2.2.2. Computational Domain and Meshes
The computational domain replicating the experimental setup was simulated using ANSYS-Fluent (release 2016, ANSYS, Canonsburg, PA, USA). This study used the three-dimensional (3D) steady-state method to solve the governing equations.
As shown in
Figure 4, this study established a 3D geometric model of the experimental greenhouse, which took the southwest corner of the greenhouse as the coordinate origin (0,0,0), the east–west direction as the transverse direction (span direction), the north–south direction as the longitudinal direction (depth direction), the depth direction of the greenhouse as the
y-axis positive direction, the span direction of the greenhouse as the
x-axis positive direction, the height direction of the greenhouse as the
z-axis positive direction, and the top window opening angle as a maximum of 45°.
As shown in
Figure 5, the greenhouse was located at the center of the external flow field, and the ground center points of the two fields coincided. The length of the external watershed was 10 times larger than the greenhouse building to ensure full development of the fluid flow process [
13]. The size of the inner flow field was 72 m (L) × 72 m (W) × 7.9 m (H), and the size of the outer flow field was 792 m (L) × 232 m (W) × 48 m (H) under natural ventilation.
Considering the irregularity of the top structure of the greenhouse, this study used ICEM to divide the computational domain into unstructured grids, increase the density of the grid on the vent and wall of the greenhouse, and carry out photocoagulation treatment.
After pre-experiments, the number of grids generated was 7,130,172, the number of grid nodes was 1,162,296, the grid had no negative volume, and the grid quality was greater than 0.3. As shown in
Figure 6, the grid division of the greenhouse model under natural ventilation was determined.
2.2.3. Governing Equations
The airflow in the greenhouse is a low-speed flow field at room temperature, which can be regarded as an incompressible fluid [
14], and its transport process satisfies the governing equation in Equation (3):
In Equation (3), is the fluid density, is the velocity vector of , is the generalized diffusion coefficient, and is the source item.
The continuity equation is given by Equation (4) when
, where
is the source item of mass.
The momentum equation is given by Equations (5)–(7) when
, where
,
and
are the source items of momentum.
The energy equation is given by Equation (8) when
, where T is the temperature of the airflow in the greenhouse and p is the air pressure in the greenhouse.
In Equation (8),
is effective thermal conductivity given by Equation (9), where
is the turbulent heat transfer coefficient determined by the turbulence model.
In Equations (10) and (11), E is the total energy of the fluid, and h is the total enthalpy of an ideal gas.
In Equation (12),
is the enthalpy of the humid air transport process. And
is given by Equation (13), where
.
2.2.4. Numerical Model
In this study, the heat transfers and airflow in the greenhouse under natural ventilation were considered. The measured wind speed was less than 2.0 m/s, which accorded with the low-speed flow field. The airflow process in the test area was fully developed, the air in the simulated area can be regarded as a steady incompressible fluid, and the airflow conforms to Boussinesq hypothesis. In addition, the flow state of the fluid in the greenhouse was judged by the ratio of the Rayleigh number to the
Prandtl number, which conformed to the turbulent motion form [
6,
9,
14]. The standard
k-ε model was selected to simulate the greenhouse under natural ventilation in Equations (14)–(16).
In Equation (14), is the eddy viscosity coefficient, k is the turbulence fluctuation kinetic energy, is the turbulence dissipation rate, and is the turbulence constant, while in Equations (15) and (16), is the laminar eddy viscosity coefficient, and are empirical constants.
In addition, solar radiation is another important factor affecting the environmental distribution in the greenhouse, and the influence of solar radiation on the microclimate in the greenhouse is closely related to the solar azimuth angle and the geographical position of the greenhouse. In this paper, discrete ordinates (DO) was the radiation model, and the radiation transfer equation is shown in Equation (17).
In Equation (17),
is the solid space angle of direct sunlight, which conforms to Equation (18).
where
is the solar zenith angle,
is the solar azimuth,
is the latitude of the test area,
is the solar declination, and
is the hour angle. In addition,
is calculated by Equation (19).
In Equation (19), N indicates the number of days before January 1st of the current year.
In Equation (17), is the position vector, is the direction vector, is the scattering direction, s is the length along the route, is the absorption coefficient, n is the refractive index, is the scattering coefficient, is the Stefan–Boltzmann constant, I is the radiation intensity which depends on position and direction , T is the local temperature, and are phase functions.
Solar Ray Tracing (SRT) was used to load the solar-load model to calculate the solar radiation intensity, and the Solar Calculator (SC) was used to set the geographical position (109°50′ E, 18°26′ N) and time zone (GMT + 8) of Lingshui area. The trend of the greenhouse was north–south, the due north direction was y-axis positive (0,1,0), and the due east direction was x-axis positive (1,0,0).
2.2.5. Boundary Conditions
Based on the actual physical structure, the distribution of temperature and airflow in the plastic greenhouse with a semi-open roof under natural ventilation was mainly considered. The cover material in the simulation model was 0.15 mm aging-resistant polyethylene film, and the surrounding protective materials were insect-proof nets and general polyethylene film. The physical properties of the greenhouse model are shown in
Table 2.
For the convenience of numerical simulation and considering the computer performance, reasonable assumptions were made after integrating the actual situation of the greenhouse. The temperature of the coating was uniformly distributed, and the heat transfer coefficient was constant. Crops cultivated in the greenhouse model were all in the seedling stage, and the transpiration was minor, ignoring the transpiration of crops in the greenhouse. The evaporation of soil in the greenhouse was ignored. The heat exchange through doors and windows in the greenhouse was not considered. Because of the large size of the experimental greenhouse, the experimental area was a part of the whole greenhouse, so all four sides of the experimental greenhouse were regarded as contacting the outside world.
As shown in
Table 3, the boundary condition parameters of the experimental greenhouse numerical simulation model were set.
In addition, the protective materials around the greenhouse were an insect-proof net and general polyethylene film. The physical characteristics of the insect-proof net are shown in
Table 4.
In the numerical simulation model, the insect-proof net was regarded as a one-dimensional porous medium, which was according to the Porous Jump boundary condition. According to Equation (20), the permeability coefficient K of the insect-proof net was calculated, and the porosity
was obtained from Equation (21), where L denotes the mesh size of the insect-proof net and d denotes the diameter of the insect-proof net line.
2.2.6. Solution of Discrete Differential Equation
In this paper, the differential equation was solved based on the finite volume method, and its discretization format is shown in
Table 5.
In the CFD module, the finite volume method was used to solve the computational domain. And the pressure-based solver was used to solve incompressible fluid flow problems in numerical simulation models. For solving discrete equations, a separate method requires less computation time, while a coupled method consumes a lot of memory, and SIMPLE algorithm is efficient in solving incompressible flow fields, so the SIMPLE algorithm was selected.
In this study, the default convergence standard of the continuity equation and momentum equation in ANSYS was lower than 10
−3, and that of the energy equation was lower than 10
−5. After pre-experiments, the convergence standards were determined as follows: continuity and momentum equations were 10
−5, and the energy equation was 10
−7. The empirical constants in Equations (14) and (16) were set as follows: