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International Journal of Scientific and Technical Research in Engineering (IJSTRE)
www.ijstre.com Volume 3 Issue 1 ǁ January 2018.
Manuscript id. 214563900 www.ijstre.com Page 14
Experimental Study on Toxic Gas Produced during Pipeline Gas
Explosions
JIA Zhi-wei1,2
XU Sheng-ming1
(1.School of Safety Science and Engineering, Henan Polytechnic University, Jiaozuo, 454003, China
2.Central Plains Economic Zone Coal Methane cooperative innovation center in Henan Province,Jiaozuo, 454003, China)
Abstract: Dangerous gas explosion accidents result in considerable amount of casualties and property damage.
Hence, an investigation on the generation of poisonous gases in gas explosions exerts important implications
for accident prevention and control and in the decision-making processes of fire rescue. Therefore, a gas
explosion piping test system is established in this paper. Experimental research on gas explosion is conducted by
selecting methane/air premixed gases with concentrations of 7%, 9%, 11%, 13%, and 15% in the gas explosive
range. This research aims to reveal the regularity of CO generation after gas explosion in pipelines.
Experimental results showed that when the gas concentration is small (< 9%), 1500–3000 ppm CO will be
produced. When the gas concentration is large (> 9%), the CO amount will reach 3000–40000 ppm. The
variation trend in CO concentration and the quantity of explosive gas are also obtained.
Key Words: gas explosion, piping test system, gas concentration, CO concentration
I. Background and significance of the study
Approximately 95% of China’s coal is obtained through underground mining, which involves complex
geological conditions and relatively adverse working environments. In 2013, the average mining depth of large
and medium coal mines is 650 m; the mining depth of Pingdingshan coal mine in Henan Province is 1000 m,
which extends downward with an average annual rate of 10 m [1-3]
. With the increased coal mining depth, the gas
content and pressure in the coal and the gas emission quantity also increase, thereby causing increasingly severe
gas explosions and coal and gas outbursts. In recent years, with the gradual increase in the coal mine safety
management level and safety investment in China, the death rate per million ton coal decreases annually, and
gas disaster has been effectively controlled [4-5]
. Nevertheless, in 2013, the death rate per million tons of coal in
China remains 10 times that of the United States; additionally, the death rate from gas and coal dust explosions
still exceeds 100 each year [6-7]
. In the past 10 years, considerable local and international research has been
performed about the factors influencing the gas explosion generation and the effects of shape, size, angle, and
wall roughness of underground roadway on the generation of flame and wave during gas explosion [8-14]
.
However, study on the mechanism and propagation law of gas explosion is still limited. In particular, research
on the generation and influencing factors of toxic gas during gas explosion lacks a system. Results cannot also
provide guidance on disaster relief decision for gas explosion accidents. Major coal dust explosion accidents
result in a substantial amount of casualties and property losses, a remarkable psychological trauma to the people,
and negative effects on the community. Therefore, research on the generation of shock wave, flame, and toxic
gas during gas explosion presents important guiding significance for accident control and disaster relief decision
[15]
. The generation and propagation of toxic gas, which causes considerable harm, should be investigated. The
Experimental Study on Toxic Gas Produced during Pipeline Gas Explosions
Manuscript id. 214563900 www.ijstre.com Page 15
obtained research results are largely important for estimating the diffusion range of toxic gas in underground
tunnel after gas explosion accidents.
II. Experimental study on carbon monoxide produced by gas explosion in pipelines
2.1 Establishment of experimental systems
In this experiment, we used the experimental system with a total length of 20.9 m. The explosion pipeline
showed a dimension of 80 mm × 80 mm. The gas explosion concentrations of 7%, 9%, 11%, 13%, and 15% of
methane/air premixed gas were selected to produce CO. We concluded that the CO amount in the gas explosion
accident is associated with the change in gas concentration. The schematic diagram of the gas explosion
experiment system is shown in Fig. 1.
