Abstract
The outflow depth from the radial porous media (inflow to the well) is very useful as the downstream boundary condition and the starting point for water surface profile calculations. Based on the studies, unlike the Stephenson's hypothesis (the outflow depth is equal to the critical depth), the outflow depth from the rockfill media is a coefficient (Γ) of the critical depth. In the present study, using several (large scale and almost real) experimental data in the radial non-Darcy flow condition, dimensional analysis and the particle swarm optimization (PSO) algorithm, an equation was presented to calculate the mentioned coefficient based on upstream water depth (h) and distance between the well center and the upstream (R). Then, using the calculated outflow depth and the 1D flow analysis equations, the water surface profile in the radial non-Darcy condition was calculated for the first time. The results showed that considering an outflow depth equal to the critical depth and using the proposed solution in the present study, the mean relative error (MRE) values of 83.43% and 3.53% were obtained, respectively. In addition, using the proposed solution for different experimental conditions, an average MRE of 2.58% was calculated for the water surface profile.
HIGHLIGHTS
Using the experimental data with almost real scale.
Calculation of the output flow depth from the radial porous media.
Providing a relationship based on the upstream water depth (h) and the distance of well center from upstream (R) to calculate the output flow depth.
Calculation of water surface profile in radial non-Darcy flow using gradually varied flow theory.
Using PSO algorithm in calculations.
INTRODUCTION
Flow through coarse-grained porous media is classified into parallel flows (such as flow through rockfill dams, gabions, etc.) and radial flows (convergent) (such as flow near drilled wells in coarse-grained alluvial beds, groundwater, etc.). Both types exist in the form of free and pressured flows. An example of radial flows is flow near wells drilled in coarse-grained alluvial beds and aquifers. Groundwater is one of the sources of water storage in the world (Jamie et al. 2019). Groundwater resources can be achieved using drilled deep and semi-deep wells, springs and aqueducts (Akbarpour 2016). Investigation of water flow in the above mentioned cases is very important to evaluate the volume of water that can be exploited from aquifers.
Steady non-Darcy flow is studied using one-dimensional (1D) analysis (gradually varied flow theory) and two-dimensional (2D) analysis (Parkin equation). The governing equations on radial non-Darcy flow (combination of continuity equation in cylindrical coordinates and power equation between hydraulic gradient and flow velocity) are solved using numerical methods of finite differences, finite elements and finite volumes (Sadeghian 2013). Solving the mentioned equations requires boundary conditions and a lot of data and is therefore massive, time consuming and costly. However, gradually varied flow theory requires much less data and is easier and less expensive. (Bari & Hansen 2002) studied non-Darcy flows using the standard step method. Bazargan & Shoaei (2010) studied non-Darcy steady flow using the gradually varied flows theory. Gudarzi et al. (2020) studied the effect of drag force on the accuracy of water surface profile calculations passing through coarse-grained porous media using the gradually varied flows theory. Sadeghian et al. (2013) evaluated the binomial and power equations in calculating the changes in hydraulic gradient based on the flow velocity in the free surface radial flow. Shayannejad & Ebrahimi (2020) proposed an equation between discharge and hydraulic potential in the radial flow of free aquifers using the fractional derivative of the flow velocity relative to the hydraulic gradient under steady state conditions. Venkataraman & Rao (2000) studied the binomial equation in convergent pressured flows and proposed the modified coefficients a and b. Many researchers (Ward 1964; Ahmed & Sunada 1969; Sedghi-Asl & Ansari 2016; Norouzi et al. 2022a) studied parallel non-Darcy flows and few studies have been done on radial non-Darcy flows in the free-surface case. In order to use the binomial equation to calculate the changes in the hydraulic gradient based on the flow velocity in the radial flow case, the coefficients a and b of the parallel flow need to be corrected (Venkataraman & Rao 2000). Whereas the coefficients m and n in the power equation need no corrections and the same values can be used in both parallel and radial flows using optimization, and have better performance in the non-Darcy radial case (Sadeghian et al. 2013). For this reason, the power equation is preferred to the binomial equation in the case of radial non-Darcy flow.
