Influence of Ventilation Duct Parameter Optimization on Pollutant Diffusion in Spiral Tunnels
Abstract
:1. Introduction
2. Orthogonal Experiment and Numerical Simulation Method
2.1. Orthogonal Experimental Design
2.2. Numerical Simulation
2.2.1. Assumed Conditions
- Considering that the ventilation airflow in the tunnel or air duct was at low speed, this took the air as incompressible fluid.
- The low speed airflow was turbulent at a steady stage. Then, standard k-ε model, which was widely applied as viscous model, was used during computation.
- The tunnel wall could not transfer energy; the fluid field was at a constant temperature. There was no chemical reaction during the diffusion movement.
- During tunnel mucking, most of the harmful gases generated by engines were nitrogen oxides; carbon oxides were minimal, and 90% of nitrogen oxides were nitric oxide [21]. Therefore, the nitric oxide (NO) was selected as the harmful gas during the tunnel slagging.
- The dust, carbon monoxide (CO) and nitrogen dioxide (NO2) involved in the simulation process were all generated during the construction process. The air content under initial conditions was 21% oxygen and 79% nitrogen.
2.2.2. Turbulence Model
2.2.3. Initial Conditions
- When studying carbon monoxide (CO) concentration after blasting, assuming that the carbon monoxide gas was instantaneously filled and evenly distributed within a distance after the tunnel face at one concentration, this distance was called smoke casting distance. The CO mass fraction within the smoke casting distance was calculated by:
- The main source of dust diffusion in this study is the gunite lining. The largest dust comes from spraying to the roof, which rebounds into the tunnel space, and continuously spreads out of the tunnel with the wind flow. During this period, settlement may occur. In this research, it is assumed that the dust settles After reaching the ground, dust was caught and stopped flying in the air. Using a discrete phase model (DPM) to compute dust particles transportation, the velocity of rebounded dust was around 60 m/s; the mass flow was 0.06 kg/s. The dust pollution source was a 3-m width range on the tunnel wall, shown in Figure 3.
- 3.
- For the based tunnel in this research, the total power of diesel engines during tunnel mucking was 402.9 KW. However, considering nitric oxide would be oxidized, the gas source would be set to release nitrogen dioxide directly. Converting the mass flow of NO into NO2, the total mass flow of NO2 from gas sources was 0.00035 kg/s. Assuming there were three NO2 gas sources (excavator, tipper, and spraying machine), the schematic diagram is shown in Figure 4.
2.2.4. Boundary Conditions
3. Results
3.1. Carbon Monoxide Concentration in Tunnel after Blasting
3.2. Dust Concentration in Tunnel during Gunite Lining
4. Spiral Tunnel Ventilation System Optimization
5. Enlightenment of Current Research Work
6. Conclusions
- For the time required for the concentration of carbon monoxide in the tunnel to drop to the standard after blasting, the distance from the air duct to the tunnel face has no significant effect on it.
- For the dust concentration at the height of human respiration during the spraying process, the three factors of air duct speed, the hanging position of the air duct, and the distance from the air duct to the face have certain influence, but the effect is not significant.
- The optimal ventilation layout calculated is that the air duct is suspended on the outer side of the midline and the air duct is about 15 m away from the tunnel face, and the wind speed is 27.65 m/s. However, considering the economic cost and the problem of dust in the tunnel, the best ventilation scheme recommended for spiral tunnels in the context of this project is for the air duct to be suspended at the outer arch of the center line, the distance between the air duct and the tunnel face to be about 15–20 m, and the wind speed to be around 23–25 m/s.
- The ventilation optimization results of the spiral tunnel can improve the ventilation effect and the ventilation quality and provide a reference for the ventilation problems in the construction of other spiral tunnels. In addition, it is necessary to establish a physical model of a spiral tunnel to study the influence of various factors on pollutants in spiral tunnel construction.
