes will be sugars in various forms, such as glucose or fructose. From these feedstocks a range of chemicals can be synthesized using heterogeneous catalysis, immobilized enzymes, homogeneous catalysts, soluble enzymes, fermentations or combinations thereof. This presents a particularly interesting process integration challenge since the optimal conditions for each conversion step will be considerably different from each other. Furthermore, compared to oil-based refineries the feedstock represents a relatively high proportion of the final product value and therefore yield and selectivity in these steps are of crucial importance. In this paper using the conversion of glucose to 2,5-furandicarboxylic acid and associated products as an example, alternative routes will be compared with respect to achievable selectivity, and achievable yield.
AB - The development of biorefineries means that a key feedstock for many new processes will be sugars in various forms, such as glucose or fructose. From these feedstocks a range of chemicals can be synthesized using heterogeneous catalysis, immobilized enzymes, homogeneous catalysts, soluble enzymes, fermentations or combinations thereof. This presents a particularly interesting process integration challenge since the optimal conditions for each conversion step will be considerably different from each other. Furthermore, compared to oil-based refineries the feedstock represents a relatively high proportion of the final product value and therefore yield and selectivity in these steps are of crucial importance. In this paper using the conversion of glucose to 2,5-furandicarboxylic acid and associated products as an example, alternative routes will be compared with respect to achievable selectivity, and achievable yield.
U2 - 10.1016/j.cherd.2009.06.010
DO - 10.1016/j.cherd.2009.06.010
M3 - Journal article
SN - 0263-8762
VL - 87
SP - 1318
EP - 1327
JO - Chemical Engineering Research & Design
JF - Chemical Engineering Research & Design
IS - 9
ER -