This paper describes an experimental and analytical study that examined the effects of soil on leakage rate from defective water pipes. An experimental model was designed and constructed to simulate idealized cracks in defective water pipes discharging into a bed of granular materials. Tests were run on three different materials: LBS-B, LBS-A, and glass ballotini with different characteristics. The results reveal that the presence of bedding material surrounding a leaking pipe causes a significant change in the leakage rate versus free flow conditions. The bedding has a greater impact on larger defect openings. There was a significant drop in the values of the coefficient of discharge (Cd) when the pipe discharged into a soil bed versus free flow conditions; this value was 38% lower for coarse particles and 70% for finer particles. The results also showed that high leakage rates could flow from the defective pipe without fluidization of the bedding materials. An analytical model based on the method of fragments was presented to predict the leakage rate after which the predicted results were compared with values measured experimentally.

  • An analytical model has been presented to predict the leakage rate, in the presence of soil, that provides reasonable estimates of the leakage rate.

  • Soil with different characteristics (permeability, particle size, particle shape, and bed height) was tested.

  • Influence of the surrounding soil on the hydraulic behaviour of leakage was examined.

Leaks in water distribution systems (WDSs) are serious issues that occur on a global scale. A significant volume of water is lost annually from WDSs. This loss amounts to some 126 billion m3 per annum (expressed as non-revenue water) (Liemberger & Wyatt 2019). In some countries, this loss accounts for 40% to 50% of the water supplied compared to an estimated global average of 30% for most systems (Global Water Market 2017). Concurrently, water demand is rising due to population growth, while resources are diminishing (Adedeji et al. 2018). Consequently, understanding the mechanism of leakage and the factors controlling it can play a crucial role in minimizing water scarcity.

Several models have been proposed to model and assess leakage rates from WDSs. Many of these proposed models use the orifice flow equation to simulate leaks (Al-Khomairi 2005; Walski et al. 2006). This equation neglects the effect of soil around water pipes and suggests that leaks vary in proportion to the square root of the head in the pipe (having a leakage exponent of 0.5) as flow:
(1)

Here, q is the flow rate (m3/s), is the discharge coefficient, is the orifice area (m2), g is the acceleration due to gravity (m/s2), and h is the pipe head (m).

Experimental and field research has demonstrated that the leakage exponent may be much more than the 0.5 of the orifice flow equation and typically fluctuates between 0.35 and 2.95 (Farley & Trow 2003; Greyvenstein & van Zyl 2007), thus demonstrating that leaks in WDSs are more pressure sensitive than expected based on the orifice flow equation. The work of van Zyl & Clayton (2007) proposed a number of potential contributing factors to explain the range of leakage exponents found in the literature including pipe material behaviour, leak hydraulics, soil hydraulics, and water demand, but these are not yet fully understood. Changes in the geometry of the unconfined flow regime, piping, and hydraulic fracture have complicated the interactions between leaky pipes and the surrounding soil.

Several studies have attempted to assess the effect of the pipes' surrounding media on leakage rates (Walski et al. 2006; De Paola et al. 2014). Walski et al. (2006) studied orifice/soil interactions in pipe leaking utilizing narrow long tube equipment assuming one-dimensional flow. They studied the two components of head loss that were due to flow through an orifice (ho) and Darcy flow in soil (hs). They then developed a dimensionless ‘orifice/soil’ (OS) number to quantify their significance. Walski et al. (2006) found that ‘in most real-world scenarios, the OS number is large,’ suggesting that orifice head loss is dominant. De Paola et al. (2014) also reached a similar conclusion based on an experimental study in which it was acceptable to neglect the effects of the surrounding soil on the leakage rate. However, other studies indicate that seepage heads may dominate. For example, Burnell & Race (2000) found that leakage from their supply pipes correlated linearly with pipe internal pressure, thus indicating that soil head loss controlled leakage in that instance.

Noack & Ulanicki (2008) quantitatively investigated the influence of soil on leakage characteristics. Their major focus was on soil permeability, and they used 100 different types of soils with hydraulic permeabilities ranging from to m/s. Their findings reveal that the leaking characteristic for high permeability soil (such as sandy soil) is similar to that for discharge to air – namely a square root rule. For low-permeability soil, the exponent rises while the leakage discharge drops. Ćipranić & Sekulić (2015) concluded that the impact of water percolating through the soil cannot be ignored in low-permeability soils.

Fox et al. (2016) investigated the impact of an idealized porous medium on the leaking behaviour of longitudinal slits in viscoelastic tubing. Their results show that the existence of an idealized porous media around the pipe causes a significant increase in the pressure while leading to a reduction in the leakage flow rate versus a free discharge leak. They further highlight the limitations of current dynamic leakage modelling, which simplifies or ignores the impact of soil conditions.

Latifi et al. (2018) also investigated the impact of the soil surrounding the pipe on leakage flow from a 1 mm orifice diameter. They considered different soil types and found that the leakage varied as a function of soil parameters. However, they found no relevant correlation between leakage and certain parameters. They concluded that hydraulic permeability is an important variable in determining the leakage rate.