1 2 3 4
5 6 7 8 9 10 11 12
1 - High Energy Ignition Device, 2 - Vacuum Flow Meter, 3 - Spherical Valve, 4 – Poison Gas Collection, 5–8
Front CO Detection Point, 9–12 Rear CO Detection Point
Figure 1 Gas explosion experiment system
Prior to the experiment, the spherical valve was opened. The vacuum pump was picked up at point 4, the
pipe was evacuated, the spherical valve was closed, and the gas with different concentrations was injected by the
vacuum flow meter. The gas explosion started at the ignition device and continued in the ball valve on the left
side of the pipeline. Points 5–8 were used to measure the gas explosion generated by the CO concentration. The
distance between points 5–8 and point 1 was 0.25, 1.35, 2.2, and 3.95 m, respectively. The physical model of the
experimental gas explosion system is shown in Figs. 2 and 3.
Figure 2 Cavity gas explosion experiment Figure 3 Gas explosion experimental
pipe system
2.2 Experimental data and treatment
Gas explosion with different gas concentrations (30 times) produced six groups of CO. Experimental results
are shown in Table 1。
Experimental Study on Toxic Gas Produced during Pipeline Gas Explosions
Manuscript id. 214563900 www.ijstre.com Page 16
Table 1 Relationship between each measuring point and the gas concentration
CH4 concentration
/%
CO concentration/ppm
Measuring point1 Measuring point2 Measuring point3 Measuring point4
7 1550 1600 1550 1400
9 2100 1900 1550 2200
11 16300 15200 17500 10700
13 26750 31050 28350 29500
15 39300 36900 32500 40300
7 1350 1400 1200 1750
9 2200 1350 1400 1700
11 11250 12000 11000 14550
13 27750 28050 29350 30500
15 33300 37000 31500 40500
7 1650 1750 1300 1400
9 2400 2200 2000 2150
11 13250 12050 13050 14550
13 28500 29150 29550 28700
15 39500 43200 44050 39500
7 1850 1300 1650 1400
9 2150 2150 2150 2150
11 11250 14050 11050 10050
13 31750 28350 29650 27850
15 39050 30500 32050 36500
7 1550 1350 2450 1050
9 2100 2050 1800 1350
11 13050 10500 11050 10300
13 31750 29000 30750 31550
15 35050 38050 40450 36750
7 1700 1350 1300 1650
9 2200 1700 1450 2050
11 13300 12500 13200 14300
13 28550 29350 31050 29850
15 33050 39500 27050 37050
The six groups of experimental results were averaged. The relationship between the gas concentration and
CO concentration was determined through the gas explosions with different concentrations, as shown in Fig. 4.
Experimental Study on Toxic Gas Produced during Pipeline Gas Explosions
Manuscript id. 214563900 www.ijstre.com Page 17
Figure 4 CO concentration with prefilled gas concentration
The relationship between CO and the amount of explosion gas involved in the enclosed confined space was
obtained using the following equations:
2 . 3 2 4 8
8 6 9 . 8 8xy  ;
9359.02
R .
III. Data analysis and conclusion
The amount of CO produced after a gas explosion in the pipeline is related to the concentration of the gas
during explosion. Therefore, the gas concentration determines the peak density of CO. When the gas
concentration exceeds 9%, the CO concentration also increases evidently; high gas concentration results in a
large amount of CO produced. This result is attributed to that when the gas concentration is small (< 9%), the
amount of oxygen in contact with the gas is relatively abundant. Consequently, methane can be fully reacted.
Given that the gas density is less than that of air, a stratified phenomenon occurs in the pipeline mixing process:
the gas is in the upper part, and the air is in the lower part. A small amount of gas combustion during explosion
is insufficient, thereby producing a small amount of CO. When the gas concentration is relatively large (> 9%),
the reaction occurs when the critical point begins to react strongly with a highly representative reaction.
Furthermore, the oxygen cannot fully support all methane combustion, and the amount produced by the CO
increases rapidly with increased gas concentration.
Experimental data analysis resulted in the following conclusions:
(1) When the gas concentration is small (< 9%), the gas explosion will produce a small amount of CO
(1500–3000 ppm). By contrast, when the gas concentration is relatively large (> 9%), the gas explosion will
produce a large amount of CO (3000–40000 ppm).
(2) High gas concentration results in large amount of CO produced. The following relation is also
obtained: 2.3248
869.88xy  .
IV. Acknowledgement
This study was supported by Program for National Natural Science Foundation of China (No.51774120).
Experimental Study on Toxic Gas Produced during Pipeline Gas Explosions
Manuscript id. 214563900 www.ijstre.com Page 18
References:
[1] WANG Hai-yan, ZHOU Xin-quan, QU Zhi-ming. Study on influence and interrelation between shock
wave and combustion wave of gas explosion [J]. Coal mine safety, 2008, 39(4): 1-4.
[2] XU Shao-qian, CAI Zhou-quan, LI Jian-xin. Experimental study on dissemination of low concentration
gas explosion in pipelines [J]. Mining Safety and Environmental Protection, 2008, 35(2): 22-24
[3] LI Run-zhi. SI Rong-jun, ZHANG Yan-song, etc. Experimental study of low concentration gas
explosion dissemination in pipeline [J]. Journal of Shandong University of Science and Technology,
2009, 28(1): 35-39
[4] JIA Zhi-wei, LI Xiao-jun, YANG Shu-zhao. The research progress of gas explosion dissemination in
Coal[J]. Mining Safety and Environmental Protection, 2008, 35(6): 73-75.
[5] JIA Zhi-wei. Research on theoretical spreading law of shockwave of gas explosion in general air
area[D].Henan Polytechnic University, 2008
[6] TAN Guo-qing, ZHOU Xin-quan, CAO Tao, ZHANG Dai-yue. The new characteristics of serious gas
explosion accidents and especially serious gas explosion accidents in the resent years[J]. China Coal,
2009(4):713
[7] LIU Jian-sheng, WANG Xiao-lei. study on the basic characteristics and occurrence regularity of gas
explosion from 2001 to 2013[J]. Zhongzhou Coal, 2014, 9:72-76
[8] JING Guo-xun, YANG Shu-zhao. Experimental study on propagation characteristics of coal dust
explosion[J]. Journal of China Coal Society, 2010, 35(4): 605-608.
[9] JING Guo-xun, DUAN Zhen-wei, CEHN Lei, YANG Shu-zhao. Research progressing explosion
characteristics and spread law of gas and coal dust[J]. China Safety Science Journal, 2009, (19)4: 67-72.
[10 ]YANG Shu-zhao, JING Guo-xun, JIA Zhi-wei. Injury study on impact current of gas explosion in coal
mine[J]. Journal of China Coal Society, 2009(10): 145-149
[11] JIA Zhi-wei, LIU Yan-wei, JING Guo-xun. Propagation characteristic about shockwave of gas explosion
at lane way corner[J]. Journal of China Coal Society, 2011, 36(1): 97-100
[12] JIANG Bing-you, LIN Bai-quan, ZHU Chuan-jie, etc. Influence of uniform electric firld on flame
transimission and blast wave in gas explosion[J]. Proceedings of 2010(Shenyang) International
Colloquium on Safety Science and Technology,2010: 267-272
[13] LIN Bai-quan, JIAN Cong-guang. Inducement of turbulence and its effect on fire transmission in gas
explosion[J]. Journal of China Univ ersity o f Mining and Tech no logy, 2003, 32(2): 108-110.
[14] LIN Bai-quan, GUI Xiao-hong. Computer simulation on the temperature Field of gas explosion and lab
measurement for the flame thickness[J]. Journal of Experimental Mechanics, 2002, 17(22): 227-233.