Particle swarm optimization (PSO) algorithm is a population-based evolutionary algorithm and is used in civil engineering and water resources optimization problems such as reservoir performance (Nagesh Kumar & Janga Reddy 2007), water quality management (Lu et al. 2002; Chau 2005; Afshar et al. 2011), optimization of the Muskingum method coefficients (Chu & Chang 2009; Moghaddam et al. 2016; Bazargan & Norouzi 2018; Norouzi & Bazargan 2020; Norouzi & Bazargan 2021) and optimization of the parameters of the porous media equations (Norouzi et al. 2022a; Safarian et al. 2021).
For this reason, in the present study, the PSO algorithm was used to optimize the power equation coefficients (m, n) and the coefficient of the presented equation to calculate the output flow depth. Calculation of the water surface profile (1D flow analysis using the gradually varied flows theory) and the depth of the output radial flow from the coarse-grained porous media (the input flow depth to the well) is of great importance as the starting point of the 1D analysis of steady flow calculations. In addition, water surface profile and outflow depth is widely used as the boundary condition in the 2D analysis of steady non-Darcy flow (solving Parkin equation) and to study the flow passing through the gravel media. According to previous studies and literature review, the outflow depth in radial non-Darcy flow condition is not equal to the critical depth. In the present study, for the first time, large-scale (almost real) experimental data, dimensional analysis and PSO algorithm was used to present an equation to calculate the outflow depth from the radial coarse-grained porous media. Then, using the exponential equation of hydraulic gradient changes in terms of the flow velocity (Equation (3), coefficients m and n of which were optimized using the PSO algorithm), the gradually varied flows theory and the calculated outflow depth as the starting point of calculations, the water surface profile was calculated for different experimental data with appropriate accuracy.
MATERIALS AND METHODS
Experimental data
Flow characteristics and water surface profile recorded in the laboratory
Radius (cm) . | Height of pumped water (cm) . | |||||||||
---|---|---|---|---|---|---|---|---|---|---|
53 . | 60 . | 70 . | 85 . | 95 . | 110 . | 120 . | 140 . | 150 . | 160 . | |
Discharge (L/s) . | ||||||||||
50.03 . | 49.94 . | 50.38 . | 50.95 . | 51.24 . | 53.16 . | 52.22 . | 52.80 . | 52.68 . | 52.95 . | |
Water surface profiles (cm) . | ||||||||||
25 | 415 | 535 | 655 | 813 | 934 | 1,085 | 1,180 | 1,386 | 1,488 | 1,593 |
50 | 476 | 563 | 675 | 831 | 944 | 1,094 | 1,189 | 1,393 | 1,493 | 1,598 |
75 | 491 | 575 | 683 | 839 | 947 | 1,097 | 1,192 | 1,396 | 1,495 | 1,600 |
105 | 494 | 584 | 689 | 845 | 949 | 1,099 | 1,194 | 1,399 | 1,497 | 1,602 |
140 | 494 | 591 | 693 | 849 | 951 | 1,101 | 1,196 | 1,400 | 1,498 | 1,603 |
180 | 507 | 596 | 697 | 853 | 953 | 1,103 | 1,198 | 1,402 | 1,499 | 1,604 |
225 | 516 | 601 | 700 | 856 | 954 | 1,104 | 1,199 | 1,403 | 1,499 | 1,604 |
275 | 522 | 605 | 702 | 859 | 955 | 1,105 | 1,200 | 1,404 | 1,500 | 1,605 |
Radius (cm) . | Height of pumped water (cm) . | |||||||||
---|---|---|---|---|---|---|---|---|---|---|
53 . | 60 . | 70 . | 85 . | 95 . | 110 . | 120 . | 140 . | 150 . | 160 . | |
Discharge (L/s) . | ||||||||||
50.03 . | 49.94 . | 50.38 . | 50.95 . | 51.24 . | 53.16 . | 52.22 . | 52.80 . | 52.68 . | 52.95 . | |
Water surface profiles (cm) . | ||||||||||
25 | 415 | 535 | 655 | 813 | 934 | 1,085 | 1,180 | 1,386 | 1,488 | 1,593 |
50 | 476 | 563 | 675 | 831 | 944 | 1,094 | 1,189 | 1,393 | 1,493 | 1,598 |
75 | 491 | 575 | 683 | 839 | 947 | 1,097 | 1,192 | 1,396 | 1,495 | 1,600 |
105 | 494 | 584 | 689 | 845 | 949 | 1,099 | 1,194 | 1,399 | 1,497 | 1,602 |
140 | 494 | 591 | 693 | 849 | 951 | 1,101 | 1,196 | 1,400 | 1,498 | 1,603 |
