Research article Special Issues

Qualitative and kinetic analysis of torrefaction of lignocellulosic biomass using DSC-TGA-FTIR

  • Received: 28 June 2015 Accepted: 01 November 2015 Published: 12 November 2015
  • Torrefaction is a thermochemical conversion technique to improve the fuel properties of lignocellulosic biomass by treating at temperature 200 ℃-300 ℃ in the minimum oxygen environment for a reasonable residence time. In this study, thermal decomposition and thermal activities of miscanthus and wheat straw during the torrefaction at 200 ℃, 275 ℃, and 300 ℃ in a nitrogen environment for 45 minutes of residence time are analyzed in a simultaneous thermogravimetric analyzer (micro TGA) with a differential scanning calorimetry (DSC), and a macro-TGA. The output of the micro TGA is fed into the Fourier transform infrared spectrometry (FTIR) and qualitative analysis of the gaseous product is carried out. The composition of different gas products during the torrefaction of biomass are compared critically and kinetics were analyzed. It is found that the weight loss due to degradation of initial biomass in second stage (torrefaction process) is a much faster conversion process than the weight loss process in the first stage (drying process). The weight loss of biomass increases with increase in the residence time and torrefaction treatment temperatures. The yield after torrefaction is a solid bio-coal product. The torrefied product were less reactive and has nearly 25% better heating value than the raw biomass. Between the two feedstocks studied, torrefied miscanthus proved to be a more stable fuel than the torrefied wheat straw. The major gaseous components observed during torrefaction are water, carbon dioxide, carbon monoxide, 1,2-Dibromethylene.

    Citation: Bimal Acharya, Ranjan R. Pradhan, Animesh Dutta. Qualitative and kinetic analysis of torrefaction of lignocellulosic biomass using DSC-TGA-FTIR[J]. AIMS Energy, 2015, 3(4): 760-773. doi: 10.3934/energy.2015.4.760

    Related Papers:

  • Torrefaction is a thermochemical conversion technique to improve the fuel properties of lignocellulosic biomass by treating at temperature 200 ℃-300 ℃ in the minimum oxygen environment for a reasonable residence time. In this study, thermal decomposition and thermal activities of miscanthus and wheat straw during the torrefaction at 200 ℃, 275 ℃, and 300 ℃ in a nitrogen environment for 45 minutes of residence time are analyzed in a simultaneous thermogravimetric analyzer (micro TGA) with a differential scanning calorimetry (DSC), and a macro-TGA. The output of the micro TGA is fed into the Fourier transform infrared spectrometry (FTIR) and qualitative analysis of the gaseous product is carried out. The composition of different gas products during the torrefaction of biomass are compared critically and kinetics were analyzed. It is found that the weight loss due to degradation of initial biomass in second stage (torrefaction process) is a much faster conversion process than the weight loss process in the first stage (drying process). The weight loss of biomass increases with increase in the residence time and torrefaction treatment temperatures. The yield after torrefaction is a solid bio-coal product. The torrefied product were less reactive and has nearly 25% better heating value than the raw biomass. Between the two feedstocks studied, torrefied miscanthus proved to be a more stable fuel than the torrefied wheat straw. The major gaseous components observed during torrefaction are water, carbon dioxide, carbon monoxide, 1,2-Dibromethylene.