The soil surrounding the leaking water pipes might be removed as a result of the outlet jet of the leaks, thus resulting in fluidization of the soil bedding (van Zyl et al. 2013; He et al. 2017; Pike et al. 2018; Ghorbany et al. 2022; Latifi et al. 2022). van Zyl et al. (2013) investigated soil fluidization surrounding leaky water pipes and found that the head loss from a leaking pipe is composed of three components: (1) via the orifice, (2) in the fluidized zone, and (3) through static soil. They found that most of the head loss occurs within the fluidized zone. Significant (but lower) head loss occurs through the orifice, but only a small percentage of the loss occurs in the static soil. In another experimental study, Latifi et al. (2022) investigated the factors that influence the fluidized and mobile bed zone geometric parameters. They reported that water pressure and soil properties, mainly particle size, have the largest influence on the height, width, and cross-sectional area of the zones.

Ledwith et al. (1990) studied pipe pressures using two-dimensional (2D) fluidization experimental equipment. They studied the flow rate necessary for initial and complete fluidization. The experiments were conducted on sand at different depths. The results showed that although the bed of soil was only 42 cm high, it could withstand a pressure head of 33 m of water before becoming completely fluidized.

This prior work had significant value in understanding and controlling WDSs leakages. However, the effects of surrounding soil on the leakage mechanism remain unclear and require further study. The interaction of soil particles with the orifice is expected to alter the downstream jet behaviour and might obstruct a portion of the orifice itself.

According to seepage theory, the flow rate should exhibit a linear relationship with the hydraulic gradient, denoted as i, in accordance with Darcy's law (Harr 1962):
(2)
where q is the flow rate (m3/s), A is the cross-sectional area of flow (m2), k is the coefficient of permeability of the soil (m/s), and i is the hydraulic gradient (the hydraulic gradient is the change in hydraulic head Δ (m) divided by the length of the flow path l (m)). Darcy's law is widely used to describe the flow of water through porous media.

Other models utilized for predicting water flow through porous media include the Kozeny–Carman and Poiseuille models. The Kozeny–Carman equation is commonly employed to estimate permeability (k) but necessitates additional input parameters such as porosity, tortuosity, and specific surface area (Kozeny 1927; Carman 1937). On the other hand, the Poiseuille equation is typically used as a starting point for developing predictive equations (Yong et al. 2012). It is often combined with the assumption of the validity of Darcy's law, and subsequently, relationships are derived (Taylor et al. 1990). Darcy's law serves as the foundation for the majority of models used to predict water flow through porous media (Lambe & Whitman 1979; Olson & Daniel 1981) and has been adopted by numerous researchers, including Harr (1962) and Madanayaka & Sivakugan (2016), in the analytical solutions of confined seepage flow when employing the method of fragments (see later, section 3.2).

This study illustrates the results of a series of experiments to investigate the impact of bedding materials surrounding leakage pipes on leakage behaviour. The experiments were conducted in a modified seepage tank with leakage flow from a model of a defective water pipe into a bed of granular sand. Three different sands with different characteristics were considered: sand-fraction B (LBS-B), sand-fraction A (LBS-A), and glass ballotini (GB). The leakage rate, applied pressure in the pipe, and pore-water pressure head downstream of the defect were measured. Our study also presents an analytical model based on the method of fragments to predict the leakage rate in the presence of soil. The predicted results were then compared with those measured experimentally.

Experimental set-up

Experiments were conducted to investigate the impact of bedding materials on the hydraulic behaviour of leakage from failed water pipes. Figure 1 shows a diagram of the experimental set-up, which consisted of an engineered leak orifice placed at the bottom of a clear plexiglass seepage tank to enable observations of the bed behaviour. The dimensions of the tank were 700 × 600 × 153 mm. The rest of the set-up consisted of a water storage tank, a water pump to produce appropriate pressure, pipes to connect the pump to the seepage tank, a pressure control valve, a pressure gauge, a flow meter, and a pressure tapping connected to a sight tube to measure the pore pressure head downstream of the defect within the granular bed.
Figure 1

Schematic diagram of the experimental apparatus for lateral flow.

Figure 1

Schematic diagram of the experimental apparatus for lateral flow.

Close modal

Specially constructed boxes measuring 100 × 100 × 132 mm and having narrow (typically fractions of a mm) defect openings spanning the full width of the boxes simulated fractured water distribution pipes. The engineered leak openings were manufactured using laser cutting machines with high-dimension precision. They were constructed of two square-edged stainless-steel plates 10 mm thick and butted above the machined boxes and then welded to the required aperture. The defect sizes were adjusted using flat feeler gags measuring between 0.33 and 0.92 mm. The form of the defects remained unchanged with square-edged orifices 10 mm thick and 132 mm long.

