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Method of choosing optimal composition of biomass mixtures

Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
Biomass has high content of volatile matter, hence devolatilization process is rapid. Necessity of supplying high fluxes of combustion air is usually one of the factor which leads to high values of air excess ratio and, as a consequence to decrease of energy efficiency. However it is possible to use mixture of different sorts of biomasses and thus obtain fuel which might equalize devolatilization rate. In this paper procedure for choosing optimal mixture of given sorts of biomasses based on their composition is presented. First, pyrolysis process of hemicellulose, cellulose and lignin was conducted using thermobalance. Based on the results and assuming that there are no interactions between pure components, optimal composition of the mixture were calculated. In the next step, according to obtained optimal composition, proportions of oak, pine, rape straw and wheat straw were calculated. Finally, pyrolysis of selected biomass mixtures was carried out. It was found that due to the presence of cellulose, which decomposes in very narrow temperature range, all of mixtures are characterized by the devolatilization with local maximum occurring at the temperature around 350°C.
Słowa kluczowe
Rocznik
Strony
27—34
Opis fizyczny
Bibliogr. 21 poz., rys., tab.
Twórcy
  • Silesian University of Technology Institute of Thermal Technology Konarskiego 22, Gliwice 44 - 100, Poland, tel.: +48 32 237 23 40; fax: +48 32 237 28 72
autor
  • Silesian University of Technology Institute of Thermal Technology Konarskiego 22, Gliwice 44 - 100, Poland, tel.: +48 32 237 23 40; fax: +48 32 237 28 72
autor
  • Silesian University of Technology Institute of Thermal Technology Konarskiego 22, Gliwice 44 - 100, Poland, tel.: +48 32 237 23 40; fax: +48 32 237 28 72
Bibliografia
  • [1] Raveendran K., Ganesh A., Khilar K. C.: Pyrolysis characteristics of biomass and biomass components. Fuel 75 No.8, (1996), pp. 987-998;
  • [2] Sharma A. K., Ravi M. R., Kohli S.: Modelling Product Composition in Slow Pyrolysis of Wood. SESI Journal, 16(1), (2006), pp.1-11;
  • [3] Biagini E., Barontini F., Tognotti L.: Devolatilization of Biomass Fuels and Biomass Components Studied by TG-FTIR Technique. Industrial & Engineering Chemistry Research, 45, (2006), pp. 4486-4493;
  • [4] Bernhard P.: Prediction of pyrolysis of pistachio shells based on its components hemicellulose, cellulose and lignin. Fuel Processing Technology, 92, (2011), pp. 1993-1998;
  • [5] Rao T. R., Sharma A.: Pyrolysis rates of biomass materials. Energy, 23, Issue 11, (1998), pp. 973–978;
  • [6] Yang H., Yan R., Chen H., Zheng C., Lee D. H., Liang D. T.: In-Depth Investigation of Biomass Pyrolysis Based on Three Major Components: Hemicellulose, Cellulose and Lignin. Energy &Fuels, 20, (2006), pp. 388-393;
  • [7] Wang S., Guo X., Wang K., Luo Z.: Influence of the interaction of components on the pyrolysis behavior of biomass. Journal of Analytical and Applied Pyrolysis, 91 (1), (2011), pp. 183-189;
  • [8] Couhert C., Commandre J.M., Salvado S.: Is it possible to predict gas yields of any biomass after rapid pyrolysis at high temperature from its composition in cellulose, hemicellulose and lignin? Fuel, 88, (2009), pp. 408–417;
  • [9] Giudicianni P., Cardone G., Ragucci R., Cellulose, hemicellulose and lignin slow steam pyrolysis: Thermal decomposition of biomass components mixtures. Journal of Analytical and Applied Pyrolysis, 100, (2013), pp. 213-222;
  • [10] Liu Q., Zhong Z., Wang S., Luo Z.: Interactions of biomass components during pyrolysis: A TG-FTIR study. Journal of Analytical and Applied Pyrolysis, 90, (2011), pp. 213-218;
  • [11] Hosoya T., Kawamoto H., Saka S.: Cellulose-hemicellulose and cellulose-lignin interactions in wood pyrolysis at gasification temperature. Journal of Analytical and Applied Pyrolysis, 80, (2007), pp. 118- 125;
  • [12] Worasuwannarak N., Sonobe T., Tanthapanichakoon W.: Pyrolysis behaviours of rice straw, rice husk, and corncob by TG-MS technique. Journal of Analytical and Applied Pyrolysis, 78, (2007), pp. 265-271
  • [13] Han L., Wang Q. H., Ma Q. A., Yu C. J., Luo Z. Y., Cen K. F.: Influence of CaO additives on wheatstraw pyrolysis as determined by TG-FTIR analysis. Journal of Analytical and Applied Pyrolysis, 88, (2010), pp. 199-206;
  • [14] Eom I. Y., Kim J. Y., Kim T. S., Lee S. M., Choi D., Choid I. G., Choi J.: Effect of essential inorganic metals on primary thermal degradation of lignocellulosic biomass. Bioresource Technology, 104, (2012), pp. 687–694;
  • [15] Yang H., Yan R., Chen H., Zheng C., Lee D. H., Liang D. T.: Influence of mineral matter on pyrolysis of palm oil wastes. Combustion and Flame, 146, (2006), pp. 605-611;
  • [16] Bibrzycki J., Katelbach-Woźniak A., Niestrój M., Szlęk A.: Badania procesu rozkładu termicznego podstawowych substancji organicznych biomasy. Archiwum Spalania, 12, No 1-2, (2012), pp. 39-45, ISSN 1641-8549;
  • [17] Wang D., Xiao R., Zhang H., He G.: Comparison of catalytic pyrolysis of biomass with MCM-41 and CaO catalysts by using TGA-FTIR analysis. Journal of Analytical and Applied Pyrolysis, 89 (2), (2010), pp. 171-177;
  • [18] Patwardhan P. R., Satrio J. A., Brown R. C., Shanks B. H.: Influence of inorganic salts on the primary pyrolysis products of cellulose. Biosource Technology, 101, (2010), pp. 4646–4655;
  • [19] Jeguirim M., Limousy L., Dutournie P.: Pyrolysis kinetics and physicochemical properties of agropellets produced from spent ground coffee blended with conventional biomass. Chemical Engineering Research and Design (2014)
  • [20] DOI: 10.1016/j.cherd.2014.04.018
  • [21] Vassilev S.V., Baxter D., Andersen L.K., Vassileva C.G., Morgan T.J.: An overview of the organic and inorganic phase composition of biomass. Fuel 94, (2012), pp. 1-33.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-a4e651ad-05e7-4eb0-a566-5ecd7a2eb7f5
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