Preparation of bio-polyols from lignocellulosic waste by liquefaction

Document Type : Research Paper

Authors

1 Ph.D. student, Wood and paper science department, Faculty of natural resources, Tarbiat Modares university, Noor, Iran

2 Associate Prof., Wood and paper science department, Faculty of natural resources, Tarbiat Modares university, Noor, Iran

3 Professor, Polyurethane and material advanced department, Faculty of science, Polymer and petrochemical institute, Tehran, Iran

Abstract

Rigid polyurethane foam (PUF) with desirable properties such as low thermal conductivity, easy production and processing is extensively used in the industrial applications. Currently, the PU industry is heavily petroleum-dependent, because its two major feedstocks, i.e. polyols and isocyanates, are largely petroleum-derived. Due to concerns over the depletion of fossil resources, pollution, there has been a great deal of interest in developing bio-based polyols from renewable resources. Lignocellulosic biomass is considered to be suitable for production of bio-based polyols, having hydroxyl group rich compounds. In bio-refining processes, the lignocellulosic macromolecular are broken down and converted into a viscous liquid using certain solvents. The use of high volumes of liquefaction solvents increases the production cost of bio-polyols. This has led to research on low cost and renewable solvents such as crude glycerol. In this research crude glycerol was used as solvent for liquefaction of sawdust and polyol production. The influence of process variables such as reaction temperature and time on polyol properties, namely biomass conversion ratio, acid number, hydroxyl number and viscosity were measured according to the certain standards. With increasing liquefaction temperature, increased production efficiency and viscosity and acid, hydroxyl number of polyols decreased. Finally, polyol of liquefaction at 180 and 360 min with production efficiency of 51%, acid, hydroxyl number and viscosity of 9/7, 325 mgKOH/g and 18 Pa,s was determinate as optimum polyol.

Keywords

Main Subjects


[1] Xu, Z.B, Tang, X.L., Gu, A.J. and Fang, Z.P., 2007. Novel preparation and mechanical properties of rigid polyurethane foam/organoclay nanocomposites. Applied Polymer Science, 106 (4): 439-442.
[2] Petrovic, Z.S., Yang, L., Zlatanic, A., Zhang, W. and Javni, I., 2007. Network structure and properties of polyurethanes from soybean oil. Applied Polymer Science, 105 (5): 2717–2727.
[3] Sercer, M., Raos, P. and Rujni Sokele, M., 2012. Study on thermal properties of synthetic and bio-based polyurethane. Science Journal, 5 (2): 1-11.
[4] Hatakeyama, H., Kosugi, R. and Hatakeyama, T., 2008. Thermal properties of lignin-and molasses-based polyurethane foams.Thermal Analysis and Calorimetry, 92 (2): 419-424.
[5] Zheng, Z., Pan, H., Huang, Y., Chung, Y.H., Zhang, X. and Feng, H., 2011. Rapid liquefaction of wood in polyhydric alcohols under microwave heating and its liquefied products for preparation of rigid polyurethane foam.The Open Materials Science Journal, 5 (3): 1-8.
[6] Xu, J., Jiang, J., Hse, C.Y. and Shupe, T.F., 2013. Preparation of polyurethane foams using fractionated products in liquefied wood. Applied Polymer Science, 84 (4): 1-7.
[7] Demirbas, A., 2010. Biorefineries for biomass upgrading facilities. Green Energy and Technology, 12 (2): 139-149.
[8] Chen, F. and Lu, Z., 2009. Liquefaction of wheat straw and preparation of rigid polyurethane foam from the liquefaction products. Applied Polymer Science, 111 (3): 508-516.
[9] Lee, S.H., Yoshioka, M. and Shiraishi, N., 2000. Liquefaction of corn bran (CB) in the presence of alcohols and preparation of polyurethane foam from its liquefied polyol. Applied Polymer Science, 78 (3): 319-325.
[10] Satpathy, P., Thosa A. and Rajan, A.R., 2014. Green technology for glycerol waste from biodiesel plant. Current Microbioloy and Applied Science, 3 (2): 730-739.
[11] Hu, S., Wan, C. and Li, Y., 2012. Production and characterization of bio-polyols and polyurethane foams from crude glycerol based liquefaction of soybean straw. Bio-resource Technology, 103 (5): 227–233.
[12] Hu, S. and Li, Y., 2014. Two-step sequential liquefaction of lignocellulosic biomass by crude glycerol for the production of polyols and polyurethane foams. Bioresource Technology, 161 (6): 410–415.
[13] Kosmela, P., Hejna, A., Formela, K., Haponiuk, J.K. and Piszczyk, L., 2016. Bio-polyols obtained via crude glycerol-based liquefaction of cellulose: their structural, rheological and thermal character. Cellulose, 23: 2929–2942.
[14] Standard Test Method for Acid Value Determination of polyester or polyether polyols. ASTM D 4662, 2008.
[15] Standard Test Method for Hydroxyl Value Determination of polyester or polyether polyols. ASTM D 4274, 2005.
[16] Wang, Y., Wu, J., Wan, Y.L.H., Yu, F., Chen, P., Lin, X., Liu, Y. and Ruan, R., 2009. Liquefaction of corn stover using industrial biodiesel glycerol. Agricultural and Biological Engineering, 2 (2): 32–40.
[17] Standard Test Method for Viscosity Determination of Asphalt at Elevated Temperatures Using a Rotational Vis-cometer. ASTM D 4878, 2008.
[18] Biswas, A.K. and Ganguly, D., 1960. Esteriļ¬cation of fatty acids with glycerol. Nature, 188: 56-57.
[19] Yao, Y., Yoshioka, M. and Shiraishi, N., 1995. Rigid polyurethane foams from liquefaction mixture of wood and starch. Mokuzai Gakkaishi, 41 (7): 659-668.