Measurements of flow and pressure upstream of the defect

The flow rate through the defect was measured initially using the volume-time method by intercepting the outflow and collecting it in a graduated cylinder to a given volume and timing the procedure. This was repeated three times for each flow rate, and an average value was obtained. Later, a flow meter (model Signet 2551) with a display unit was used to record the leakage rate. The meter has a feature for averaging the flow rate (i.e., setting a time over which the meter averages the flow signals). This feature was set to 25 s during each test run to smooth the display on the liquid crystal display (LCD). The flow meter's specifications achieve ±2% accuracy. Pressure measurements upstream of the engineered leak opening was obtained using a pressure indicator (Model-DPI 261) with a head range up to 351 m (3,441 kPa) and an accuracy of 0.04%.

Measurements of pore pressure head

The pore-water pressure head in the bedding material was measured using a sight tube. A 3-mm diameter hole was drilled through the rear wall of the tank and connected to the sight tube. This hole was constructed along the centreline of the defect at a height 10 mm above the defect. A needle with a 2 mm diameter was inserted into this hole. This needle was long enough to provide a good connection point for the sight tube and the inside of the tank. Prior to preparing the test sample in the tank, the needle was covered with a screen to prevent grains from entering the pressure tap, thus preventing the needles from being obstructed. This might have affected the measured pressure head in the bed. Pore-water pressure head readings were taken directly from a vertically positioned water manometer with a water column precision of 1 mm.

Materials tested and specimen preparation

Tests were performed using three different granular materials: (1) sand-fraction B (LBS-B), (2) sand-fraction A (LBS-A), and (3) GB. An electron micrograph of these materials is shown in Figure 2: The GB had high sphericity, and the sands were subrounded and somewhat elongated and flattened. Figure 3 presents the size distribution of these materials and shows that the LBS-B ranged between 0.6 and 1.18 mm with a D50 size of 0.9 mm. GB was graded uniformly and had a D50 size of 0.9 mm, while LBS-A was coarser (D50 = 1.6 mm).
Figure 2

Scanning electron micrographs of the tested materials: (a) sand-fraction B (LBS-B), (b) GB, and (c) sand-fraction A (LBS-A).

Figure 2

Scanning electron micrographs of the tested materials: (a) sand-fraction B (LBS-B), (b) GB, and (c) sand-fraction A (LBS-A).

Close modal
Figure 3

Particle size distribution of the tested materials.

Figure 3

Particle size distribution of the tested materials.

Close modal

All tests were performed using saturated materials. Soil specimens were made by pouring a known amount of sand from a funnel with a 14 mm diameter nozzle into the tank. The height for pouring was maintained in a fixed position at about 15 mm above the tank's water level. Raining the soil into water minimized the air between the grains, which might have occluded voids and decreased permeability, thus affecting the measured head. Following deposition, specimens were densified by tapping the tank's base in a symmetrical manner with a rammer. Table 1 lists the properties of the test specimens. The permeability coefficient of the tested materials is between 0.24 and 0.87 cm/s.

Table 1

Properties of test specimens

MaterialDry density (mg/m3)Specific gravityVoid ratioPermeability (cm/s)
Glass ballotini 1.58 2.5 0.57 0.47 
Sand-fraction B (LBS-B) 1.73 2.65 0.53 0.24 
Sand-fraction A (LBS-A) 1.70 2.66 0.56 0.87 
MaterialDry density (mg/m3)Specific gravityVoid ratioPermeability (cm/s)
Glass ballotini 1.58 2.5 0.57 0.47 
Sand-fraction B (LBS-B) 1.73 2.65 0.53 0.24 
Sand-fraction A (LBS-A) 1.70 2.66 0.56 0.87 

This research did not consider the impact of clay around the pipes. Clay is normally avoided as a bedding material because moisture changes can cause a significant volume increase or decrease. However, it is expected that materials with very low permeability, i.e., clay, will be resistant to fluidization, instead undergo hydraulic fracture.

Test procedures

Tests were performed at controlled pressures upstream of the defect. Some tests used controlled flow rates while monitoring the behaviour of the particulate bed. Water was allowed to flow vertically through the defect into the bed of particles. Initially, a small pressure was applied (such as 2 kPa) after which the leakage rate then increased incrementally. For each increment in pressure (thus indicating leakage rate), the pore pressure head in the particulate bed was recorded after being allowed to stabilize for some time (3 min). Pore-water pressure heads in the bed were obtained using the sight tube, whereas pressure upstream of the defect was read from the pressure indicator. The flow rate (i.e., leakage rate) was read from the flow meter. The same procedure was repeated with each increment in pressure and leakage rate. At least three tests were conducted under similar conditions to validate the test results for repeatability and reproducibility.

Effects of bedding materials

The presence of bedding material surrounding a leaking pipe caused a significant change in the leakage rate versus free flow conditions. This material had a greater impact on larger defect widths.

Figure 4(a) shows the pressure–leakage relationship under increasing pressure for flow through a 0.62-mm defect width into a 300-mm bed height of different materials (LBS-B, GB, and LBS-A). The figure also shows the pressure–leakage relationship in the case of free flow conditions (without media), and the curve of the pressure–leakage relationship was fitted according to the orifice flow equation (Equation (1)), thus suggesting that leakages vary in proportion to the square root of the pipe's pressure head. Examining the pressure–leakage relationship in the case of free flow conditions (without soil) shows notable behaviour (Figure 4(a)). The data indicate that the leakage rate initially varied with the pressure following the orifice flow equation. However, a discrepancy from the orifice flow equation was seen, and this discrepancy grew larger as the pressure increased beyond 20 kPa. This observation is interesting but is beyond the scope of this work. The discrepancies are likely due to cavitation (Alsaydalani 2023).
Figure 4

Effect of soil on the leakage rate for: (a) different bedding materials (sand fractions LBS-B and LBS-A and glass GB), 300 mm bed height; defect width 0.62 mm; (b) two different defect widths (0.33 and 0.92 mm), and 300 mm bed height of LBS-B.

Figure 4

Effect of soil on the leakage rate for: (a) different bedding materials (sand fractions LBS-B and LBS-A and glass GB), 300 mm bed height; defect width 0.62 mm; (b) two different defect widths (0.33 and 0.92 mm), and 300 mm bed height of LBS-B.

Close modal

Figure 4(a) shows that, in the case of discharge into the soil acting as a bedding material, the bedding materials significantly changed the leakage rate versus free flow conditions (without soil). A significant drop in the leakage rate occurred when discharges flowed into a bed of sand. This drop became larger for finer sand particles. Particle size and therefore permeability can be expected to have a large impact on leakage rate. For example, an applied pressure in the pipe of 15 kPa produced a leakage rate of about 1,200 L/h through a defect width of 0.62 mm under free flow conditions. When discharged into a bed of coarse particles (1.6 mm) LBS-A, this same applied pressure produced 540 L/h. The same conditions produced a leakage rate of about 300 L/h in a similar bed height containing finer particles of LBS-B (0.9 mm).

The effect of soil on leakage rate is more pronounced for larger defect widths. Figure 4(b) shows the pressure–leakage relationship for two different defect widths (0.33 and 0.92 mm) discharging into the same bed of materials (a 300-mm bed height of LBS-B). In comparison to the free flow condition (Figure 4(b)), we see that the soil impact on the leakage rate is greater for the larger defect size of 0.92 mm.

The change in discharge coefficient is simply a reflection of the energy lost by the fluid as it flows through the orifice. This coefficient can be affected by a number of factors such as pipe material, orifice shape and size, and the head upstream of the orifice. Brater et al. (1996) reported that the values for the discharge coefficients of short tubes – namely orifices with a large ratio of length (pipe thickness) to orifice size, which was the case in this study, were found to vary from approximately 0.72 to 0.83.

Figure 5 shows the coefficient of discharge as a function of Reynolds number for flow through a 0.62-mm defect width in the case of free flow (without soil) conditions and discharge into 300 mm beds of granular soils, fine and coarse sands (LBS-B and A). The discharge coefficient was calculated using the orifice equation (Equation (1)). The Reynolds number was represented by Re = 4VR/v in which V is the velocity, v is the fluid's kinematic viscosity, and R is the hydraulic radius of the orifice. (R can be calculated as the area A over wetted perimeter P). Figure 5 shows that the values of in the case of free flow condition were approximately 0.73, which is consistent with the range indicated by Brater et al. (1996). However, a significant drop in the values of was observed in the case of discharge into beds of granular materials. The value of was reduced by about 38% for coarse particles and by 70% for the case of finer particles compared to free flow conditions.
Figure 5

Coefficient of discharge as a function of Reynolds number for different discharge conditions (fine sand, coarse sand, and free flow); 300-mm bed heights; 0.62-mm defect opening.

Figure 5

Coefficient of discharge as a function of Reynolds number for different discharge conditions (fine sand, coarse sand, and free flow); 300-mm bed heights; 0.62-mm defect opening.

Close modal

The presence of bedding material surrounding a leaking pipe produced significant changes in the coefficient of discharge and added dependence on the defect and particle sizes; thus, the permeability of the bedding material.

Leakage rate estimates using the method of fragments

The leakage rate in the presence of soil can be computed using the method of fragments, which is an analytical method to solve for confined seepage flow problems. It was originally proposed by Pavlovsky in 1935 (Pavlovsky 1956) and advanced by Harr (1962). Here, the flow region is divided into a number of fragments with the assumption that the equipotential at different parts of the flow region can be approximated by straight vertical lines. A dimensionless form factor is thus defined for each fragment that depends on fragment geometry. The leakage rate q can be calculated using form factors:
(3)

Here, q is the flow (leakage) rate (m3/s), h is the head loss over the flow domain (m), k is the soil permeability (m/s), and Φ is dimensionless form factor; Φ is defined as the number of equipotential drops in ith fragment to number of flow channels . The head loss through the fragment is assumed to change linearly. Harr (1962) presented six types of fragments for confined flow systems. Fragment types I and IV are considered in the current study because they are relevant to the leakage model presented here. Harr (1962) provides details for fragments Types II, III, V, and VI.

The form factor was derived based on the one-dimensional flow for fragment type I (Figure 6), i.e., parallel flow between impervious boundaries.
Figure 6

Type I fragment (adopted from Harr 1962).

