Regimes of Nonpremixed Combustion of Hot Low-Calorific-Value Gases Derived from Biomass Gasification

被引:24
|
作者
Kwiatkowski, Kamil [1 ,2 ]
Mastorakos, Epaminondas [3 ]
机构
[1] Univ Warsaw, Inst Theoret Phys, Fac Phys, Pasteura 5, PL-02093 Warsaw, Poland
[2] Univ Warsaw, Interdisciplinary Ctr Math & Computat Modelling, Prosta 69, PL-00838 Warsaw, Poland
[3] Univ Cambridge, Dept Engn, Hopkinson Lab, Trumpington St, Cambridge CB2 1PZ, England
关键词
MILD COMBUSTION; UPDRAFT GASIFICATION; REACTION ZONE; NATURAL-GAS; JET FLAMES; TEMPERATURE; TECHNOLOGIES; SIMULATIONS; FEATHERS; DILUTION;
D O I
10.1021/acs.energyfuels.5b02580
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Combustion of the hot, diluted gases derived from biomass gasification was investigated in mixture fraction space. The composition of the fuels corresponds to those measured in industrial gasification plants operated on wood chips and organic residuals. The temperatures of both the fuel and the oxidizer are within the range accessible to gasifiers which naturally produce hot gases. Simulations of counterflow laminar nonpremixed flames show that only the maximum temperatures and temperature profiles of the biomass syngases are comparable to those obtained for methane diluted with nitrogen to the same calorific value. In contrast, the profiles of the heat release rate (HRR) are significantly different, being widely spread across the mixture fraction space when syngas is burning but with a narrow distribution for the methane equivalent. There are also differences in profiles of OH, important from an experimental point of view. From this perspective, methane equivalents cannot be treated as an analog of real biomass-derived gases. Wood-derived gases are generally burned conventionally or, when both reactants are highly preheated, in the high-temperature air combustion (HTAC) regime. Lower calorific-value gases derived from organic residuals are most commonly burned in pilot-assisted regimes, but the favorable regime of moderate and/or intense level of dilution (MILD) can be achieved when the reactants are sufficiently preheated. Moreover, even when the oxidizer is cold, highly diluted and preheated residual-derived gases can be burned within the MILD combustion regime. Wood-derived gases typically do not achieve MILD combustion, even when additional exhaust gas recirculation (EGR) is introduced or when the scalar dissipation rate (SDR) is increased. Although based on the simplified mixture-fraction approach, a survey of the combustion regimes qualitatively agrees with the properties of the combustion processes observed in industrial gasification plants. Gases from wood chips are burned conventionally, whereas less calorific-value gases derived from organic residuals achieve MILD combustion for three different geometrical configurations of the industrial combustion.
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页码:4386 / 4397
页数:12
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共 45 条
  • [1] Clean and efficient combustion of simulated low-calorific-value gases in swirl burner/furnace systems
    Fick, W
    Syred, N
    Klinge, T
    Griffiths, AJ
    O'doherty, T
    JOURNAL OF THE INSTITUTE OF ENERGY, 1998, 71 (486): : 12 - 20
  • [2] MILD combustion of low calorific value gases
    Zhou, Shengquan
    Yan, Beibei
    Mansour, Mohy
    Li, Zhongshan
    Cheng, Zhanjun
    Tao, Junyu
    Chen, Guanyi
    Bai, Xue-Song
    PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2024, 104
  • [3] FLAME STRUCTURE OF ATTACHED AND LIFTED JET FLAMES OF LOW-CALORIFIC-VALUE GASES
    GOLLAHALLI, SR
    ZADEH, GK
    ENERGY SOURCES, 1985, 8 (01): : 43 - 66
  • [4] Combustion of Low-Calorific-Value Fuels in Fluidized-Bed Furnaces.
    Langer, Karl
    Berg- und Huettenmaennische Monatshefte, 1988, 133 (01): : 95 - 100
  • [5] Combustion of low calorific value gases in porous burners
    Verbrennung von niederkalorischen Gasen in Porenbrennern
    Diezinger, S. (sdiez@lstm.uni-erlangen.de), 2005, Vulkan Verlag GmbH (54):
  • [6] COMBUSTION OF LOW CALORIFIC VALUE GASES - PROBLEMS AND PROSPECTS
    CHOMIAK, J
    LONGWELL, JP
    SAROFIM, AF
    PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 1989, 15 (02) : 109 - 129
  • [7] Tars and the combustion of biomass derived low calorific value gas in a gas turbine combustor
    Van Der Wel, M.
    De Jong, W.
    Spliethoff, H.
    VDI Berichte, 2003, (1750): : 187 - 193
  • [9] REVIEW OF COMBUSTION PROBLEMS ASSOCIATED WITH LOW CALORIFIC VALUE GASES
    SYRED, N
    DAHMEN, KR
    STYLES, AC
    NAJIM, SA
    JOURNAL OF THE INSTITUTE OF FUEL, 1977, 50 (405): : 195 - 207
  • [10] Combustion of Low Calorific Value Gases in Gas Turbines.
    Odgers, J.
    Kretschmer, D.
    Entropie Paris, 1985, 22 (130-131): : 144 - 150