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Synthesis of Platform Chemicals from Renewable Resources by Applying Micro Reaction Technology Tobias Türcke, Dr. Stefan Löbbecke, Fraunhofer Institute for Chemical Technology ICT, 76327 Pfinztal, Germany Despite the fact that today’s chemical production is still dominated by petroleumderived chemical components, the interest in renewable resources as chemical feedstock’s has been growing fast in recent years. Diminishing petrochemical resources, increasing oil costs as well as growing concerns about global warming and rising CO 2 emissions are major drivers to increasingly seek for sustainable resources. Therefore, biomass is currently considered as a promising and renewable substitute for fossil-based resources. Not only the exploitation of new resources but also the efficient use of biomass by effluent treatment and the recovery of chemicals from biomass waste streams have become industrial issues of major economic and environmental importance. The ability to convert industrial waste streams into valuable products can make the difference between realizing and abandoning a chemical process. Here, we report on our recent studies on the continuous conversion of fructose from biomass into 5-hydroxymethylfurfural (5-HMF) and xylose from pulp waste into furfural by applying micro reaction technology. Both 5-HMF and furfural are promising building blocks for chemical industry to form polymers, fine chemicals and solvents. Different continuous microreaction processes for rapid screening of different process condition were set up to analyze and improve the acid-catalyzed dehydration of fructose to 5-HMF and the conversion of xylose to furfural. To allow processing of viscous media under harsh process conditions special designed micro reactors were developed. The microreactors were made of glass and could be operated at pressures up to 25 bar and temperatures up to 300°C. The reactions were carried out either in pure aqueous solutions or by using appropriate organic co-solvents for product extraction. Variations in temperature (150-200°C), residence time (30-60 s) and acid concentration were done by processing both freshly prepared solutions and diluted aqueous waste streams coming from the pulp process. The reactions were terminated by rapid quenching of the reaction mixture. The latter was analyzed by HPLC. 5-HMF was obtained with 75% selectivity and 54% yield at 71% fructose conversion in a pure aqueous solution. In comparison to published data, a 24% increase in selectivity and a 21% increase in conversion were achieved. For the xylose containing waste media conversions of more than 50% and furfural yields higher than 20% could be reached. Moreover, by adding organic co-solvents and extraction agents to the reaction system the conversion and yield were dramatically increased. For the fructose conversion both 5-HMF selectivity and yield could be further enhanced to 85% and 82%, respectively. For the pulp waste streams a xylose conversion of more than 80% and yields higher than 50% were achieved.