The pyrolysis characteristics of wood waste containing different types of varnishes

The pyrolysis characteristics of wood waste containing different types of varnishes

The wood industry produces large amounts of wood waste. This waste usually contains a number of nonwood materials, such as paints or varnishes. In this study, the pyrolysis characteristics of wood waste containing synthetic, polyurethane, and polyester varnishes were investigated for conversion into renewable liquid fuels. The elemental analysis and higher heating values of the biooils were determined. The chemical compounds present in the bio-oils obtained at an optimum temperature were identified by gas chromatography/mass spectroscopy analysis. The product yields and compositions were affected by the types of varnishes. The maximum bio-oil yield of 46.7% was obtained from pyrolysis of waste wood containing polyester varnish at a final pyrolysis temperature of 500 °C. The bio-oil produced from wood waste containing varnishes was composed mainly of phenols, aldehydes, acids, ketones, alcohols, benzenes, and N-containing compounds. The phenols accounted for the largest amount of compounds in the bio-oils. Therefore, the bio-oil produced from varnished wood waste could be a potential substitute for biofuels and green chemicals.

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  • American Society for Testing and Materials (1997). Standard Test Method for Direct Moisture Content Measurement of Wood and Wood-Base Materials. ASTM Standard D 4442-92. Easton, MD, USA: ASTM.
  • American Society for Testing and Materials (1983). Standard Test Method for Ash in Wood. ASTM Standard D 1102-84. Easton, MD, USA: ASTM.
  • American Society for Testing and Materials (2004). Standard Test Method for Volatile Matter in Analysis Sample Refuse Derived Fuel. ASTM Standard E 897-88. Easton, MD, USA: ASTM.
  • Amutio M, Lopez G, Artetxe M, Elordi G, Olazar M, Bilbao J (2012). Influence of temperature on biomass pyrolysis in a conical spouted bed reactor. Resour Conserv Recy 59: 23-31.
  • Balat M, Ayar G (2005). Biomass energy in the world. Use of biomass and potential trends. Energ Source 27: 931-940.
  • Borchers AM, Duke JM, Parsons GR (2007). Does willingness to pay for green energy differ by source? Energ Policy 35: 3327-3334. Bridgwater AV (2003). Renewable fuels and chemicals by thermal processing of biomass. Chem Eng J 91: 87-102.
  • Bu Q, Lei H, Wang L, Wei Y, Zhu L, Liu Y, Liang J, Tang J (2013). Renewable phenols production by catalytic microwave pyrolysis of Douglas fir sawdust pellets with activated carbon catalysts. Bioresource Technol 142: 546-552.
  • Bu Q, Lei H, Wang L, Zhang Q, Tang J, Ruan R (2012). Production of phenols and biofuels by catalytic microwave pyrolysis of lignocellulosic biomass. Bioresource Technol 108: 274-279.
  • Channiwala SA, Parikh PP (2002). A unified correlation for estimating HHV of solid, liquid and gaseous fuels. Fuel 81: 1051-1063.
  • Chiaramonti D, Oasmaa A, Solantausta Y, (2007). Power generation using fast pyrolysis liquids from biomass. Renew Sust Energ Rev 11: 1056-1086.
  • Conesa JA, Font R, Fullana A, Martın-Gullon I, Aracil I, Galvez A, Molto J, Gomez-Rico MF (2009). Comparison between emissions from the pyrolysis and combustion of different wastes. J Anal Appl Pyrol 84: 95-102.
  • Demiral İ, Ayan EA (2011). Pyrolysis of grape bagasse: effect of pyrolysis conditions on the product yields and characterization of the liquid product. Bioresource Technol 102: 3946-3951.
  • Ertaş M (2010). Slow pyrolysis of some biomass residues and characterization of pyrolysis products. PhD, Kahramanmaraş Sütçü Imam University, Kahramanmaraş, Turkey.