180 | 507 | 596 | 697 | 853 | 953 | 1,103 | 1,198 | 1,402 | 1,499 | 1,604 |
225 | 516 | 601 | 700 | 856 | 954 | 1,104 | 1,199 | 1,403 | 1,499 | 1,604 |
275 | 522 | 605 | 702 | 859 | 955 | 1,105 | 1,200 | 1,404 | 1,500 | 1,605 |
Different parts of the experimental device: (a) schematic view of experimental model, (b) front view of experimental model, and (c) placement of parallel pumps on the model.
Different parts of the experimental device: (a) schematic view of experimental model, (b) front view of experimental model, and (c) placement of parallel pumps on the model.
Depth of output flow from the rockfill media
In the previous studies, values of Γ were calibrated by different researchers using experimental data. Using such data, Sedghi-Asl et al. (2010) obtained the value of Γ coefficient for the angular and rounded materials as 2.3 and 2.4, respectively. There is no doubt that Γ value for open channels which lack rockfill materials is equal to 1. In other words, the difference between values of Γ is due to the fact that in the angular materials, porosity of media is more than the rounded ones and is closer to 1, which is the same as the porosity of open channels (Sedghi-Asl et al. 2010). In another study, Chabokpour & Tokaldani (2018) used their own experimental data and obtained the value of Γ coefficient for a length of 100 cm as 1.83 and 2.05 for aggregate diameters of 16 and 30 mm, respectively; and for a length of 193 cm as 1.58 and 1.84, respectively, considering the same aggregate diameters. Norouzi et al. (2022b) used experimental data in different conditions as well as PSO algorithm and dimensional analysis to present an equation to calculate the coefficient based on the physical properties of the aggregates and parallel flow characteristics in rockfill media.
In the present study, using the mentioned experimental data, dimensional analysis and PSO algorithm, an equation was presented to calculate the coefficient in the case of radial non-Darcy flow.
Gradually varied flows theory

Given the above equation, flow depth at a point must be available to start the calculations. According to the solution presented in the present study to calculate the depth of the output flow from the porous media, the calculations started from downstream (output flow from the radial media or input flow to the well).
Particle Swarm Optimization (PSO) algorithm
This algorithm was first developed and introduced by (Eberhart & Kennedy 1995). PSO is a population-based searching algorithm that is inspired by the nature like Genetic Algorithm (GA), Ant Colony and Artificial Bee Colony and is developed based on the collective intelligence and social behavior of the bird flocking or fish schooling. The advantages of this algorithm include simplicity of the structure and implementation, small number of controllable parameters, high convergence speed and high computational efficiency. The basic idea of PSO is based on the assumption that potential solutions are flown through hyperspace with acceleration towards more optimum solutions. Each particle adjusts its flying according to the experiences of both itself and its companions. During the process, the overall best value attained by all the particles within the group and the coordinates of each element in hyperspace associated with its previous best fitness solution are recorded in the memory (Chau 2007; Nagesh Kumar & Janga Reddy 2007).
Efficiency, high convergence speed and proper accuracy of the PSO algorithm have been examined and approved in previous studies. Therefore, the PSO algorithm was selected to optimize the coefficients of the power equation (m, n), and coefficients of the proposed equation. The details of PSO can be obtained elsewhere (Clerc & Kennedy 2002; Gurarslan & Karahan 2011; Karahan 2012; Di Cesare et al. 2015).