Figure 6

Type I fragment (adopted from Harr 1962).

Close modal
From Darcy's law, the flow rate q in the soil for a given head will be as follows (Harr 1962):
(4)
Hence, from Equation (4), the form factor is
(5)
For an elemental Type I section (Figure 6(b)),
(6)

This elemental section can be used to derive the form factor for fragment type IV, which represents the leakage model considered here.

Figure 7 shows the leakage model which is a fragment with a boundary length S at the defect, bed height b, and defect width a. This work adopted the Pavlovsky approach to the type IV fragment, which is based on the results of electrical analogue tests. The flow region could be divided into two parts: active and passive. The dividing line OD is at an angle θ (Figure 7). Pavlovsky used analogue studies and assumed that θ = 45°, which resulted in two conditions, depending on the ratio of b to S: (1) bS; and (2) bS. The case where bS represents the model of this study. Here, the active zone is comprised of elements of type I fragments of height dy as illustrated in Figure 7. Hence, the form factor is the integral of dy over x from 0 at the bottom of the bed (i.e., at the defect) to b at the bed surface:
(7)
Figure 7

Leakage model using the method of fragments solution.

Figure 7

Leakage model using the method of fragments solution.

Close modal
Before Equation (7) can be integrated, x must be expressed in terms of y:
(8)
Based on Pavlovsky's assumption that angle θ = 45, we see that:
(9)
and, from Equation (9),
(10)
and, substituting in Equation (7),
(11)
Integrating Equation (11) results in a form factor of:
(12)
and, substituting in Equation (3), we get the formula for predicting the leakage rate in which leakage from defect and seepage through media:
(13)

Here, q is the leakage rate (m3/s), h is the head loss over the flow domain (m), K is the soil permeability (m/s), b is bed height (m), and a is the defect width (m).

Substituting the values of the experimental model (bed height b = 0.3 m and defect width a = 0.33 mm (0.00033 m)), in Equation (12), we find that the approximate solution gives a form factor Φ = 6.813. The leakage rate can be predicted using Equation (13) for a given soil permeability k, head loss over the flow domain, h, bed height b, and defect width a.

Figure 8 compares the leakage rate predicted using the method of fragments with those measured in the current experiments. There was good agreement as demonstrated in the line of equality in Figure 8. Most of the data fall within ±5% of the error line in this figure. The method of fragments provides sensible estimates of the leakage rate and is relatively fast in providing the solutions.
Figure 8

Comparison of leakage rate predictions using the method of fragments with those measured from experiments.

Figure 8

Comparison of leakage rate predictions using the method of fragments with those measured from experiments.

Close modal

Fluidization of bedding materials

Bedding materials fluidization occurs when particles in the bed become free to move with the pore fluid (i.e., the particles become separated and in motion with the pore fluid) (van Zyl et al. 2013). The onset of this phenomenon can be predicted by examining the pressure–leakage relationship. Therefore, tests were performed at controlled pressures and in some tests at controlled flow rates while monitoring the behaviour of the particulate bed for fluidization. Other controlling parameters affecting fluidization and leakage rate were also considered in the study, such as particle size, particle shape, bed depth, and defect size (see Sections 3.4 and 3.5).

Figure 9(a) shows the pressure–leakage relationship under higher applied pressure (thus flow rate). This step examined the effect of soil fluidization on leakage behaviour. In this case, the discharge occurs through a 0.62 mm defect width into a 300 mm height of LBS-B. The data of pressure and leakage rates for the free flow condition are plotted in addition to the curve of the pressure–leakage relationship obtained using the orifice flow equation. The pressure–leakage relationship (Figure 9(a)) shows that the initial phase (A) occurs in cases in which an approximate linear relationship is seen between pressure and leakage rates. Here, the soil had a substantial impact on the pressure–leakage relationship and reduced the leakage rate by approximately 70% versus free flow conditions. Further increases in the applied pressure (and thus leakage rate), another phase (B) was observed. This is the fluidized stage. In this experiment, fluidization of the bedding materials was observed at a leakage rate of about 350 L/h. Beyond this leakage rate at which fluidization was initiated, a significant increase in the leakage rate (from 350 to 1,050 L/h) occurred. This increase was accompanied by a dramatic drop in the applied pressure upstream of the defect until it reached a value similar to that observed under the free flow case (without soil). Here, the leakage rate varied with pressure following the orifice flow equation. However, a discrepancy from the orifice flow equation was seen at a certain point (at a leakage rate greater than 1,250 L/h). This discrepancy grew larger as the pressure and leakage rate increased. The discrepancy from the orifice flow equation occurred because of cavitation development in the orifice (as discussed earlier). The measured leakage rate was lower than that calculated using the orifice equation during cavitation conditions.
Figure 9

Pressure–leakage relationship for a defect width of 0.62 mm discharged into a 300-mm bed of (a) LBS-B; (b) GB; and (c) LBS-A.

