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The geometric model in this paper is determined based on the 'Code for Design of Garage Buildings' (JGJ100-2015) and the 'Code for Design of Concrete Structures' (GB50010-2010) (2015 edition). The length, width, and height of the underground garage are 21, 16.6, and 3.2 m, respectively. Each parking space has a length and width of 5.3 and 2.4 m, respectively. The hydrogen fuel cell vehicle has dimensions of 4.8 m in length, 1.8 m in width, and 1.4m in height, with a vertical parking arrangement. According to the specifications, the diameter of the columns should be no less than 0.3 m and no less than 1/6 of their height, with a maximum height of 12 m and no more than 20 times their diameter. Therefore, based on the actual situation, the cross-sectional dimensions of the columns in this paper are 0.6 m × 0.6 m, with a height of 3.2 m. For ease of analysis, the cross-sectional dimensions of the beams are also set to 0.6 m × 0.6 m. The distances between the columns in the garage under the 4-parking space bay pattern, 3-parking space bay pattern, and 2-parking space bay pattern are 9.6, 7.2, and 4.8 m, respectively. The geometric models of the three parking patterns designed in this paper and the bottom view of the garage under the 4-parking space bay pattern are shown in Fig. 1. The garage models under the 4-parking space bay pattern with different numbers of ventilation openings are shown in Fig. 2, where the garage doors are all open, with a width of 5 m and a height of 2.1 m. A total of six monitoring points are set in this paper, located at P (1.8, 15.6, 3.2), A (0, 11.9, 3.2), B (0, 16.6, 3.2), C (1.8, 16.6, 3.2), D (3, 16.6, 3.2), and E (3, 15.6, 3.2), respectively. Additionally, the hydrogen leak source in this paper is located at coordinates (1.8, 15.6, 1.4) within the space.
Figure 1.
Geometric model of the garage with different parking space modes and the base view of the garage with a 4-parking space mode.
Assuming that a hydrogen fuel cell vehicle parked at the corner of an underground garage experiences an accidental leakage, with hydrogen escaping upwards through a 2 mm circular leak hole. The internal pressure of the hydrogen tank is 35 MPa, while the temperature and pressure inside the underground garage are 300 K and 101.325 kPa, respectively. The parameters of the hydrogen leak hole are calculated using the modified Brich1987 virtual nozzle model, which incorporates the Abel-Nobel real gas equation of state[22]. According to the model, the hydrogen mass flow rate at the leak hole is determined to be 0.0678 kg/s. This leakage rate is used to investigate the diffusion and distribution patterns of high-pressure hydrogen in the event of accidental leakage within the underground garage. The specific parameters at the leakage point are presented in Table 1. The simulated conditions for this study are outlined in Table 2.
Table 1. Summary of hydrogen leakage port parameters.
Parameter Actual leakage port Virtual nozzle Diameter (mm) 2 21.8 Velocity (m/s) 1369.3 2217.9 Temperature (K) 249 300 Pressure (MPa) 18.4 0.101325 Pressure inside the bottle (MPa) 35 Temperature inside the bottle (K) 300 Ambient temperature (K) 300 Ambient pressure (MPa) 0.10325 Table 2. Summary of modelled conditions.
Serial number Parking space
bay patternVentilation mode No. of ventilation openings 1 2 No 0 2 3 No 0 3 4 No 0 4 4 Mechanical ventilation 2 5 4 Mechanical ventilation 4 Numerical method
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In this paper, Fluent software is used to conduct a simulation study on hydrogen leakage and diffusion. During the calculation process, the mass conservation equation, energy conservation equation, momentum conservation equation, and species transport equation are employed to describe the behavior of hydrogen leakage and diffusion[23]. However, since the high-pressure hydrogen leakage studied in this paper also involves turbulent flow, the turbulence control equation must be considered as well. The following are the governing equations involved in this study:
(1) Mass conservation equation
$ \dfrac{\partial \rho }{\partial t}+\dfrac{\partial \left(\rho {u}_{i}\right)}{\partial {x}_{i}}=0 $ (1) where, ui is the component of the velocity vector in the direction of x, y, z, m/s; ρ is the density of the substance, kg/m3.
(2) Energy conservation equation
$\dfrac{\partial \left(\rho T\right)}{\partial t}+\dfrac{\partial \left(\rho {u}_{i}T\right)}{\partial {x}_{i}}=-\dfrac{\partial }{\partial {x}_{i}}\left(\dfrac{k}{{c}_{p}}\frac{\partial T}{\partial {x}_{i}}\right) $ (2) where, cp is the specific heat capacity, J/(kg K); k is the heat transfer coefficient of the fluid; T is the fluid temperature, K.