RESULTS AND DISCUSSION
The present study consisted of the following stages:
- 1.
Assuming an output flow depth from the radial porous media equal to the critical depth (Equation (4)):
According to the hypothesis by Stephenson (1979), the depth of the output flow from the rockfill media is equal to the critical depth. A review of studies conducted on parallel non-Darcy flow indicated that the output flow depth in this case is significantly different from the critical depth. The studies conducted in the present study in the case of radial non-Darcy flow also indicated this inaccuracy of the mentioned equation.
- 2.
Using Equation (5) to calculate the depth of the output flow from the radial porous media:
According to previous studies, the output flow depth in the case of non-Darcy flow is a coefficient (
) of critical depth. In the present study, using large-scale (almost real) experimental data, dimensional analysis and PSO algorithm, an equation was presented based on upstream flow depth (h) and the distance between the center of the well and upstream (R) to calculate
and, consequently, the output flow depth from the radial non-Darcy media.
- 3.
Calculation of coefficients m and n of the power equation:
The calculation of hydraulic gradient changes (i) based on the flow velocity (V), which indicates the nonlinearity of the flow passing through the coarse-grained porous media, is of great importance in the 1D and 2D analyzes of the steady flow. In the case of radial non-Darcy flow, the power equation (Equation (3)) is more efficient than the binomial equation (Equation (2)) (Sadeghian et al. 2013). In the present study, using the PSO algorithm, the coefficients m and n of the power equation were optimized for 10 different upstream pumped depths.
- 4.
One-dimensional analysis of radial non-Darcy flow in steady flow case:
Calculation of water surface profile is widely used to study flow through the radial non-Darcy media and also as the main boundary condition in 2D analysis of the mentioned flow. To use the theory of gradually varied flow, the flow depth at a point is needed to start the calculations. The depth of the output flow from the porous media (input depth to the well), which is calculated using the solution presented in step (2), is the starting point of the calculations. In other words, in the present study, using computational output flow depth, 1D flow analysis was started from downstream of the coarse-grained porous media.
Depth of output flow from the porous media in the case of radial flow
Changes in experimental output flow depth and critical depth versus flow discharge.
Changes in experimental output flow depth and critical depth versus flow discharge.

Using the PSO algorithm, the value of the J coefficient was optimized as 20.75. In other words, the value of the J coefficient was optimized so that the computational and observational (recorded in the laboratory) output flow depths would be as consistent as possible.

Changes in the observational and computational output flow depths versus flow discharge (using the solution presented in the present study).
Changes in the observational and computational output flow depths versus flow discharge (using the solution presented in the present study).