Figure 9

Pressure–leakage relationship for a defect width of 0.62 mm discharged into a 300-mm bed of (a) LBS-B; (b) GB; and (c) LBS-A.

Close modal

Figure 9(b) presents the data for a 300-mm bed of GB and a 0.62-mm defect width. The initial phase up to the leakage rate of approximately 600 L/h shows a linear relationship between the applied pressure and leakage rate. Fluidization was observed above this flow rate, and there was a significant increase in leakage rate associated with a slight drop in the applied pressure. However, in this instance, the flow remained below those of the orifice flow. Beyond a certain point of flow, namely 1,400 L/h, the leakage did not continue to increase as the pressure increased because of cavitation in the orifice.

Figure 9(c) shows similar data but for a 300-mm bed of coarse material (LBS-A) and a 0.62-mm defect size. The material did not fluidize even though there was a high leakage rate (1,400 L/h) during the test. The data also show a linear correlation between the applied pressure and leakage rate up to a rate of about 1,300 L/h (until cavitation) as is clear from the free flow conditions. Similar to the data in Figure 9(b), the flow remained below those for the orifice flow. In this test, the effect of soil was more pronounced on leakage than the orifice alone at all stages.

Effects of particle size and shape

Particle size is another important factor affecting leakage rates and fluidization of the bedding material. For example, a leakage rate of 632 L/h yielded a pore-water pressure head downstream of the defect of 650 mm in 0.9 mm LBS-B: This pressure head was sufficient to fluidize the bedding material as shown in Figure 10. The coarser sand (1.6 mm) LBS-A, under the same flow rate, yielded a pore-water pressure head of only 143 mm.
Figure 10

Pore-water pressure head versus leakage rate for 300 mm bed of LBS-B (D50 = 0.9 mm, subrounded and slightly elongated), LBS-A (coarse particles, D50 = 1.6 mm), and GB (D50 = 0.9 mm, high sphericity) with a defect width of 0.62 mm.

Figure 10

Pore-water pressure head versus leakage rate for 300 mm bed of LBS-B (D50 = 0.9 mm, subrounded and slightly elongated), LBS-A (coarse particles, D50 = 1.6 mm), and GB (D50 = 0.9 mm, high sphericity) with a defect width of 0.62 mm.

Close modal

Particle shape also has a substantial impact on leakage rate, and the pore-water pressure head downstream of the defect that initiates fluidization. In our experiments, the pore-water pressure head for the LBS-B (0.9 mm), which is sand-subrounded and slightly elongated and flattened – compared with those of GB with the same particle size; it had high sphericity. Fluidization of LBS-B was initiated at a leakage rate of about 632 L/h, whereas a leakage rate of about 1,500 L/h was required to fluidize a similar bed of GB. Higher spherical material fluidized at higher pressure and flow rates.

Effects of bed depth and defect size

Figure 11 shows the measured pore-water pressure above the defect as a function of the leakage rate for various bed heights: (1) 300 mm, (2) 220 mm, and (3) 150 mm of LBS-B over a 0.33-mm defect opening. The figure illustrates that the pore-water pressure head in the bed increased as the leakage rate increased. The value increased approximately linearly at a lower leakage rate (up to about 200 L/h), thus suggesting Darcy flow. At higher rates, however, a nonlinear regime could be observed possibly due to the effect of both laminar and turbulent flow through the bedding materials (see Niven (2002)). Once the pore-water pressure head peaked, it dropped rapidly for each bed height after fluidization. The peak pore-water pressure head at which fluidization occurred for the 300 mm bed height was higher than that of the 220 mm. This difference could be attributed to the higher resistance of water to flow into the granular bed as a result of the increase in the total stress.
Figure 11

Pore-water pressure head versus leakage rate for various bed depths: (1) 300 mm, (2) 220 mm, and (3) 150 mm of LBS-B over a 0.33 mm defect opening.

Figure 11

Pore-water pressure head versus leakage rate for various bed depths: (1) 300 mm, (2) 220 mm, and (3) 150 mm of LBS-B over a 0.33 mm defect opening.

Close modal
Figure 12 shows the pore-water pressure head at the defect as a function of leakage rate for different defect widths of 0.33, 0.62, and 0.92 mm. Similar to the observation in Figure 11, we see that the pore-water pressure head increases approximately linearly with leakage rates at lower leakage rates. The pressure then follows a nonlinear regime at higher leakage rates. Once the leakage rate reached a certain value (about 630 L/h), the pore-water pressure head peaked and then dropped rapidly while the leakage rate continued to increase because of the fluidization of the bedding materials. Fluidization of granular materials reached the bed surface in all three cases at approximately the same leakage rate (about 1,000 L/h), thus indicating that the leakage rate controlled the fluidization process.
Figure 12

Pore-water pressure head versus leakage rate for various defect openings: (1) 0.33 mm, (2) 0.62 mm, and (3) 0.92 mm.

Figure 12

Pore-water pressure head versus leakage rate for various defect openings: (1) 0.33 mm, (2) 0.62 mm, and (3) 0.92 mm.

