Renewable chemical feedstocks from integrated liquefaction processing of lignocellulosic materials using microwave energy.

The objective of this investigation was to find a simple method for the production of phenolic rich products and sugar derivatives (biopolyols) via separation of liquefied lingocellulosic materials. Liquefaction of lignocellulosic materials was conducted in methanol at 180 °C for 15 min with the conversion of raw materials at about 75%. After liquefaction, the liquefied products were separated by addition of a sufficient amount of water. It was found that the hydrophobic phenolics could be largely separated from aqueous solutions. The phenolic products that precipitated from the aqueous phase were mainly composed of phenolic derivatives such as 2-methoxy-4-propyl-phenol and 4-hydroxy-3-methoxy-benzoic acid methyl ester. Afterwards, the aqueous solution was distilled under vacuum to remove water and formed a viscous liquid product henceforth termed biopolyol. As evidenced by GC-MS analysis, the biopolyols contained methyl sugar derivatives, including methyl β-D-mannofuranoside, methyl α-D-galactopyranoside, methyl α-D-glucopyranoside, and methyl β-D-glucopyranoside. The effect of glycerol on promotion of the liquefaction reaction was also studied. The yield of residue was significantly decreased from approximately 25 to 12% when a glycerol–methanol mixture was used as solvent rather than methanol. According to the GC-MS analysis, the total content of phenolics and poly-hydroxy compounds (including glycerol and sugar derivatives) in phenolic products and biopolyols was 65.9 and 84.9%, respectively. Therefore, a new method for fractionation of liquefied products was proposed according to the molecular structure of the biomass.

[1]  Anthony V. Bridgwater,et al.  Production of renewable phenolic resins by thermochemical conversion of biomass: a review , 2008 .

[2]  Caixia Wan,et al.  Production and characterization of biopolyols and polyurethane foams from crude glycerol based liquefaction of soybean straw. , 2012, Bioresource technology.

[3]  Fangeng Chen,et al.  Liquefaction of wheat straw and preparation of rigid polyurethane foam from the liquefaction products , 2009 .

[4]  Asri Gani,et al.  Effect of cellulose and lignin content on pyrolysis and combustion characteristics for several types of biomass. , 2007 .

[5]  A. Corma,et al.  Synthesis of transportation fuels from biomass: chemistry, catalysts, and engineering. , 2006, Chemical reviews.

[6]  Johnathan E. Holladay,et al.  Phenol and phenolics from lignocellulosic biomass by catalytic microwave pyrolysis. , 2011, Bioresource technology.

[7]  S. Saka,et al.  Kinetic behavior of liquefaction of Japanese beech in subcritical phenol. , 2011, Bioresource technology.

[8]  Xianwu Zou,et al.  Mechanisms and Product Specialties of the Alcoholysis Processes of Poplar Components , 2011 .

[9]  A. Bridgwater,et al.  Overview of Applications of Biomass Fast Pyrolysis Oil , 2004 .

[10]  G. Huber,et al.  Renewable Chemical Commodity Feedstocks from Integrated Catalytic Processing of Pyrolysis Oils , 2010, Science.

[11]  B. Weckhuysen,et al.  The catalytic valorization of lignin for the production of renewable chemicals. , 2010, Chemical reviews.

[12]  Seung‐Hwan Lee,et al.  Biodegradable polyurethane foam from liquefied waste paper and its thermal stability, biodegradability, and genotoxicity , 2002 .

[13]  Zhang Hairong,et al.  Investigation of liquefied wood residues based on cellulose, hemicellulose, and lignin , 2012 .

[14]  Zhijun Zhang,et al.  Catalytic upgrading of bio-oil using 1-octene and 1-butanol over sulfonic acid resin catalysts , 2011 .

[15]  T. Asano,et al.  Analysis on residue formation during wood liquefaction with polyhydric alcohol , 2004, Journal of Wood Science.

[16]  Juan Liu,et al.  Liquefaction of Bagasse and Preparation of Rigid Polyurethane Foam from Liquefaction Products , 2009 .

[17]  E. Hassan,et al.  Polyhydric alcohol liquefaction of some lignocellulosic agricultural residues , 2008 .