Simulation Model of Pyrolysis Biofuel Yield Based on Algal Components and Pyrolysis Kinetics
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  • 作者:Xiaoyi Yang (1)
    Xin Wang (1)
    Bingwei Zhao (1)
    Ya Li (1)
  • 关键词:Algal biomass ; Kinetics ; Biofuel yield model ; Pyrolysis biofuel
  • 刊名:BioEnergy Research
  • 出版年:2014
  • 出版时间:December 2014
  • 年:2014
  • 卷:7
  • 期:4
  • 页码:1293-1304
  • 全文大小:832 KB
  • 参考文献:1. Mackinnon L, Clint W (2010) Algae-Based Biofuels. Navigant Research Web. http://www.navigantresearch.com/wordpress/wp-content/uploads/2010/10/ABBF-10-Executive-Summary.pdf
    2. Li DM, Chen LM, Yi XJ, Zhang XW, Ye NH (2010) Pyrolytic characteristics and kinetics of two brown algae and sodium alginate. Bioresour Technol 101:7131-136 CrossRef
    3. Zou SP, Wu YL, Yang MD, Li C, Tong JM (2010) Pyrolysis characteristics and kinetics of the marine microalgae / Dunaliella tertiolecta using thermogravimetric analyzer. Bioresour Technol 101:359-65 CrossRef
    4. Li DM, Chen LM, Zhang XW, Ye NH, Xing FG (2011) Pyrolytic characteristics and kinetic studies of three kinds of red algae. Biomass Bioenergy 35:1765-772 CrossRef
    5. Kawnish K, Sankar B (2012) Application of the distributed activation energy model to the kinetic study of pyrolysis of the fresh water algae / Chlorococcum humicola. Bioresour Technol 107:476-81 CrossRef
    6. Colomba DB (2008) Modeling chemical and physical processes of wood and biomass pyrolysis. Prog Energy Combust Sci 34:47-0 CrossRef
    7. Daniel N, Henrik T, Arlindo M, Luis T, Alberto G (2011) Characterization and prediction of biomass pyrolysis products. Prog Energy Combust Sci 37:611-30 CrossRef
    8. Yang XY, Jiang ZP (2009) Kinetic studies of overlapping pyrolysis reactions in industrial waste activated sludge. Bioresour Technol 100:3663-668 CrossRef
    9. Antonio P, Pedro ES, Jose MC, Luis AP (2011) Kinetic analysis of complex solid-state reactions. A new deconvolution procedure. J Phys Chem B 115:1780-791 CrossRef
    10. Arenillas A, Cuervo S, Dom??nguez A, Menéndez JA, Rubiera F, Parra JB, Merino C, Pis JJ (2004) Effects of oxidative treatments with air and CO2 on vapour grown carbon nanofibres (VGCNFs) produced at industrial scale. Thermochim Acta 423:99-06 CrossRef
    11. Wang B, Sun LS, Su S, Xiang J, Hu S, Fei H (2012) Char structural evolution during pyrolysis and its influence on combustion reactivity in air and oxy-fuel conditions. Energy Fuels 26:1565-574 CrossRef
    12. Alejandrina C, Rachel M, Michael PH, David CG, Norman MW, Robert SW (2012) Thermolysis of microalgae and duckweed in a CO2-swept fixed-bed reactor: bio-oil yield and compositional effects. Bioresour Technol 109:154-62 CrossRef
    13. Derek RV, Brajendra KS, Grant VB, Kishore R, Timothy JS (2012) Thermochemical conversion of raw and defatted algal biomass via hydrothermal liquefaction and slow pyrolysis. Bioresour Technol 109:178-87 CrossRef
    14. Umakanta J, Das KC (2011) Comparative evaluation of thermochemical liquefaction and pyrolysis for bio-oil production from microalgae. Energy Fuels 25:5472-482 CrossRef
    15. Yang WY, Zeng Y, Luo J, Tong DM, Qing RW, Fan Y, Hu CW (2011) Production of bio-oil by direct and catalytic pyrolysis of / Nannochloropsis sp. J Fuel Chem Technol 39:664-69
    16. Babich IV, van der Hulst M, Lefferts L, Moulijn JA, O’Connor P, Seshan K (2011) Catalytic pyrolysis of microalgae to high-quality liquid bio-fuels. Biomass Bioenergy 35:3199-207 CrossRef
  • 作者单位:Xiaoyi Yang (1)
    Xin Wang (1)
    Bingwei Zhao (1)
    Ya Li (1)

    1. School of Energy and Power Engineering, Energy and Environment International Center, Beihang University, 37 Xueyuan Rd., Haidian District, Beijing, People’s Republic of China
  • ISSN:1939-1242
文摘
Yield and composition of pyrolysis oil were tested by fixed bed pyrolysis reactor and GC-MS. Algae pyrolysis kinetics was also calculated by Lorentzian fitting multi-heating rate method with R 2--.98. Their activation energy was ranged from 94 to 216?kJ/mol and most of fitting peaks could be described by the random nucleation followed by growth mechanism. Higher bio-oil yield of 35.0?% for Chlorella biomass and 40.6?% for Spirulina biomass at 425?°C have been obtained, while it is 49.4?% at 450?°C for Chrysophyceae biomass. The main compounds of pyrolysis oil included aliphatic and alicyclic hydrocarbons, aromatic hydrocarbons, nitrogenated compounds (nitriles, amines, amines, and N-heterocyclic compounds), carboxylic acids, ketones, alcohols, furans, phenols, ester, and others. Carbon number distribution of bio-oil is similar to that of gasoline and diesel, and fatty acid has an influence on bio-oil carbon distribution. Components biofuel model based on algal biomass component was established and the difference between simulated value and experiment value is less 3.58?%. Kinetics biofuel model based on fitting peak areas in pyrolysis kinetics was established and the difference between simulated value and experiment value is less 3.45?%. Pyrolysis oil yield can be quickly and efficiently achieved with these two models.

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