Close modal

The measured pressure upstream of the defect at which fluidization occurred varied with the defect size (Figure 12). A smaller defect width indicated a larger pressure upstream of the defect to fluidize the bed of granular materials. For example, an applied pressure of about 31 kPa was required to fluidize a 300 mm bed of LBS-B for the 0.33-mm orifice opening. The large defect width (0.92 mm) only required 16 kPa to fluidize the same bed of granular materials. This difference might be because the small defect widths required high upstream pressure to generate a sufficient leakage rate to fluidize the granular bed.

This study investigated the influence of soil bedding on the hydraulic behaviour of leakage from failed water pipes. Using a special experimental model, a series of experiments were performed on three different soils: (1) LBS-B, (2) LBS-A, and (3) GB with different characteristics. The impact of various parameters on leakage behaviour was considered: particle size, particle shape, bed height, defect width, and fluidization of the soil bedding. The experiments were performed at controlled pressures upstream of the defect. Some tests used controlled flow rates while monitoring the behaviour of the soil bed.

Based on this study, several conclusions can be drawn:

  • The presence of bedding material surrounding a leaking pipe causes a significant change in the leakage rate versus free flow conditions. This material has a greater impact on larger defect sizes.

  • A significant drop in the values of was observed when discharged into a soil bed versus free flow condition with a reduction in the value of by about 38% for the coarse particles and by 70% in the case of finer particles.

  • High leakage rates can flow from defective pipes without fluidization of the soil bed. This implies that leaks can occur in WDSs without breaking the soil surface. This makes it more difficult to detect leaks in these systems.

  • The characteristics of soil bedding including particle size, particle shape, bed height, and defect width have a significant impact on the leakage rate and fluidization of the bedding materials. Coarser soil particles, high spherical materials, and a higher bed height fluidized at higher leakage rates and pressure.

  • In the case of fluidization of the bedding materials, the pressure–leakage relationship obeys the orifice flow equation. However, a discrepancy from the orifice flow equation can occur at high applied pressure and leakage rates as a result of cavitation in the orifice.

An analytical model based on the method of fragments predicts the leakage rate in the presence of the surrounding soil. Here, the flow region is divided into a number of fragments with a defined dimensionless form factor. The leakage rate can be predicted for a given soil permeability k, head loss over the flow domain h, bed height b, and defect width a. Comparisons of the results show a good fit between predicted and measured values. The method of fragments provides sensible estimates of the leakage rate and is relatively fast.

The following points are suggested to reduce leakage rates from underground water pipes:

  • Applying pressure management techniques (e.g., using pressure-reducing valves (PRV)) to control the water pressure inside the pipeline is recommended.

  • Considering a backfill soil specification with finer particles instead of coarser particles.

  • Increasing the depth of embedment of water pipes to increase the soil resistance to fluidization and thus reduce the leakage rate. However, shallow depths may be preferred to allow quick flow of water to the surface so that leaks can be found and repaired quickly.

The author would like to thank Umm Al-Qura University, Saudi Arabia, for the support provided during the present work.

All relevant data are included in the paper or its Supplementary Information.

The authors declare there is no conflict.