(3) Momentum conservation equation
$ \dfrac{\partial \left(\rho {u}_{i}\right)}{\partial t}+\dfrac{\partial \left(\rho {u}_{i}{u}_{j}\right)}{\partial {x}_{j}}=-\dfrac{\partial p}{\partial {x}_{i}}+\dfrac{\partial {\tau }_{ji}}{\partial {x}_{j}}+{F}_{i} $ (3) where, p is the pressure, Pa; τji is the component of the viscous force in the x, y, z direction; Fi is the component of the volumetric force in the x, y, z direction.
(4) Component transport equations
$\dfrac{\partial \left(\rho {c}_{s}\right)}{\partial t}+\dfrac{\partial \left(\rho {c}_{s}{u}_{i}\right)}{\partial {x}_{i}}=\dfrac{\partial }{\partial {x}_{i}}\left[{D}_{s}\dfrac{\partial \left(\rho {c}_{s}\right)}{\partial {x}_{i}}\right] $ (4) Where, cs is the volume fraction of component s; Ds is the diffusion coefficient of component s.
(5) Turbulence modelling
Currently, the widely used numerical simulation methods for turbulence can be classified into DNS (Direct Numerical Simulation), LES (Large Eddy Simulation), and RANS (Reynolds-Averaged Navier-Stokes). Compared to DNS and LES, RANS requires significantly fewer computational resources such as processor and memory, and it can significantly reduce the computation time. Therefore, RANS is widely used in practical engineering applications. The turbulence model adopted in this paper is the Realizable
model under RANS, which is suitable for complex flows such as round jet flows and rotating shear flows, and can be effectively applied to the simulation of various flow types[24]. In this model, turbulent kinetic energy k and turbulent dissipation rate ε are the two basic unknowns and the corresponding transport equations are as follows:$k-\epsilon $ $ \dfrac{\partial \left(\rho k\right)}{\partial t}+\dfrac{\partial \left(\rho k{u}_{i}\right)}{\partial {x}_{i}}=\dfrac{\partial }{\partial {x}_{j}}\left[\left(\mu +\dfrac{{\mu }_{t}}{{\sigma }_{k}}\right)\dfrac{\partial k}{\partial {x}_{j}}\right]+{G}_{k}-\rho \varepsilon $ (5) $ \dfrac{\partial \left(\rho \varepsilon \right)}{\partial t}+\dfrac{\partial \left(\rho \varepsilon {u}_{i}\right)}{\partial {x}_{i}}=\dfrac{\partial }{\partial {x}_{j}}\left[\left(\mu +\dfrac{{\mu }_{t}}{{\sigma }_{\varepsilon }}\right)\dfrac{\partial \varepsilon }{\partial {x}_{j}}\right]+\rho {C}_{1}E\varepsilon -\rho {C}_{2}\dfrac{{\varepsilon }^{2}}{k+\sqrt{\nu \varepsilon }} $ (6) where, μt is the turbulent viscosity; Gk is the generation term of turbulent kinetic energy k induced by the mean velocity gradient; σk and σε are the Prandtl numbers corresponding to the turbulent kinetic energy k and the turbulent dissipation rate ε, which are taken as 1.0 and 1.2, respectively; and C1 and C2 are the empirical constants, which are taken as 1.44 and 1.92, respectively.
The basic governing equations can be simplified based on several assumptions, which are outlined in this paper[25] as follows:
(1) Hydrogen is released at a constant leakage rate;
(2) No chemical reactions or phase changes occur after hydrogen leakage;
(3) The walls of the underground garage are isothermal, adiabatic, and smooth.
Boundary conditions, initial conditions, and meshing settings
Inlet boundary conditions
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The inlet boundary is set as a mass flow inlet for hydrogen. Pure hydrogen is specified at the inlet, with a hydrogen mass flow rate calculated by the model as 0.0678 kg/s. The leakage direction at the inlet is set perpendicular to the inlet surface. When ventilation conditions are added, the supply air inlet is set as a velocity inlet with a magnitude of 3 m/s, and the velocity direction is set perpendicular to the inlet surface.
Outlet boundary conditions
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The underground garage door studied in this paper is set as a pressure outlet boundary condition with a gauge pressure of 0. When ventilation is added, the exhaust outlet is also set as a pressure outlet boundary condition.
Wall boundary conditions
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The walls, beams, columns, and surfaces of hydrogen fuel cell vehicles in the underground garage are all set as solid walls, adopting no-slip and no-mass penetration conditions.
Initial conditions
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The simulation uses a pressure-based transient solver, with a time step interval set to 0.1 s. For all simulations, the Semi-Implicit Method for Pressure Linked Equations (SIMPLE) method and second-order spatial discretization are used. The gravitational acceleration is −9.81 m/s2, and the ambient temperature and pressure in the underground garage are 300 K and 1.01325 × 105 Pa, respectively. Additionally, the total hydrogen leakage time is set to 74 s.