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Experimental Study on Toxic Gas Produced during Pipeline Gas Explosions

  • 1. International Journal of Scientific and Technical Research in Engineering (IJSTRE) www.ijstre.com Volume 3 Issue 1 ǁ January 2018. Manuscript id. 214563900 www.ijstre.com Page 14 Experimental Study on Toxic Gas Produced during Pipeline Gas Explosions JIA Zhi-wei1,2 XU Sheng-ming1 (1.School of Safety Science and Engineering, Henan Polytechnic University, Jiaozuo, 454003, China 2.Central Plains Economic Zone Coal Methane cooperative innovation center in Henan Province,Jiaozuo, 454003, China) Abstract: Dangerous gas explosion accidents result in considerable amount of casualties and property damage. Hence, an investigation on the generation of poisonous gases in gas explosions exerts important implications for accident prevention and control and in the decision-making processes of fire rescue. Therefore, a gas explosion piping test system is established in this paper. Experimental research on gas explosion is conducted by selecting methane/air premixed gases with concentrations of 7%, 9%, 11%, 13%, and 15% in the gas explosive range. This research aims to reveal the regularity of CO generation after gas explosion in pipelines. Experimental results showed that when the gas concentration is small (< 9%), 1500–3000 ppm CO will be produced. When the gas concentration is large (> 9%), the CO amount will reach 3000–40000 ppm. The variation trend in CO concentration and the quantity of explosive gas are also obtained. Key Words: gas explosion, piping test system, gas concentration, CO concentration I. Background and significance of the study Approximately 95% of China’s coal is obtained through underground mining, which involves complex geological conditions and relatively adverse working environments. In 2013, the average mining depth of large and medium coal mines is 650 m; the mining depth of Pingdingshan coal mine in Henan Province is 1000 m, which extends downward with an average annual rate of 10 m [1-3] . With the increased coal mining depth, the gas content and pressure in the coal and the gas emission quantity also increase, thereby causing increasingly severe gas explosions and coal and gas outbursts. In recent years, with the gradual increase in the coal mine safety management level and safety investment in China, the death rate per million ton coal decreases annually, and gas disaster has been effectively controlled [4-5] . Nevertheless, in 2013, the death rate per million tons of coal in China remains 10 times that of the United States; additionally, the death rate from gas and coal dust explosions still exceeds 100 each year [6-7] . In the past 10 years, considerable local and international research has been performed about the factors influencing the gas explosion generation and the effects of shape, size, angle, and wall roughness of underground roadway on the generation of flame and wave during gas explosion [8-14] . However, study on the mechanism and propagation law of gas explosion is still limited. In particular, research on the generation and influencing factors of toxic gas during gas explosion lacks a system. Results cannot also provide guidance on disaster relief decision for gas explosion accidents. Major coal dust explosion accidents result in a substantial amount of casualties and property losses, a remarkable psychological trauma to the people, and negative effects on the community. Therefore, research on the generation of shock wave, flame, and toxic gas during gas explosion presents important guiding significance for accident control and disaster relief decision [15] . The generation and propagation of toxic gas, which causes considerable harm, should be investigated. The
  • 2. Experimental Study on Toxic Gas Produced during Pipeline Gas Explosions Manuscript id. 214563900 www.ijstre.com Page 15 obtained research results are largely important for estimating the diffusion range of toxic gas in underground tunnel after gas explosion accidents. II. Experimental study on carbon monoxide produced by gas explosion in pipelines 2.1 Establishment of experimental systems In this experiment, we used the experimental system with a total length of 20.9 m. The explosion pipeline showed a dimension of 80 mm × 80 mm. The gas explosion concentrations of 7%, 9%, 11%, 13%, and 15% of methane/air premixed gas were selected to produce CO. We concluded that the CO amount in the gas explosion accident is associated with the change in gas concentration. The schematic diagram of the gas explosion experiment system is shown in Fig. 1. 