The values of discharge, observational and computational output flow depths and critical depths are listed in Table 2.
Observational and computational values of the output flow depths
Height of pumped water (cm) . | Q (L/s) . | Output water depth (cm) . | ||
---|---|---|---|---|
Experimental . | Critical . | Computed . | ||
53 | 50.03 | 41.5 | 13.72 | 50.3 |
60 | 49.94 | 53.5 | 13.71 | 56.9 |
70 | 50.38 | 65.5 | 13.79 | 66.8 |
85 | 50.95 | 81.3 | 13.89 | 81.7 |
95 | 51.24 | 93.4 | 13.95 | 91.6 |
110 | 53.16 | 108.5 | 14.29 | 108.7 |
120 | 52.22 | 118 | 14.12 | 117.2 |
140 | 52.80 | 138.6 | 14.23 | 137.8 |
150 | 52.68 | 148.8 | 14.21 | 147.4 |
160 | 52.95 | 159.3 | 14.25 | 157.7 |
MRE % | 83.43 | 3.83 |
Height of pumped water (cm) . | Q (L/s) . | Output water depth (cm) . | ||
---|---|---|---|---|
Experimental . | Critical . | Computed . | ||
53 | 50.03 | 41.5 | 13.72 | 50.3 |
60 | 49.94 | 53.5 | 13.71 | 56.9 |
70 | 50.38 | 65.5 | 13.79 | 66.8 |
85 | 50.95 | 81.3 | 13.89 | 81.7 |
95 | 51.24 | 93.4 | 13.95 | 91.6 |
110 | 53.16 | 108.5 | 14.29 | 108.7 |
120 | 52.22 | 118 | 14.12 | 117.2 |
140 | 52.80 | 138.6 | 14.23 | 137.8 |
150 | 52.68 | 148.8 | 14.21 | 147.4 |
160 | 52.95 | 159.3 | 14.25 | 157.7 |
MRE % | 83.43 | 3.83 |
One-dimensional analysis of steady flow in the case of radial non-Darcy flow
Water surface profile calculation is used to study water flow behavior. In addition, with a known water surface profile as the main boundary condition in the 2D analysis of steady flow (solving the Parkin equation), upstream and downstream boundary conditions will also be available. For this reason, in the present study, using large-scale (almost real) experimental data and the theory of gradually varied flow, the water surface profile in the case of radial non-Darcy flow was calculated. It is worth mentioning that in previous studies, the theory of gradually varied flow was used in calculating the water surface profile in the case of parallel non-Darcy flow. In order to calculate the water surface profile, using the experimental data for different upstream pumping heights and the PSO algorithm, the coefficients m and n of the power equation were first optimized. Then, using optimized coefficients and the equations of the gradually varied flow theory and the calculated values of the output flow depth (calculated values in Table 2 in the case of using the solution presented in the present study), the water surface profile calculations in the case of radial non-Darcy flow were done from downstream (entering the well). The optimized values of the coefficients m and n are given in Table 3. The observational and computational values of water surface profile and the MRE are also shown in Table 4.
The values of the coefficients m and n of the power equation for the different upstream pumped heights
Height of pumped water (cm) . | m (s/m) . | n (–) . |
---|---|---|
53 | 2.481 | 1.274 |
60 | 2.039 | 1.220 |
70 | 3.453 | 1.444 |
85 | 2.633 | 1.279 |
95 | 0.996 | 1.248 |
110 | 1.157 | 1.251 |
120 | 1.324 | 1.253 |
140 | 2.861 | 1,399 |
150 | 3.202 | 1.503 |
160 | 3.547 | 1.504 |
Height of pumped water (cm) . | m (s/m) . | n (–) . |
---|---|---|
53 | 2.481 | 1.274 |
60 | 2.039 | 1.220 |
70 | 3.453 | 1.444 |
85 | 2.633 | 1.279 |
95 | 0.996 | 1.248 |
110 | 1.157 | 1.251 |
120 | 1.324 | 1.253 |