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
References
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Levels | Factors | ||
---|---|---|---|
Hanging Position of the Ventilation Duct (A) | Distance between the Ventilation Duct and the Tunnel Face (B) | Ventilation Velocity at the Outlet of the Ventilation Duct (C) | |
1 | vault | 10 m | 27.65 m/s |
2 | left haunch | 15 m | 25.39 m/s |
3 | right haunch | 20 m | 23.12 m/s |
4 | left arch bottom | 25 m | 20.85 m/s |
5 | right arch bottom | 30 m | 18.59 m/s |
Test Number | Hanging Position of the Ventilation Duct (A) | Distance between the Ventilation Duct and the Tunnel Face (B) | Ventilation Velocity at the Outlet of the Ventilation Duct (C) |
---|---|---|---|
1 | A-1 | B-1 | C-1 |
2 | A-1 | B-2 | C-2 |
3 | A-1 | B-3 | C-3 |
4 | A-1 | B-4 | C-4 |
5 | A-1 | B-5 | C-5 |
6 | A-2 | B-1 | C-2 |
7 | A-2 | B-2 | C-3 |
8 | A-2 | B-3 | C-4 |
9 | A-2 | B-4 | C-5 |
10 | A-2 | B-5 | C-1 |
11 | A-3 | B-1 | C-3 |
12 | A-3 | B-2 | C-4 |
13 | A-3 | B-3 | C-5 |
14 | A-3 | B-4 | C-1 |
15 | A-3 | B-5 | C-2 |
16 | A-4 | B-1 | C-4 |
17 | A-4 | B2 | C-5 |
18 | A-4 | B-3 | C-1 |
19 | A-4 | B-4 | C-2 |
20 | A-4 | B-5 | C-3 |
21 | A-5 | B-1 | C-5 |
22 | A-5 | B-2 | C-1 |
23 | A-5 | B-3 | C-2 |
24 | A-5 | B-4 | C-3 |
25 | A-5 | B-5 | C-4 |
Discrete Phase Model | Define |
---|---|
Interaction With Continuous Phase | Open |
Update DPM Sources Every Flow Iteration | Open |
Number of Continuous Phase Iterations Per DPM Iteration | 10 |
Unsteady Particle Tracking | Open |
Max Number of Steps | 3000 |
Length Scale | 0.01 m |
Drag Law | Spherical |
Injection | Define |
---|---|
Material | SiO2 |
Injection Type | Surface |
Diameter Distribution | Rosin-Rammler |
Total Flow Rate | 0.11808 kg/s |
Min. Diameter | 1 × 10−6 |
Max. Diameter | 2 × 10−4 |
Mean. Diameter | 1.08 × 10−4 |
Spread Parameter | 3 |
Inject Using Face Normal Direction | Open |
Velocity Magnitude | 6 m/s |
Testing Number | Factor-Level | Time Required for CO Concentration to Reach the Regulations after Blasting(s) | ||
---|---|---|---|---|
Factor A | Factor B | Factor C | ||
1 | A-1 | B-1 | C-1 | 1200 |
2 | A-1 | B-2 | C-2 | 1296 |
3 | A-1 | B-3 | C-3 | 1424 |
4 | A-1 | B-4 | C-4 | 1616 |
5 | A-1 | B-5 | C-5 | 1744 |
6 | A-2 | B-1 | C-2 | 1440 |
7 | A-2 | B-2 | C-3 | 1600 |
8 | A-2 | B3 | C-4 | 1808 |
9 | A-2 | B-4 | C-5 | 1936 |
10 | A-2 | B-5 | C-1 | 1344 |
11 | A-3 | B-1 | C-3 | 1392 |
12 | A-3 | B-2 | C-4 | 1312 |
13 | A-3 | B-3 | C-5 | 1824 |
14 | A-3 | B-4 | C-1 | 1296 |
15 | A-3 | B-5 | C-2 | 1312 |
16 | A-4 | B-1 | C-4 | 1568 |
17 | A-4 | B-2 | C-5 | 1984 |
18 | A-4 | B-3 | C-1 | 1360 |
19 | A-4 | B-4 | C-2 | 1568 |
20 | A-4 | B-5 | C-3 | 1632 |
21 | A-5 | B-1 | C-5 | 2048 |