  • Ertaş M, Alma HM (2010a). Pyrolysis of laurel (Laurus nobilis L.) extraction residues in a fixed-bed reactor characterization of bio-oil and bio-char. J Anal Appl Pyrol 88: 22-29.
  • Ertaş M, Alma MH (2010b). Slow pyrolysis of chinaberry (Melia azedarach L.) seeds: Part I. The influence of pyrolysis parameters on the product yields. Energy Educ Sci Tech 26: 143-154.
  • Fagbemi L, Khezami L, Capart R (2001). Pyrolysis products from different biomasses: application to the thermal cracking of tar. Appl Energ 69: 293-306.
  • Girods P, Rogaume Y, Dufour A, Rogaume C, Zoulalian A (2008). Low-temperature pyrolysis of wood waste containing urea– formaldehyde resin. Renew Energ 33: 648-654.
  • Heo SH, Park HJ, Park YK, Ryu C, Suh DJ, Suh YW, Yim JH, Kim SS (2010). Bio-oil production from fast pyrolysis of waste furniture sawdust in a fluidized bed. Bioresource Technol 101: 91-96.
  • Ingemarsson A, Nilsson U, Nilsson M, Pedersen JR, Olsson JO (1998). Slow pyrolysis of spruce and pine samples studied with GC/MS and GC/FTIR/FID. Chemosphere 36: 2879-2889.
  • Ingram L, Mohan D, Bricka M, Steele P, Strobel D (2008). Pyrolysis of wood and bark in an auger reactor: Physical properties and chemical analysis of the produced bio-oils. Energ Fuel 22: 614- 625.
  • Jahirul MI, Rasul MG, Chowdhury AA, Ashwath N (2012). Biofuels production through Biomass pyrolysis-A technological review. Energies 5: 4952-5001.
  • Kantarelis E, Yang W, Blasiak W (2013). Production of liquid feedstock from biomass via steam pyrolysis in a fluidized bed reactor. Energ Fuel 27: 4748-4759.
  • Khalfi A Trouve G, Delobel R, Delfosse L (2000). Correlation of CO and PAH emissions during laboratory-scale incineration of wood waste furnitures. J Anal Appl Pyrol 56: 243-262.
  • Kim JW, Lee HW, Lee I, Jeon JK, Ryu C, Park SH, Jung SC, Park YK (2014). Influence of reaction conditions on bio-oil production from pyrolysis of construction waste wood. Renew Energ 65: 41-48.
  • Kim KH, Eom IY, Lee SM, Choi, D, Yeo H, Choi IG, Choi JW (2011). Investigation of physicochemical properties of bio-oils produced from yellow poplar wood (Liriodendron tulipifera) at various temperatures and residence times. J Anal Appl Pyrol 92: 2-9.
  • Kinata SE, Loubar K, Bouslamti A, Belloncle C, Tazerout M (2012). Influence of impregnation method on metal retention of CCBtreated wood in slow pyrolysis process. J Hazard Mater 233- 234: 172-176.
  • Ku CS, Mun SP (2006). Characterization of pyrolysis tar derived from lignocellulosic biomass. J Ind Eng Chem 12: 853-861.
  • Kumar A, Jones DD, Hanna MA (2009). Thermochemical biomass gasification: a review of the current status of the technology. Energies 2: 556-581.
  • Lu Q, Yang X, Dong C, Zhang Z, Zhang X, Zhu X (2011). Influence of pyrolysis temperature and time on the cellulose fast pyrolysis products: analytical Py-GC/MS study. J Anal Appl Pyrol 92: 430-438.
  • Mohammed TH, Lakhmiri R, Azmani A (2014). Bio-oil from pyrolysis of castor seeds. International Journal of Basic & Applied Sciences 14: 1-4.
  • Mourant D, Lievens C, Gunawan R, Wang Y, Hu X, Wu L, SyedHassan SSA, Li CZ (2013). Effects of temperature on the yields and properties of bio-oil from the fast pyrolysis of mallee bark. Fuel 108: 400-408.