140 | 2.861 | 1,399 |
150 | 3.202 | 1.503 |
160 | 3.547 | 1.504 |
Computational and observational (experimental) values of water surface profile
Radius (m) . | Height of pumped water (cm) . | |||||||||
---|---|---|---|---|---|---|---|---|---|---|
53 . | 60 . | 70 . | 85 . | 95 . | ||||||
. | . | Discharge (L/s) . | . | . | ||||||
50.03 . | 49.94 . | 50.38 . | 50.95 . | 51.24 . | ||||||
Observed . | Computed . | Observed . | Computed . | Observed . | Computed . | Observed . | Computed . | Observed . | Computed . | |
0.25 | 0.415 | 0.503 | 0.535 | 0.569 | 0.655 | 0.668 | 0.813 | 0.817 | 0.934 | 0.916 |
0.5 | 0.476 | 0.534 | 0.563 | 0.594 | 0.675 | 0.688 | 0.831 | 0.835 | 0.944 | 0.923 |
0.75 | 0.491 | 0.548 | 0.575 | 0.606 | 0.683 | 0.696 | 0.839 | 0.843 | 0.947 | 0.926 |
105 | 0.494 | 0.558 | 0.584 | 0.614 | 0.689 | 0.702 | 0.845 | 0.849 | 0.949 | 0.928 |
1.4 | 0.494 | 0.565 | 0.591 | 0.621 | 0.693 | 0.706 | 0.849 | 0.854 | 0.951 | 0.929 |
1.8 | 0.507 | 0.571 | 0.596 | 0.626 | 0.697 | 0.709 | 0.853 | 0.858 | 0.953 | 0.931 |
2.25 | 0.516 | 0.576 | 0.601 | 0.631 | 0.700 | 0.711 | 0.856 | 0.861 | 0.954 | 0.933 |
2.75 | 0.522 | 0.579 | 0.605 | 0.634 | 0.702 | 0.713 | 0.859 | 0.863 | 0.955 | 0.934 |
MRE% | 12.56 | 5.29 | 1.80 | 0.54 | 2.19 | |||||
Radius (m) . | Height of pumped water (cm) . | |||||||||
110 . | 120 . | 140 . | 150 . | 160 . | ||||||
. | . | Discharge (L/s) . | . | . | ||||||
53.16 . | 52.22 . | 52.80 . | 52.68 . | 52.95 . | ||||||
Observed . | Computed . | Observed . | Computed . | Observed . | Computed . | Observed . | Computed . | Observed . | Computed . | |
0.25 | 1.085 | 1.087 | 1.18 | 1.172 | 1.386 | 1.378 | 1.488 | 1.474 | 1.593 | 1.577 |
0.5 | 1.094 | 1.093 | 1.189 | 1.178 | 1.393 | 1.385 | 1.493 | 1.479 | 1.598 | 1.582 |
0.75 | 1.097 | 1.096 | 1.192 | 1.181 | 1.396 | 1.388 | 1.495 | 1.481 | 1.600 | 1.584 |
105 | 1.099 | 1.099 | 1.194 | 1.184 | 1.399 | 1.390 | 1.497 | 1.483 | 1.602 | 1.586 |
1.4 | 1.101 | 1.100 | 1.196 | 1.186 | 1.400 | 1.392 | 1.498 | 1.484 | 1.603 | 1.587 |
1.8 | 1.103 | 1.102 | 1.198 | 1.187 | 1.402 | 1.393 | 1.499 | 1.485 | 1.604 | 1.588 |
2.25 | 1.104 | 1.103 | 1.199 | 1.188 | 1.403 | 1.394 | 1.499 | 1.485 | 1.604 | 1.588 |
2.75 | 1.105 | 1.104 | 1.200 | 1.189 | 1.404 | 1.395 | 1.500 | 1.486 | 1.605 | 1.589 |
MRE% | 0.07 | 0.85 | 0.58 | 0.94 | 1.00 |
Radius (m) . | Height of pumped water (cm) . | |||||||||
---|---|---|---|---|---|---|---|---|---|---|
53 . | 60 . | 70 . | 85 . | 95 . | ||||||
. | . | Discharge (L/s) . | . | . | ||||||
50.03 . | 49.94 . | 50.38 . | 50.95 . | 51.24 . | ||||||
Observed . | Computed . | Observed . | Computed . | Observed . | Computed . | Observed . | Computed . | Observed . | Computed . | |
0.25 | 0.415 | 0.503 | 0.535 | 0.569 | 0.655 | 0.668 | 0.813 | 0.817 | 0.934 | 0.916 |
0.5 | 0.476 | 0.534 | 0.563 | 0.594 | 0.675 | 0.688 | 0.831 | 0.835 | 0.944 | 0.923 |
0.75 | 0.491 | 0.548 | 0.575 | 0.606 | 0.683 | 0.696 | 0.839 | 0.843 | 0.947 | 0.926 |
105 | 0.494 | 0.558 | 0.584 | 0.614 | 0.689 | 0.702 | 0.845 | 0.849 | 0.949 | 0.928 |
1.4 | 0.494 | 0.565 | 0.591 | 0.621 | 0.693 | 0.706 | 0.849 | 0.854 | 0.951 | 0.929 |
1.8 | 0.507 | 0.571 | 0.596 | 0.626 | 0.697 | 0.709 | 0.853 | 0.858 | 0.953 | 0.931 |
2.25 | 0.516 | 0.576 | 0.601 | 0.631 | 0.700 | 0.711 | 0.856 | 0.861 | 0.954 | 0.933 |
