高温条件下低浓度瓦斯氧化反应动力学特性研究
Study on the Kinetic Characteristics of Gas Oxidation Reaction under Low Concentration under High Temperature
DOI: 10.12677/me.2026.142048, PDF,    国家自然科学基金支持
作者: 郭玉印:济宁市金桥煤矿,山东 济宁;王 栋:济宁市煤矿安全生产监测监控中心,山东 济宁;巩 超:济宁市金桥煤矿教育培训办公室,山东 济宁;孔维奕, 李凯乐:山东科技大学安全与环境工程学院,山东 青岛;刘述勋:济宁市金桥煤矿通防科,山东 济宁
关键词: 瓦斯爆炸高温条件爆炸压力爆炸温度反应动力学Gas Explosion High-Temperature Conditions Explosion Pressure Explosion Temperature Reaction Kinetics
摘要: 为了研究不同初始温度和不同初始瓦斯浓度对低浓度瓦斯(5%以下)氧化反应特性的影响,本文利用CHEMKIN软件对不同初始条件下的瓦斯氧化反应进行模拟研究。研究结果表明:初始温度升高(1200~1400 K)加速自由基的链式反应,使点火延迟时间缩短92%,最大反应温度上升5%,而最大反应压力下降10%;促进一氧化氮和二氧化氮的生成,最终摩尔分数分别上升21.8%和1.2%,而二氧化碳的最终摩尔分数下降4.6%,同时一氧化碳的最大摩尔分数在0.04上下波动。初始瓦斯浓度升高(1%~5%)增加可燃物总量,使点火延迟时间延长64%,最大反应压力与温度分别上升57.96%和56.91%;促进二氧化碳、一氧化氮和二氧化氮的生成,最终摩尔分数分别上升45%、1.4%、1.6%,而一氧化碳的最大摩尔分数在0.00784~0.0402范围内。表明温度影响氧化反应的反应速率,瓦斯浓度影响能量释放上限。研究提出,实际应用中需平衡温度与瓦斯浓度,优先控制温度阈值以抑制致灾性气体,并通过浓度梯度优化来提升蓄热氧化效率,为低浓度瓦斯的安全利用提供理论支撑。
Abstract: In order to study the effects of different initial temperatures and different initial gas concentrations on the oxidation reaction characteristics of low-concentration gas (below 5%), CHEMKIN software was used to simulate the gas oxidation reaction under different initial conditions in this paper. The results show that the increase of initial temperature (1200~1400 K) accelerates the chain reaction of free radicals, and the ignition delay time is shortened by 92%, the maximum reaction temperature is increased by 5%, and the maximum reaction pressure is decreased by 10%. After promoting the production of nitric oxide and nitrogen dioxide, the final mole fraction increased by 21.8% and 1.2%, respectively, while the final mole fraction of carbon dioxide decreased by 4.6%. At the same time, the maximum mole fraction of carbon monoxide fluctuated around 0.04. The increase of initial gas concentration (1%~5%) increased the total amount of fuel, prolonged the ignition delay time by 64%, and increased the maximum reaction pressure and temperature by 57.96% and 56.91%, respectively. It promoted the production of carbon dioxide, nitric oxide and nitrogen dioxide, and the final mole fraction increased by 45%, 1.4% and 1.6%, respectively, while the maximum mole fraction of carbon monoxide was in the range of 0.00784 to 0.0402. The results show that temperature affects the reaction rate of oxidation reaction and gas concentration affects the upper limit of energy release. It is proposed that in practical application, it is necessary to balance temperature and gas concentration, give priority to controlling the temperature threshold to suppress the disastrous gas, and improve the heat storage and oxidation efficiency through concentration gradient optimization, so as to provide theoretical support for the safe utilization of low-concentration gas.
文章引用:郭玉印, 王栋, 巩超, 孔维奕, 刘述勋, 李凯乐. 高温条件下低浓度瓦斯氧化反应动力学特性研究[J]. 矿山工程, 2026, 14(2): 456-471. https://doi.org/10.12677/me.2026.142048

参考文献

[1] Chen, J.H., Wen, G.C., Yan, S., Lan, X.Y., et al. (2020) Oxidation and Characterization of Low-Concentration Gas in a High-Temperature Reactor. Processes, 8, Article 481.
[2] Li, X.Y., Chen, H.Y., Li, H.X. and Chen, J.H. (2021) Change Law of Lower Limit of Gas Explosion at Ultra-High Temperatures. ACS Omega, 6, 35112-35123.
[3] 柏琳. 丁集煤矿超低浓度瓦斯氧化供热技术应用研究[J]. 煤炭工程, 2020, 52(9): 33-36.
[4] Marín, P., Vega, A., Díez, F.V. and Ordóñez, S. (2020) Control of Regenerative Catalytic Oxidizers Used in Coal Mine Ventilation Air Methane Exploitation. Process Safety and Environmental Protection, 134, 333-342. [Google Scholar] [CrossRef
[5] 陈金华. 低浓度瓦斯蓄热氧化供热系统的应用研究[J]. 矿业安全与环保, 2017, 44(2): 62-65.
[6] 高鹏飞, 孙东玲, 霍春秀, 等. 超低浓度瓦斯蓄热氧化利用技术研究进展[J]. 煤炭科学技术, 2018, 46(12): 67-73.
[7] 吕元. 煤矿通风瓦斯的蓄热氧化处理装置研究[D]: [博士学位论文]. 北京: 中国科学院研究生院(工程热物理研究所), 2012.
[8] 冯长根. 热爆炸理论[M]. 北京: 科学出版社, 1988.
[9] 赵江平, 王振成. 热爆炸理论在粉尘爆炸机理研究中的应用[J]. 中国安全科学学报, 2004, 14(5): 80-83.
