主管:中华人民共和国应急管理部
主办:应急管理部天津消防研究所
ISSN 1009-0029  CN 12-1311/TU

消防科学与技术 ›› 2022, Vol. 41 ›› Issue (10): 1396-1400.

• • 上一篇    下一篇

双层盾构公路隧道侧向重点排烟效果研究

余 沛,袁建平,方 正,唐 智   

  1. (武汉大学 土木建筑工程学院,湖北 武汉 430072)
  • 出版日期:2022-10-15 发布日期:2022-10-15
  • 通讯作者: 湖北省重点研发计划项目(2021BCA217);武汉中交交通工程有限责任公司科研项目
  • 作者简介:作者简介:余 沛(1998- ),女,武汉大学土木建筑工程学院硕士研究生,主要从事隧道防排烟以及建筑消防技术研究,湖北省武汉市武昌区东湖南路8号,430072。

Study on lateral point smoke exhaust efficiency in double-deck shield road tunnel

Yu Pei,Yuan Jianping,Fang Zheng,Tang Zhi   

  1. (School of Civil Engineering, Wuhan University, Hubei Wuhan 430072, China)
  • Online:2022-10-15 Published:2022-10-15

摘要: 摘 要:利用FDS对某双层盾构公路隧道的侧向重点排烟系统进行了模拟研究,探讨了排烟口面积、间距、排烟口开启方案以及纵向通风对排烟效果的影响。结果表明:在无纵向风的条件下,火灾稳定后排烟口的面积为3~5 m2、排烟口间距为60~100 m时,排烟口的面积和间距对排烟效果的影响很小。随着纵向通风风速的增大和上游排烟口开启数量的增加,隧道侧向排烟系统的排烟效率明显减小。双层隧道上下层排烟口的排烟效率分布规律基本相同,下层隧道的总排烟效率略高一些。本文所研究的双层隧道发生20 MW火灾时,在纵向通风风速2 m/s下,排烟口间距为60 m,排烟口面积为4 m2,上游开启2个排烟口、下游开启4个排烟口时排烟效果更好。

关键词: 关键词:双层盾构隧道, 侧向重点排烟, 数值模拟, 排烟效率

Abstract: Abstract: Fluent software was used and the Euler multiphase flow model was used to simulate the along-path resistance, flow velocity and dry powder concentration distribution characteristics of ultra-fine dry powder fire extinguishing agent with a particle size of 18 μm sprayed in a horizontal straight pipe with a diameter of 8 cm. The results show that in the range of flow velocity 25~150 m/s and ultrafine dry powder volume fraction 5%~15%, the resistance along the horizontal straight pipe has a quadratic function relationship with the flow velocity, and a linear function relationship with the dry powder volume fraction. The range of resistance value is 0.003 28~0.259 81 MPa/m. Affected by the friction of the pipe wall, the flow velocity of the two-phase flow on the cross section of the pipe presents a distribution characteristic of fast in the middle and slow in the surrounding area, and the effect of the volume fraction of solid particles on the flow velocity can be ignored. The gas-phase drag force generated by the different velocity distributions on the cross-section leads to the annular distribution of the ultrafine dry powder volume fraction. The gas-phase drag force is related to the initial velocity and has nothing to do with the dry powder volume fraction. When the flow rate is lower than 70 m/s, the ultra-fine dry powder is distributed in a crescent shape, and the volume fraction of the ultra-fine dry powder is the highest at the lower part of the pipeline close to the pipe wall. The volume fraction is the lowest near the pipe wall, and the flow velocity is greater than 70 m/s, which can effectively inhibit the sedimentation of ultra-fine dry powder.

Key words: Key words: gas-solid two-phase flow, ultra-fine dry powder, numerical simulation, resistance along the way