2.75 | 0.522 | 0.579 | 0.605 | 0.634 | 0.702 | 0.713 | 0.859 | 0.863 | 0.955 | 0.934 |
MRE% | 12.56 | 5.29 | 1.80 | 0.54 | 2.19 | |||||
Radius (m) . | Height of pumped water (cm) . | |||||||||
110 . | 120 . | 140 . | 150 . | 160 . | ||||||
. | . | Discharge (L/s) . | . | . | ||||||
53.16 . | 52.22 . | 52.80 . | 52.68 . | 52.95 . | ||||||
Observed . | Computed . | Observed . | Computed . | Observed . | Computed . | Observed . | Computed . | Observed . | Computed . | |
0.25 | 1.085 | 1.087 | 1.18 | 1.172 | 1.386 | 1.378 | 1.488 | 1.474 | 1.593 | 1.577 |
0.5 | 1.094 | 1.093 | 1.189 | 1.178 | 1.393 | 1.385 | 1.493 | 1.479 | 1.598 | 1.582 |
0.75 | 1.097 | 1.096 | 1.192 | 1.181 | 1.396 | 1.388 | 1.495 | 1.481 | 1.600 | 1.584 |
105 | 1.099 | 1.099 | 1.194 | 1.184 | 1.399 | 1.390 | 1.497 | 1.483 | 1.602 | 1.586 |
1.4 | 1.101 | 1.100 | 1.196 | 1.186 | 1.400 | 1.392 | 1.498 | 1.484 | 1.603 | 1.587 |
1.8 | 1.103 | 1.102 | 1.198 | 1.187 | 1.402 | 1.393 | 1.499 | 1.485 | 1.604 | 1.588 |
2.25 | 1.104 | 1.103 | 1.199 | 1.188 | 1.403 | 1.394 | 1.499 | 1.485 | 1.604 | 1.588 |
2.75 | 1.105 | 1.104 | 1.200 | 1.189 | 1.404 | 1.395 | 1.500 | 1.486 | 1.605 | 1.589 |
MRE% | 0.07 | 0.85 | 0.58 | 0.94 | 1.00 |
According to Table 4, for the heights of the pumped water upstream equal to 53, 60, 70, 85, 95, 110, 120, 140, 150 and 160 cm, MRE values for the calculated and observed water surface profiles were calculated as 12.56, 5.29, 1.80, 0.54, 2.19, 0.07, 0.85, 0.58, 0.94 and 1%, respectively. In other words, the theory of gradually varied flow in the 1D analysis of steady flow in the case of radial non-Darcy flow is accurate and efficient enough.
CONCLUSIONS
Calculation of the water surface profile and the outflow depth from the porous media in the steady-radial condition is widely used in 1D and 2D flow analysis. In the present study, using large-scale (almost real) experimental data (large-scale semi-cylindrical test device with a diameter of 6 m and a height of 3 m considering 10 different pumped water heights in upstream of the rockfill media), first by using dimensional analysis and the PSO algorithm, the coefficient (the ratio between the outflow depth from the rockfill media and the critical depth) was optimized as a function of the upstream water depth (h) and the distance between the well center and the upstream (R). Then, using the optimized m and n coefficients using the PSO algorithm, the calculated depth of the outflow (the starting point of the calculations) and the gradually varied flows theory, the water surface profile of the steady flow in the radial non-Darcy condition was calculated. The results showed that the MRE of the calculated outflow depth from the radial porous media using the proposed solution improved by 95.8% compared to the case of assuming an outflow depth equal to the critical depth. In addition, the average MRE for 10 different depths of pumped water in the upstream of the rockfill media was calculated as 2.58%. In other words, the solution presented in the present study is suitably accurate in the analysis of steady flow in radial non-Darcy condition.
DATA AVAILABILITY STATEMENT
All relevant data are included in the paper or its Supplementary Information.
CONFLICT OF INTEREST
The authors declare there is no conflict.