[10] Lu, T. and Law, C.K. (2008) A Criterion Based on Computational Singular Perturbation for the Identification of Quasi Steady State Species: A Reduced Mechanism for Methane Oxidation with NO Chemistry. Combustion and Flame, 154, 761-774. [Google Scholar] [CrossRef
[11] 杨龙龙, 刘艳, 杨春丽. 不同湿度和近爆炸下限条件下甲烷-空气混合物爆炸特征[J]. 爆炸与冲击, 2021, 41(2): 166-175.
[12] 梁运涛, 王连聪, 罗海珠, 等. 激波诱导瓦斯爆炸反应动力学计算模型[J]. 煤炭学报, 2017, 42(6): 1475-1481.
[13] 贾进章, 朱金超, 甄纹浩. 乙炔对瓦斯爆炸的化学动力学影响模拟研究[J]. 中国安全科学学报, 2020, 30(9): 29-36.
[14] 李祥春, 聂百胜, 杨春丽, 等. 封闭空间内瓦斯浓度对瓦斯爆炸反应动力学特性的影响[J]. 高压物理学报, 2017, 31(2): 135-147.
[15] 罗振敏, 吴刚. 密闭空间瓦斯爆炸数值模拟研究[J]. 煤矿安全, 2020, 51(2): 1-4.
[16] 李东方, 刘会彩, 张锦. 基于层次分析法的受限空间瓦斯爆炸数值模拟研究[J]. 煤炭技术, 2022, 41(9): 108-111.
[17] 周振兴. 障碍物形状和数量对含尘瓦斯爆炸激励效应影响的数值模拟研究[D]: [硕士学位论文]. 廊坊: 华北科技学院, 2023.
[18] Jiang, B., Lin, B., Shulei, S., Zhu, C., Liu, Q. and Zhai, C. (2012) A Numerical Simulation of the Influence Initial Temperature Has on the Propagation Characteristics Of, and Safe Distance From, a Gas Explosion. International Journal of Mining Science and Technology, 22, 307-310. [Google Scholar] [CrossRef
[19] Van den Schoor, F. and Verplaetsen, F. (2006) The Upper Explosion Limit of Lower Alkanes and Alkenes in Air at Elevated Pressures and Temperatures. Journal of Hazardous Materials, 128, 1-9. [Google Scholar] [CrossRef] [PubMed]
[20] Gao, N. (2013) Effect of Initial Temperature on Free Radicals of Gas Explosion in Restricted Space. Advanced Materials Research, 798, 138-142. [Google Scholar] [CrossRef
[21] Li, C.W., Qiao, Z., Hao, M., et al. (2025) The Variation of Environmental Parameters after Gas Explosion in Semi-Closed Pipeline. Energy Sources, Part A: Recovery, Utilization, and Environmental Effects, 47, 11650-11664. [Google Scholar] [CrossRef
[22] Pekalski, A.A., Schildberg, H.P., Smallegange, P.S.D., Lemkowitz, S.M., Zevenbergen, J.F., Braithwaite, M., et al. (2005) Determination of the Explosion Behaviour of Methane and Propene in Air or Oxygen at Standard and Elevated Conditions. Process Safety and Environmental Protection, 83, 421-429. [Google Scholar] [CrossRef
[23] Gieras, M., Klemens, R., Rarata, G. and Wolański, P. (2006) Determination of Explosion Parameters of Methane-Air Mixtures in the Chamber of 40 dm3 at Normal and Elevated Temperature. Journal of Loss Prevention in the Process Industries, 19, 263-270. [Google Scholar] [CrossRef
[24] Zhang, Z., Lin, B., Li, G. and Ye, Q. (2013) Explosion Pressure Characteristics of Coal Gas. Combustion Science and Technology, 185, 514-531. [Google Scholar] [CrossRef
[25] Ning, J.G., Wang, C. and Lu, J. (2006) Explosion Characteristics of Coal Gas under Various Initial Temperatures and Pressures. Shock Waves, 15, 461-472. [Google Scholar] [CrossRef
[26] Zhian, H., Zhigang, L., Shengguo, C., Yansong, Z. and Yinghua, Z. (2012) Numerical Simulation and Study on the Transmission Law of Flame and Pressure Wave of Pipeline Gas Explosion. Safety Science, 50, 806-810. [Google Scholar] [CrossRef
[27] Niu, Y.H., Shi, B.M. and Jiang, B.Y. (2019) Experimental Study of Overpressure Evolution Laws and Flame Propagation Characteristics after Methane Explosion in Transversal Pipe Networks. Applied Thermal Engineering, 154, 18-23. [Google Scholar] [CrossRef
[28] Gao, K., Liu, Z., Wu, C., Li, J., Liu, K., Liu, Y., et al. (2021) Effect of Low Gas Concentration in Underground Return Tunnels on Characteristics of Gas Explosions. Process Safety and Environmental Protection, 152, 679-691. [Google Scholar] [CrossRef
[29] Chen, J., Wen, G., Yan, S., Lan, X. and Xiao, L. (2020) Oxidation and Characterization of Low-Concentration Gas in a High-Temperature Reactor. Processes, 8, Article 481. [Google Scholar] [CrossRef
[30] 吴云飞. 基于GRI-Mech 3.0的脉动燃烧NOx生成机理简化方法研究与分析[D]: [硕士学位论文]. 杭州: 浙江工业大学, 2012
[31] 高娜, 张延松, 胡毅亭, 等. 受限空间瓦斯爆炸链式反应动力学分析[J]. 中国安全科学学报, 2014, 24(1): 60-65.
[32] 李晓文. 采空区含瓦斯条件下煤自燃气体产物的爆炸特性及爆炸传输规律研究[D]: [硕士学位论文]. 徐州: 中国矿业大学, 2022.