1 2 3 4 5 6 7 8 9 10 11 12 1 - High Energy Ignition Device, 2 - Vacuum Flow Meter, 3 - Spherical Valve, 4 – Poison Gas Collection, 5–8 Front CO Detection Point, 9–12 Rear CO Detection Point Figure 1 Gas explosion experiment system Prior to the experiment, the spherical valve was opened. The vacuum pump was picked up at point 4, the pipe was evacuated, the spherical valve was closed, and the gas with different concentrations was injected by the vacuum flow meter. The gas explosion started at the ignition device and continued in the ball valve on the left side of the pipeline. Points 5–8 were used to measure the gas explosion generated by the CO concentration. The distance between points 5–8 and point 1 was 0.25, 1.35, 2.2, and 3.95 m, respectively. The physical model of the experimental gas explosion system is shown in Figs. 2 and 3. Figure 2 Cavity gas explosion experiment Figure 3 Gas explosion experimental pipe system 2.2 Experimental data and treatment Gas explosion with different gas concentrations (30 times) produced six groups of CO. Experimental results are shown in Table 1。
  • 3. Experimental Study on Toxic Gas Produced during Pipeline Gas Explosions Manuscript id. 214563900 www.ijstre.com Page 16 Table 1 Relationship between each measuring point and the gas concentration CH4 concentration /% CO concentration/ppm Measuring point1 Measuring point2 Measuring point3 Measuring point4 7 1550 1600 1550 1400 9 2100 1900 1550 2200 11 16300 15200 17500 10700 13 26750 31050 28350 29500 15 39300 36900 32500 40300 7 1350 1400 1200 1750 9 2200 1350 1400 1700 11 11250 12000 11000 14550 13 27750 28050 29350 30500 15 33300 37000 31500 40500 7 1650 1750 1300 1400 9 2400 2200 2000 2150 11 13250 12050 13050 14550 13 28500 29150 29550 28700 15 39500 43200 44050 39500 7 1850 1300 1650 1400 9 2150 2150 2150 2150 11 11250 14050 11050 10050 13 31750 28350 29650 27850 15 39050 30500 32050 36500 7 1550 1350 2450 1050 9 2100 2050 1800 1350 11 13050 10500 11050 10300 13 31750 29000 30750 31550 15 35050 38050 40450 36750 7 1700 1350 1300 1650 9 2200 1700 1450 2050 11 13300 12500 13200 14300 13 28550 29350 31050 29850 15 33050 39500 27050 37050 The six groups of experimental results were averaged. The relationship between the gas concentration and CO concentration was determined through the gas explosions with different concentrations, as shown in Fig. 4.
  • 4. Experimental Study on Toxic Gas Produced during Pipeline Gas Explosions Manuscript id. 214563900 www.ijstre.com Page 17 Figure 4 CO concentration with prefilled gas concentration The relationship between CO and the amount of explosion gas involved in the enclosed confined space was obtained using the following equations: 2 . 3 2 4 8 8 6 9 . 8 8xy  ; 9359.02 R . III. Data analysis and conclusion The amount of CO produced after a gas explosion in the pipeline is related to the concentration of the gas during explosion. Therefore, the gas concentration determines the peak density of CO. When the gas concentration exceeds 9%, the CO concentration also increases evidently; high gas concentration results in a large amount of CO produced. This result is attributed to that when the gas concentration is small (< 9%), the amount of oxygen in contact with the gas is relatively abundant. Consequently, methane can be fully reacted. Given that the gas density is less than that of air, a stratified phenomenon occurs in the pipeline mixing process: the gas is in the upper part, and the air is in the lower part. A small amount of gas combustion during explosion is insufficient, thereby producing a small amount of CO. When the gas concentration is relatively large (> 9%), the reaction occurs when the critical point begins to react strongly with a highly representative reaction. Furthermore, the oxygen cannot fully support all methane combustion, and the amount produced by the CO increases rapidly with increased gas concentration. Experimental data analysis resulted in the following conclusions: (1) When the gas concentration is small (< 9%), the gas explosion will produce a small amount of CO (1500–3000 ppm). By contrast, when the gas concentration is relatively large (> 9%), the gas explosion will produce a large amount of CO (3000–40000 ppm). (2) High gas concentration results in large amount of CO produced. The following relation is also obtained: 2.3248 869.88xy  . IV. Acknowledgement This study was supported by Program for National Natural Science Foundation of China (No.51774120).
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