CH4/O2/CO2预混体系爆炸动力学研究

钟飞翔 郑立刚 马鸿雁 杜德朋 王玺 潘荣锟

钟飞翔, 郑立刚, 马鸿雁, 杜德朋, 王玺, 潘荣锟. CH4/O2/CO2预混体系爆炸动力学研究[J]. 爆炸与冲击, 2022, 42(1): 012101. doi: 10.11883/bzycj-2021-0191
引用本文: 钟飞翔, 郑立刚, 马鸿雁, 杜德朋, 王玺, 潘荣锟. CH4/O2/CO2预混体系爆炸动力学研究[J]. 爆炸与冲击, 2022, 42(1): 012101. doi: 10.11883/bzycj-2021-0191
ZHONG Feixiang, ZHENG Ligang, MA Hongyan, DU Depeng, WANG Xi, PAN Rongkun. A study of explosion dynamics of a CH4/O2/CO2 premixed system[J]. Explosion And Shock Waves, 2022, 42(1): 012101. doi: 10.11883/bzycj-2021-0191
Citation: ZHONG Feixiang, ZHENG Ligang, MA Hongyan, DU Depeng, WANG Xi, PAN Rongkun. A study of explosion dynamics of a CH4/O2/CO2 premixed system[J]. Explosion And Shock Waves, 2022, 42(1): 012101. doi: 10.11883/bzycj-2021-0191

CH4/O2/CO2预混体系爆炸动力学研究

doi: 10.11883/bzycj-2021-0191
基金项目: 国家自然科学基金(51674104,51874120)
详细信息
    作者简介:

    钟飞翔(1996- ),男,硕士研究生,390057630@qq.com

    通讯作者:

    郑立刚(1979- ),男,博士,教授,zhengligang97@163.com

  • 中图分类号: O381

A study of explosion dynamics of a CH4/O2/CO2 premixed system

  • 摘要: 为探究甲烷在富氧条件下的火焰动力学规律,以CH4/O2/CO2预混体系为研究对象,在小尺度方形透明管道中进行了一系列爆炸实验,探讨了初始环境温度波动对爆炸参数的影响,并对预混体系的燃烧机理进行分析。结果表明:在273 K的环境温度下,化学当量比$\varphi $=0.8~1.0且氧气相对比γ<0.30和$\varphi $=1.2且γ<0.35的预混体系不能被点燃,而其他预混体系均可被点燃,最终产生郁金香与非郁金香两种火焰类型,并且根据郁金香火焰独特的演变特征,又划分为T形郁金香火焰和不对称郁金香火焰;随着γ的增大,无量纲火焰传播速度v/(SLσ)的变化趋势由“两升两降”转变为“一升一降”。初始环境温度的升高并未对火焰传播速度和爆炸超压的变化趋势产生影响,但是会导致最大爆炸超压pmax和最大火焰传播速度降低。值得注意的是,初始环境温度对爆炸强度的影响随化学当量比的减小而增强。另外,与最大爆炸超压相比,最大火焰传播速度与层流燃烧速度之间的关系更紧密。从敏感性分析中可知:层流燃烧速度对自由基链式反应R38(即H+O2=O+OH)表现出最大的正敏感度,对R52(即H+CH3 (+M)=CH4 (+M))表现出最大的负敏感度,并且对自由基OH的生成速率最敏感,当初始环境温度升高至303 K时,层流燃烧速度对R38(正)和R52(负)的敏感度降低;H、O和OH自由基总摩尔分数的增大会削弱热扩散的不稳定性,增强流体力学的不稳定性。
  • 图  1  实验装置

    Figure  1.  Experimental facility

    图  2  火焰状态统计

    Figure  2.  Statistics of flame status

    图  3  郁金香火焰的3种演变模式

    Figure  3.  Three patterns of evolution process of tulip flames

    图  4  Lewis数和σ/δγ的变化趋势

    Figure  4.  Variation of Lewis number and σ/δ with γ

    图  5  归一化火焰传播速度与火焰前锋位置之间的关系

    Figure  5.  Relation between the normalized flame propagation velocity and the flame front position