    加载中
    [1] Wood SM, Layzell DB (2003) A Canadian biomass inventory: feedstocks for a bio-based economy. BIOCAP canada foundation: 18-24.
    [2] Acharya B, Sule I, Dutta A (2012) A review on advances of torrefaction technologies for biomass processing. Biomass conversion biorefinery 2: 349-369. doi: 10.1007/s13399-012-0058-y
    [3] Bergman PCA, Boersma AR, Zwart RWH, et al. (2005) Torrefaction for biomass co-firing in existing coal-fired power stations. Report ECN-C-05-013, ECN, Petten, Netherlands.
    [4] Repellin V, Govin A, Rolland M, et al. (2010) Energy requirement for fine grinding of torrefied wood. Biomass bioenerg 34: 923-930 doi: 10.1016/j.biombioe.2010.01.039
    [5] Bridgeman TG, Jones JM, Shield I, et al. (2008) Torrefaction of reed canary grass, wheat straw and willow to enhance solid fuel qualities and combustion properties. Fuel 87: 844-856. doi: 10.1016/j.fuel.2007.05.041
    [6] Acharya B (2013) Torrefaction and Pelletization of Different Forms of Biomass of Ontario MASc thesis, University of Guelph, Canada. Available from: https://dspace.lib.uoguelph.ca/xmlui/handle/10214/6608.
    [7] Acharya B, Dutta A (2013) Characterization of Torrefied Willow for Combustion Application. J biobased mater bioenergy 7: 667-674. doi: 10.1166/jbmb.2013.1372
    [8] Tumuluru JS, Wright CT, Hess JR, et al. (2011) A review of biomass densification systems to develop uniform feedstock commodities for bioenergy application. Biofuels, bioprod biorefin 5: 683-707.
    [9] Tapasvi D, Khalil R, Skreiberg O, et al. (2012) Torrefaction of Norwegian birch and spruce: an experimental study using macro-TGA. Energy fuel 26: 5232-5240. doi: 10.1021/ef300993q
    [10] Medic D (2012) Investigation of torrefaction process parameters and characterization of torrefied biomass. PhD thesis, Iowa State University, USA. Available from: http://lib.dr.iastate.edu/etd/12403/.
    [11] Bradbury AG, Sakai Y, Shafizadeh F (1979) A kinetic model for pyrolysis of cellulose. J appl polymer sci 23: 3271-3280. doi: 10.1002/app.1979.070231112
    [12] Di Blasi C, Lanzetta M (1997) Intrinsic kinetics of isothermal xylan degradation in inert atmosphere. J analyt appl pyroly 40-41: 287-303. doi: 10.1016/S0165-2370(97)00028-4
    [13] Prins MJ, Ptasinski KJ, Janssen FJ (2006) More efficient biomass gasification via torrefaction. Energy 31: 3458-3470. doi: 10.1016/j.energy.2006.03.008
    [14] Nocquet T, Dupont C, Commandré JM, et al. (2011) Study on mass loss and gas release during torrefaction of woody biomass and its constituents for injection in entrained flow gasifier. In: 3rd International Congress on Green Process Engineering, Kuala-Lumpur.
    [15] Shang L, Ahrenfeldt J, Holm JK, et al. (2013) Intrinsic kinetics and devolatilization of wheat straw during torrefaction. J anal appl pyrolysis 100: 145-152. doi: 10.1016/j.jaap.2012.12.010
    [16] Funke A, Ziegler F (2010) Hydrothermal carbonization of biomass: A summary and discussion of chemical mechanisms for process engineering. Biofuel bioprod biorefin 4: 160-177. doi: 10.1002/bbb.198
    [17] Eseltine D, Thanapal SS, Annamalai K, et al. (2013) Torrefaction of woody biomass (Juniper and Mesquite) using inert and non-inert gases. Fuel 113: 379-388. doi: 10.1016/j.fuel.2013.04.085
    [18] Sule I (2012) Torrefaction Behaviour of Agricultural Biomass, M.A.Sc. dissertation, University of Guelph, ON, Canada.
  • Reader Comments
  • © 2015 the Author(s), licensee AIMS Press. This is an open access article distributed under the terms of the Creative Commons Attribution License (http://creativecommons.org/licenses/by/4.0)
通讯作者: 陈斌, bchen63@163.com
  • 1. 

    沈阳化工大学材料科学与工程学院 沈阳 110142

  1. 本站搜索
  2. 百度学术搜索
  3. 万方数据库搜索
  4. CNKI搜索

Metrics

Article views(7020) PDF downloads(1367) Cited by(15)

Article outline

Figures and Tables

Figures(10)  /  Tables(4)

Other Articles By Authors

/

DownLoad:  Full-Size Img  PowerPoint
Return
Return

Catalog