22 | A-5 | B-2 | C-1 | 1344 |
23 | A-5 | B-3 | C-2 | 1392 |
24 | A-5 | B-4 | C-3 | 1600 |
25 | A-5 | B-5 | C-4 | 1664 |
Variables | Sum of Squares | Deg. of Freedom | Mean Square | F-Value | Significance |
---|---|---|---|---|---|
Factor A | 192,040.960 | 4 | 48,010.240 | 6.480 | 0.005 |
Factor B | 26,562.560 | 4 | 6640.640 | 0.896 | 0.496 |
Factor C | 1,050,460.160 | 4 | 262,615.040 | 35.447 | 0.000 |
Random Error | 88,903.680 | 12 | 7408.640 | ||
SUM | 61,277,952.00 | 25 |
Testing Mumber | Factor-Level | Concentration of Dust at Steady Stage during Gunite Lining (mg/m3) | ||
---|---|---|---|---|
Factor A | Factor B | Factor C | ||
1 | A-1 | B-1 | C-1 | 25.960 |
2 | A-1 | B-2 | C-2 | 24.200 |
3 | A-1 | B-3 | C-3 | 43.130 |
4 | A-1 | B-4 | C-4 | 51.590 |
5 | A-1 | B-5 | C-5 | 50.240 |
6 | A-2 | B-1 | C-2 | 37.790 |
7 | A-2 | B-2 | C-3 | 88.860 |
8 | A-2 | B-3 | C-4 | 44.880 |
9 | A-2 | B-4 | C-5 | 83.490 |
10 | A-2 | B-5 | C-1 | 57.130 |
11 | A-3 | B-1 | C-3 | 47.790 |
12 | A-3 | B-2 | C-4 | 46.740 |
13 | A-3 | B-3 | C-5 | 46.370 |
14 | A-3 | B-4 | C-1 | 53.120 |
15 | A-3 | B-5 | C-2 | 75.890 |
16 | A-4 | B-1 | C-4 | 42.430 |
17 | A-4 | B-2 | C-5 | 81.600 |
18 | A-4 | B-3 | C-1 | 42.670 |
19 | A-4 | B-4 | C-2 | 32.680 |
20 | A-4 | B-5 | C-3 | 54.840 |
21 | A-5 | B-1 | C-5 | 68.420 |
22 | A-5 | B-2 | C-1 | 35.550 |
23 | A-5 | B-3 | C-2 | 27.970 |
24 | A-5 | B-4 | C-3 | 29.200 |
25 | A-5 | B-5 | C-4 | 42.900 |
Variables | Sum of Squares | Deg. Of Freedom | Mean Square | F-Value | Significance |
---|---|---|---|---|---|
Factor A | 1871.715 | 4 | 467.929 | 1.967 | 0.164 |
Factor B | 886.085 | 4 | 221.521 | 0.931 | 0.478 |
Factor C | 2188.545 | 4 | 547.136 | 2.300 | 0.119 |
Random Error | 2854.521 | 12 | 237.877 | ||
SUM | 68,853.346 | 25 |
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Bai, J.; Wu, Z.; Chen, T.; Li, W.; Zhang, P.; Li, Y. Influence of Ventilation Duct Parameter Optimization on Pollutant Diffusion in Spiral Tunnels. Sustainability 2022, 14, 10540. https://doi.org/10.3390/su141710540
Bai J, Wu Z, Chen T, Li W, Zhang P, Li Y. Influence of Ventilation Duct Parameter Optimization on Pollutant Diffusion in Spiral Tunnels. Sustainability. 2022; 14(17):10540. https://doi.org/10.3390/su141710540
Chicago/Turabian StyleBai, Jiashe, Zhongbin Wu, Tongyong Chen, Wenqiang Li, Ping Zhang, and Yu Li. 2022. "Influence of Ventilation Duct Parameter Optimization on Pollutant Diffusion in Spiral Tunnels" Sustainability 14, no. 17: 10540. https://doi.org/10.3390/su141710540
APA StyleBai, J., Wu, Z., Chen, T., Li, W., Zhang, P., & Li, Y. (2022). Influence of Ventilation Duct Parameter Optimization on Pollutant Diffusion in Spiral Tunnels. Sustainability, 14(17), 10540. https://doi.org/10.3390/su141710540