    图  6  当量比为0.8时各氧气相对比下爆炸超压曲线

    Figure  6.  Explosion overpressure-time history for various oxygen fractions at $\varphi $=0.8

    图  7  最大爆炸超压和最大火焰传播速度与层流燃烧速度之间的关系

    Figure  7.  Dependence of the maximum explosion overpressure and the maximum flame propagation velocity on laminar burning velocity

    图  8  不同初始环境温度对pmax${\bar v_{{\text{max}}}} $的影响

    Figure  8.  Influence of different initial ambient temperatures on pmax and $ {\bar v_{{\text{max}}}} $

    图  9  2种初始环境温度下(dp/dt)maxSLσ2(σ−1)/(σ+1)的关系

    Figure  9.  Relationship between (dp/dt) max and SLσ2(σ−1)/(σ+1) for two initial ambient temperatures

    图  10  各种氧气相对比下主要链式反应对层流燃烧速度的敏感度系数

    Figure  10.  Sensitivity coefficients of the main chain reactions to laminar burning velocity for various oxygen fractions

    图  11  不同初始环境温度下OH自由基的生成速率

    Figure  11.  Rates of production of the free radical OH at different initial ambient temperatures

    图  12  层流燃烧速度和膨胀比随自由基OH的生成速率变化

    Figure  12.  Variation of laminar burning velocity and expansion ratio with the rate of production of OH free radical

    图  13  火焰不稳定与H、O、OH自由基最大摩尔分数的拟合关系

    Figure  13.  Fitting relationship between the flame instability and the maximum mole fraction of H, O and OH radicals

    表  1  临界未点火预混体系甲烷体积分数

    Table  1.   Critical volume fractions of methane in unignited premixed systems

    气体组分临界未点火预混体系甲烷体积分数/%
    $\varphi $ =0.8, γ =0.25$\varphi $ =1.0, γ =0.25$\varphi $ =1.2, γ =0.30
    O222.7322.2225.43
    CH4 9.0911.1115.26
    下载: 导出CSV

    表  2  $p_{\max} $$ {\bar v_{{\text{max}}}} $在环境温度由$273\;{\rm{K}} $升高到$303\;{\rm{K}} $影响下的下降百分比

    Table  2.   Decrease percentage of pmax and $ {\bar v_{{\text{max}}}} $ affected by ambient temperature from $273\;{\rm{K}} $ to $303\;{\rm{K}} $

    γpmax下降百分比/% $ {\bar v_{{\text{max}}}} $下降百分比/%
    $\varphi $=0.8$\varphi $=1.0$\varphi $=1.2$\varphi $=0.8$\varphi $=1.0$\varphi $=1.2
    0.3021.9431.16 32.3330.76
    0.3543.3838.8216.43 29.8130.9530.32
    0.4034.0631.23 4.77 49.5440.56 8.65
    0.4534.6622.4510.05 41.7617.0810.03
    0.5026.3027.9414.56 14.0210.07 8.67
    下载: 导出CSV

    表  3  预混体系中主要的链式反应

    Table  3.   Main chain reactions in the premixed system

    反应序号主要链式反应反应序号主要链式反应
    R11O+CH4=OH+CH3R98OH+CH4=CH3+H2O
    R38H+O2=O+OHR99OH+CO=H+CO2
    R43H+OH+M=H2O+MR119HO2+CH3=OH+CH3O
    R45H+H2O=H2+OHR135CH2+O2=OH+H+CO
    R52H+CH3 (+M)=CH4 (+M)R153CH2(s)+CO2=CH2O+CO
    R53H+CH4=CH3+H2R166HCO+H2O=H+CO+H2O
    下载: 导出CSV
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出版历程
  • 收稿日期:  2021-05-14
  • 修回日期:  2021-08-23
  • 网络出版日期:  2021-12-01
  • 刊出日期:  2022-01-20

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