摘要
为研究大型火灾的远程扑救问题,以1.7 m×1.8 m×180.0 m的混凝土结构为隧道实体模型,分别研究5、40μm的冷气溶胶灭火剂在无火源释放后的运动过程,研究其弥漫特性与淹没效果。磷酸二氢铵的质量流速为3.5 kg/s,空气的速度为3 m/s。运用Gambit建模,以ANSYS 15.0开展数值模拟研究,与试验结果进行对比分析。结果表明:冷气溶胶灭火剂的颗粒粒径影响隧道内不同位置处的微粒浓度;灭火剂粒径越小,其在狭长隧道前端的浓度越低,而在隧道后端的浓度越高;模拟时灭火剂的平均粒径越小,其浓度误差越低,并且模拟能检测到更低数量级的微粒浓度。
In order to study the long-range fire-fighting problem of large-scale fires, the concrete structure of 1.7 m × 1.8 m × 180.0 m was used as the real type tunnel, and the motion processes of 5 and40 μm cold aerosol fire extinguishing agents after no fire source release was studied, and the diffuse features and the inundation effect were studied too. The mass flow of ammonium dihydrogen phosphate was 3.5 kg/s, the air speed was 3 m/s. Gambit was used to model and numerical simulation was carried out by ANSYS15.0. The simulation results were compared with the experimental results. The simulation results showed that the particle size of the cold aerosol fire extinguishing agent affected the concentration of particles at different locations in the tunnel. The smaller the particle size of the fire extinguishing agent was, the lower the concentration on the front of the narrow tunnel and the higher the concentration at the rear of the tunnel would be. The smaller the average particle size of the extinguishing agent was, the lower the concentration error would be. Moreover, the simulation could detect particle concentration with lower order.
引文
[1]梁国栋.冷气溶胶与热气溶胶灭火剂在扑灭隧道火灾中的应用[J].山西科技,2013,28(4):146-147.
[2]戴彪,张树海,陈亚红.新型冷气溶胶灭火剂灭火性能的研究[J].科学技术与工程,2016,16(28):308-312.
[3]KIBERT C J,DIERDORFD.Solid particulate aerosol fire suppressants[J].Fire Technology,1994,30(4):387-399.
[4]徐大用,戴晓莹,华敏,等.无火源释放后冷气溶胶灭火剂运动过程的数值模拟[J].南京工业大学学报(自然科学版),2012,34(6):130-135.
[5]崔健.聚磷酸铵阻燃剂技术进展及应用[J].现代塑料加工应用,2000,12(2):36-38.
[6]KRASNYANSKY M.Remote extinguishing of large fires with powder aerosols[J].Fire and Materials:An International Journal,2006,30(5):371-382.
[7]殷志平.磷酸铵盐微粒灭火剂在单室火灾抑制过程中的动力学性能研究[D].南京:南京理工大学,2008.
[8]李碧英.冷气溶胶灭火剂的制备及性能研究[D].南京:南京理工大学,2004.
[9]KRASNYANSKY M.Studies of Fundamental Physical-chemical Mechanisms and Processes of Flame Extinguishing by Powder Aerosols[J].Fire and Materials:An International Journal,2008,32(1):27-47.
[10]王福军.计算流体动力学分析-CFD软件原理与应用[M].北京:清华大学出版社,2004.
[11]李艳强,吴超,易斌,等.受限空间内粉尘流动的浓度分布模型及其数值模拟[J].中国安全科学学报,2007,17(10):50-55+181.
[12]CROWE C T,TROUTT T R,CHUNG J N.Numerical models for two-phase turbulent flows[J].Annual Review of Fluid Mechanics,1996,28(1):11-43.
[13]ZHOU L X,CHEN T.Simulation of swirling gas-particle flows using USM and k-ε-kp two-phase turbulence models[J].Powder Technology,2001,114(1-3):1-11.
[14]RAHUL G.Modeling and simulation of two-phases flow[D].Ames:Iowa State University,2009.
[15]ZHANG X,ISMAIL M H S,HEE C.Hot aerosol fire extinguishing agents and the associated technologies:a review[J].Brazilian Journal of Chemical Engineering,2015,32(3):707-724.