Effect of pyrolysis temperature on the yield and properties of bio-oils obtained from the auger pyrolysis of Douglas Fir wood

This paper reports the effect of pyrolysis temperature on the yield and composition of bio-oils obtained from the auger pyrolysis of Douglas Fir wood. The tests were conducted at reactor wall temperatures between 200 and 600 °C. Due to the relatively low heat transfer rates achieved between the reac...

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Main Authors: Liaw, S., Wang, Z., Ndegwa, P., Frear, C., Ha, S., Li, Chun-Zhu, Garcia-Perez, M.
Format: Journal Article
Published: Elsevier 2012
Online Access:http://hdl.handle.net/20.500.11937/46667
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author Liaw, S.
Wang, Z.
Ndegwa, P.
Frear, C.
Ha, S.
Li, Chun-Zhu
Garcia-Perez, M.
author_facet Liaw, S.
Wang, Z.
Ndegwa, P.
Frear, C.
Ha, S.
Li, Chun-Zhu
Garcia-Perez, M.
author_sort Liaw, S.
building Curtin Institutional Repository
collection Online Access
description This paper reports the effect of pyrolysis temperature on the yield and composition of bio-oils obtained from the auger pyrolysis of Douglas Fir wood. The tests were conducted at reactor wall temperatures between 200 and 600 °C. Due to the relatively low heat transfer rates achieved between the reactor wall and the biomass particles, the temperature of the solid residue obtained was much lower (between 117 and 420 °C). Bio-oil yields were close (maximum yield: 59 mass%) to those reported for fluidized bed reactors (more than 60 mass%). The maximum oil yield was obtained at a reactor wall temperature of 500 °C (biomass residue heated up to 328 °C). At this temperature, maximum yields of Douglas Fir primary degradation products (lignin oligomers, anhydrosugars, 2-furaldehyde, 2(5H)-furanone, 2-furanmethanol, β-methoxy-(S)- and alkylated and methoxylated phenols) were observed. The yield of products from secondary thermochemical reactions (phenol; phenol, 4-ethyl, O-cresol; phenol, 3,4-dimethyl; cresol; pyrotechol, and phenol 2,4-dimethyl, methanol and gases) increased with temperature. In all cases, the yield of the products from secondary reactions was higher than those reported for fluidized bed reactors at comparable temperatures. The water yield (11 mass%) obtained with the auger reactor was comparable to those reported for other materials processed in fluidized bed reactors. The results obtained confirm that the auger reactor is able to achieve good yields of both bio-oil and bio-char but that the overall composition of the oil obtained will be affected by the slower heating rates achieved and the intensification of secondary reactions in gas phase.
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spelling curtin-20.500.11937-466672017-09-13T14:08:48Z Effect of pyrolysis temperature on the yield and properties of bio-oils obtained from the auger pyrolysis of Douglas Fir wood Liaw, S. Wang, Z. Ndegwa, P. Frear, C. Ha, S. Li, Chun-Zhu Garcia-Perez, M. This paper reports the effect of pyrolysis temperature on the yield and composition of bio-oils obtained from the auger pyrolysis of Douglas Fir wood. The tests were conducted at reactor wall temperatures between 200 and 600 °C. Due to the relatively low heat transfer rates achieved between the reactor wall and the biomass particles, the temperature of the solid residue obtained was much lower (between 117 and 420 °C). Bio-oil yields were close (maximum yield: 59 mass%) to those reported for fluidized bed reactors (more than 60 mass%). The maximum oil yield was obtained at a reactor wall temperature of 500 °C (biomass residue heated up to 328 °C). At this temperature, maximum yields of Douglas Fir primary degradation products (lignin oligomers, anhydrosugars, 2-furaldehyde, 2(5H)-furanone, 2-furanmethanol, β-methoxy-(S)- and alkylated and methoxylated phenols) were observed. The yield of products from secondary thermochemical reactions (phenol; phenol, 4-ethyl, O-cresol; phenol, 3,4-dimethyl; cresol; pyrotechol, and phenol 2,4-dimethyl, methanol and gases) increased with temperature. In all cases, the yield of the products from secondary reactions was higher than those reported for fluidized bed reactors at comparable temperatures. The water yield (11 mass%) obtained with the auger reactor was comparable to those reported for other materials processed in fluidized bed reactors. The results obtained confirm that the auger reactor is able to achieve good yields of both bio-oil and bio-char but that the overall composition of the oil obtained will be affected by the slower heating rates achieved and the intensification of secondary reactions in gas phase. 2012 Journal Article http://hdl.handle.net/20.500.11937/46667 10.1016/j.jaap.2011.09.011 Elsevier restricted
spellingShingle Liaw, S.
Wang, Z.
Ndegwa, P.
Frear, C.
Ha, S.
Li, Chun-Zhu
Garcia-Perez, M.
Effect of pyrolysis temperature on the yield and properties of bio-oils obtained from the auger pyrolysis of Douglas Fir wood
title Effect of pyrolysis temperature on the yield and properties of bio-oils obtained from the auger pyrolysis of Douglas Fir wood
title_full Effect of pyrolysis temperature on the yield and properties of bio-oils obtained from the auger pyrolysis of Douglas Fir wood
title_fullStr Effect of pyrolysis temperature on the yield and properties of bio-oils obtained from the auger pyrolysis of Douglas Fir wood
title_full_unstemmed Effect of pyrolysis temperature on the yield and properties of bio-oils obtained from the auger pyrolysis of Douglas Fir wood
title_short Effect of pyrolysis temperature on the yield and properties of bio-oils obtained from the auger pyrolysis of Douglas Fir wood
title_sort effect of pyrolysis temperature on the yield and properties of bio-oils obtained from the auger pyrolysis of douglas fir wood
url http://hdl.handle.net/20.500.11937/46667