  • Murata K, Liu Y, Inaba M, Takahara I (2012). Catalytic fast pyrolysis of jatropha wastes. J Anal Appl Pyrol 94: 75-82.
  • Özbay G (2015). Pyrolysis of firewood (Abies bornmülleriana Mattf.) sawdust: characterization of bio-oil and bio-char. Drvna Industrija 66: 105-114.
  • Özbay G, Özçifçi A, Karagöz S (2013). Catalytic pyrolysis of waste melamine coated chipboard. Environmental Progress and Sustainable Energy 32: 156-161.
  • Özçifçi A, Özbay G (2013). Bio-oil production from catalytic pyrolysis method of furniture industry sawdust. Journal of the Faculty of Engineering & Architecture of Gazi University 28: 473-479 (in Turkish with English abstract).
  • Phan AN, Ryu C, Sharifi VN, Swithenbank J (2008). Characterisation of slow pyrolysis products from segregated wastes for energy production. J Anal Appl Pyrol 81: 65-71.
  • Ren S, Lei H, Wang L, Quan Q, Chen S, Wu J, Julson J, Ruan R (2012). Biofuel production and kinetics analysis for microwave pyrolysis of Douglas fir sawdust pellet. J Anal Appl Pyrol 94: 163-169.
  • Rowell RM, Pettersen R, Han JS, Rowell JS, Tshabalala MA (2005). Handbook of Wood Chemistry and Wood Composites. Boca Raton, FL, USA: CRC Press.
  • Roy C, Lu X, Pakdel H (2000). Process for the Production of PhenolicRich Pyrolysis Oils for Use in Making Phenol-Formaldehyde Resole Resins. U.S. Patent 6143856.
  • Shen DK, Gu S (2009). The mechanism for thermal decomposition of cellulose and its main products. Bioresource Technol 100: 6496-6504.
  • Song Y, Tahhmasebi A, Yu J (2014). Co-pyrolysis of pine sawdust and lignite in a thermogravimetric analyzer and a fixed-bed reactor. Bioresource Technol 174: 204-211.
  • Taşçıoğlu C, Tufan M (2011). A general evaluation for recycling process of impregnated wood removed from the service. Artvin Çoruh University Faculty of Forestry Journal 12: 86-91 (in Turkish with English abstract).
  • Technical Association of the Pulp and Paper Industry (1997). Solvent Extractives of Wood and Pulp. TAPPI T 204 cm-97. Atlanta, GA, USA: TAPPI.
  • Technical Association of the Pulp and Paper Industry (2002). AcidInsoluble Lignin in Wood and Pulp. TAPPI T 222 om-02. Atlanta, GA, USA: TAPPI.
  • Trinh NT, Jensen PA, Sárossy Z, Dam-Johansen K, Knudsen NO, Sørensen HR, Egsgaard H (2013). Fast pyrolysis of lignin using a pyrolysis centrifuge reactor. Energ Fuel 27: 3802-3810.
  • Tutuş A, Kurt R, Alma MH, Meriç H (2010). Sarıçam odununun kimyasal analizi ve termal özellikleri. In: III. Ulusal Karadeniz Ormancılık Kongresi, pp. 1845-1851 (in Turkish).
  • Windeisen E, Wegener G (2008). Behaviour of lignin during thermal treatments of wood. Ind Crop Prod 27: 157-162.
  • Wise LE, John EC (1952). Wood Chemistry. New York, NY, USA: Reinhold.
  • Zabeti M, Nguyen TS, Lefferts L, Heeres HJ, Seshan K (2012). In situ catalytic pyrolysis of lignocellulose using alkali-modified amorphous silica alumina. Bioresource Technol 118: 374-381. Žilnik LF, Jazbinšek A (2012). Recovery of renewable phenolic fraction from pyrolysis oil. Sep Purif Technol 86: 157-170.