Catalytic Conversion of Biomass to Fuels and Chemicals Using Ionic Liquids

Liu, Wei ; Zheng, Richard ; Brown, Heather ; Li, Joanne ; Holladay, John ; Cooper, Alan ; Rao, Tony

Pacific Northwest National Laboratory (U.S.)

关键词: Heat Transfer;    Biomass;    Mixtures;    Mass Balance;    Cellulose;   

DOI  :  10.2172/1038693
RP-ID  :  PNNL-21304
RP-ID  :  DE-AC05-76RL01830
RP-ID  :  1038693

美国|英语

来源: UNT Digital Library

【 摘 要 】

This project provides critical innovations and fundamental understandings that enable development of an economically-viable process for catalytic conversion of biomass (sugar) to 5-hydroxymethylfurfural (HMF). A low-cost ionic liquid (Cyphos 106) is discovered for fast conversion of fructose into HMF under moderate reaction conditions without any catalyst. HMF yield from fructose is almost 100% on the carbon molar basis. Adsorbent materials and adsorption process are invented and demonstrated for separation of 99% pure HMF product and recovery of the ionic liquid from the reaction mixtures. The adsorbent material appears very stable in repeated adsorption/regeneration cycles. Novel membrane-coated adsorbent particles are made and demonstrated to achieve excellent adsorption separation performances at low pressure drops. This is very important for a practical adsorption process because ionic liquids are known of high viscosity. Nearly 100% conversion (or dissolution) of cellulose in the catalytic ionic liquid into small molecules was observed. It is promising to produce HMF, sugars and other fermentable species directly from cellulose feedstock. However, several gaps were identified and could not be resolved in this project. Reaction and separation tests at larger scales are needed to minimize impacts of incidental errors on the mass balance and to show 99.9% ionic liquid recovery. The cellulose reaction tests were troubled with poor reproducibility. Further studies on cellulose conversion in ionic liquids under better controlled conditions are necessary to delineate reaction products, dissolution kinetics, effects of mass and heat transfer in the reactor on conversion, and separation of final reaction mixtures.