Mesh generation
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This paper uses SpaceClaim under the WorkBench platform for 3D modeling. Considering the large spatial domain and small leakage port in this simulation, it is necessary to locally refine the mesh at the leakage port, the ceiling above the leakage port, ventilation ports, and garage doors to improve mesh quality and calculation accuracy. The fluid domain is divided into tetrahedral meshes with a minimum length set to 0.01 and a maximum length set to 0.1. After a mesh independence test, a mesh size of 700,000 is selected for subsequent calculation and simulation. Figure 3 shows the overall mesh and locally refined mesh diagrams of the underground garage in 4-parking space, 3-parking space, and 2-parking space bay modes, respectively.
Figure 3.
Schematic diagram of grid division and local encrypted grid for underground garage with different parking space modes.
Validation of the accuracy of the numerical model
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To verify the accuracy of the CFD model and method, this paper constructs a geometric model based on the experiment conducted by Pitts et al.[26], proceeds with simulations, and finally compares the simulation results with experimental data.
As shown in Fig. 4, Pitts et al.[26] built a garage model with dimensions of 6.10 m × 6.10 m × 3.05 m. There is a closed door with a width of 2.4 m and a height of 2.1 m on the front of the model. Two ventilation ports, each with dimensions of 0.2 m × 0.2 m, are located 2.3 m from the right side of the model. A square hydrogen leak source with dimensions of 0.305 m × 0.305 m × 0.15 m is placed at the center of the model and is connected to an external hydrogen storage cylinder. The external hydrogen cylinder supplies hydrogen at a uniform rate of 83.3 g/min, with a leakage duration of 3600 s. Two sensors are placed inside the garage to measure hydrogen concentration, located at (0, 2.44, 0.76) and (0, 2.44, 3.05), respectively.
To quickly generate the mesh and improve computational efficiency, the computational domain of the garage is divided into tetrahedral meshes and local refinement is applied to the leak source, ventilation ports, as well as horizontal and vertical directions of the leak source. This is done to enhance mesh quality and calculation accuracy. After a mesh independence test, a final mesh count of 640,000 is determined. The geometric model of the garage and the mesh division are shown in Fig. 5.
As can be seen from Fig. 6, the change curve of hydrogen mole fraction obtained from numerical simulation is consistent with the experimental data in trend and roughly similar in data, reflecting the characteristic that the hydrogen concentration is higher at higher locations. The error is within an acceptable range. Therefore, it can be considered that the use of CFD software for numerical simulation of hydrogen leakage scenarios in the garage matches well with the actual situation, indicating that this method is effective and feasible.
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Thanks to the two teachers and senior fellow for their advice and help in the process of writing this paper, thanks to each person who provided help in publishing this paper.
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About this article
Cite this article
Cui P, Tao G, Zhang L, Zhao C. 2024. Numerical simulation of hydrogen leakage diffusion in a small underground garage with different parking space modes. Emergency Management Science and Technology 4: e022 doi: 10.48130/emst-0024-0024
Numerical simulation of hydrogen leakage diffusion in a small underground garage with different parking space modes
- Received: 24 July 2024
- Revised: 28 September 2024
- Accepted: 08 October 2024
- Published online: 30 October 2024
Abstract: In recent years, hydrogen energy has been widely applied in various industries, but it may also bring a series of safety concerns. Especially in confined spaces like underground garages, where high-pressure hydrogen leaks can potentially cause combustion or explosions. To address this, this paper integrates numerical calculations and theoretical analysis to simulate the process of continuous high-pressure hydrogen leakage from hydrogen-powered vehicles within underground garages. Through investigating the influence of various parking space modes and the number of ventilation openings under mechanical ventilation conditions on hydrogen diffusion and distribution, it was discovered that, during the initial stages of leakage, the 2-parking space mode exhibited a slightly higher overall explosion risk in comparison to the 3- and 4-parking space modes. Notably, after 15 s, the 4-parking space mode shows the highest global explosion risk, while the 2-parking space mode consistently demonstrates the highest local explosion risk in the overhead space. Under mechanical ventilation, the number of ventilation openings significantly reduces hydrogen concentration over time. Specifically, after leakage cessation, increasing ventilation openings efficiently shortens the time required for hydrogen levels to drop to safe limits within the garage. The findings of this study can provide important references for the safety design of hydrogen fuel cell vehicle garages.
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Key words:
- Underground garage /
- Columns /
- Beams /
- Hydrogen leakage and diffusion /
- Mechanical ventilation /
- Numerical simulation