Adedeji
K. B.
,
Hamam
Y.
,
Abe
B. T.
&
Abu-Mahfouz
A. M.
2018
Pressure management strategies for water loss reduction in large-scale water piping networks: a review
. In:
Gourbesville, P., Cunge, J. & Caignaert, G. (eds)
Advances in Hydroinformatics
.
Springer Water. Springer
,
Singapore
, pp.
465
480
.
Al-Khomairi
A. M.
2005
Use of the steady-state orifice equation in the computation of transient flow through pipe leaks
.
Arab. J. Sci. Eng.
30
(
1
),
33
46
.
Alsaydalani
M. O. A.
2023
Effect of orifice hydraulic and geometric characteristics on leakage in water distribution systems
.
GEOMATE J.
25
(
107
),
59
67
.
Brater
E. F.
,
King
H. W.
,
Lindell
J. E.
&
Wei
C. Y.
1996
Handbook of Hydraulics
, 7th edn.
McGraw-Hill
,
New York
, pp.
1
640
.
Burnell
D.
&
Race
J.
2000
Water distributions systems analysis: patterns in supply-pipe leakage
. In
Building Partnerships
,
30 July–2 August
,
Minneapolis, MN
. pp.
1
11
.
Carman
P. C.
1937
Fluid flow through a granular bed
.
Trans. Inst. Chem. Eng. London
15
,
150
156
.
Ćipranić
I.
&
Sekulić
G.
2015
The analysis of the influence of soil on leakage in water supply systems
.
Teh. Vjesn.
22
(
5
),
1179
1184
.
De Paola
F.
,
Galdiero
E.
,
Giugni
M.
,
Papa
R.
&
Urciuoli
G.
2014
Experimental investigation on a buried leaking pipe
.
Procedia Eng.
89
,
298
303
.
Farley
M.
&
Trow
S.
2003
Losses in Water Distribution Networks: A Practitioner's Guide to Assessment, Monitoring and Control
.
IWA
,
London
,
UK
.
Fox
S.
,
Collins
R.
&
Boxall
J.
2016
Physical investigation into the significance of ground conditions on dynamic leakage behaviour
.
J. Water Supply: Res. Technol. – AQUA
65
(
2
),
103
115
.
doi:10.2166/aqua.2015.079
.
Ghorbany
S.
,
Hamedi
V.
&
Ghodsian
M.
2022
Experimental investigations of soil fluidization by an upward water leak jet
.
Urban Water J.
20
(
1
),
39
48
.
doi:10.1080/1573062X.2022.2134805
.
Global Water Market
.
2017
Meeting the World's Water and Wastewater Needs Until 2020
.
Global Water Intelligence
,
Oxford
,
UK
.
Greyvenstein
B.
&
Van Zyl
J. E.
2007
An experimental investigation into the pressure-leakage relationship of some failed water pipes
.
J. Water Supply: Res. Technol. – AQUA
56
(
2
),
117
124
.
Harr
M. E.
1962
Groundwater and Seepage
.
McGraw-Hill
,
New York, NY
.
He
Y.
,
Zhu
D. Z.
,
Zhang
T.
,
Shao
Y.
&
Yu
T.
2017
Experimental observations on the initiation of sand-bed erosion by an upward water jet
.
J. Hydraul. Eng.
143
(
7
),
06017007
.
doi:10.1061/(ASCE)HY.1943-7900.0001302
.
Kozeny
J.
1927
Stizurg reports on the capillary conduction of water in the soil. [Uber Kapillare Leitung des Wassersim Boden Stizurgsberichte]
.
R. Acad. Sci. Vienna, Proc. Class I
136
,
271
306
.
Lambe
T. W.
&
Whitman
R. V.
1979
Solid Mechanics, SI-Version, Series in Soil Engineering
.
John Wiley & Sons
,
New York, NY
.
Latifi
M.
,
Naeeni
S. T.
&
Mahdavi
A.
2018
Experimental assessment of soil effects on the leakage discharge from polyethylene pipes
.
Water Sci. Technol. Water Supply
18
(
2
),
539
554
.
doi:10.2166/ws.2017.134
.
Latifi
M.
,
Mohammadbeigi
S.
,
Farahi Moghadam
K.
,
Naeeni
S. T. O.
&
Kilanehei
F.
2022
Experimental study of pressure and soil effects on fluidization and mobile bed zones around buried leaking pipes
.
J. Pipeline Syst. Eng. Pract.
13
(
4
),
04022034
.
doi:10.1061/(ASCE)PS.1949-1204.0000671.
Ledwith
C.
,
Weisman
R. N.
&
Lennon
G. P.
1990
Selection of hole size for fluidization pipes
. In
Proc. Nat. Hydr. Conf., ASCE
,
New York, NY
, pp.
933
938
.
Liemberger
R.
&
Wyatt
A.
2019
Quantifying the global non-revenue water problem
.
Water Supply
19
(
3
),
831
837
.
doi:10.2166/ws.2018.129
.
Madanayaka
T. A.
&
Sivakugan
N.
2016
Approximate equations for the method of fragment
.
Int. J. Geotech. Eng.
10
(
3
),
297
303
.
doi:10.1080/19386362.2016.1144338
.
Niven
R. K.
2002
Physical insights into the Ergun and Wen &Yu equations for fluid flow in packed and fluidized beds
.
Chem. Eng. Sci.
57
(
3
),
527
534
.
doi:10.1016/S0009-2509(01)00371-2
.
Noack
C.
&
Ulanicki
B.
2008
Modelling of soil diffusibility on leakage characteristics of buried pipes
. In:
Water Distribution Systems Analysis Symposium 2006
. pp.
1
9
.
doi:10.1061/40941(247)175
.
Olson
R. E.
&
Daniel
D. E.
1981
Measurement of the hydraulic conductivity of fine-grained soils
.
Permeability Groundwater Contam. Transp. ASTM STP
746
,
18
64
.
doi:10.1520/STP28316S
.
Pavlovsky
N.
1956
Collected Works
.
Doklady Akademii Nauk USSR
,
Leningrad
,
Russia
.
Pike
S. M.
,
van Zyl
J. E.
&
Clayton
C. R. I.
2018
Scouring damage to buried pipes caused by leakage jets: experimental study
.
J. Pipeline Syst. Eng. Pract.
9
(
4
),
04018020
.
doi:10.1061/(ASCE)PS.1949-1204.0000328
.
Taylor
S. W.
,
Milly
P. C. D.
&
Jaffé
P. R.
1990
Biofilm growth and the related changes in the physical properties of a porous medium: 2. Permeability
.
Water Resour. Res.
26
(
9
),
2161
2169
.
doi:10.1029/WR026i009p02161
.
van Zyl
J. E.
&
Clayton
C. R. I.
2007
The effect of pressure on leakage in water distribution systems
.
Proc. Inst. Civ. Eng. Water Manage.
160
(
2
),
109
114
.
doi:10.1680/wama.2007.160.2.109
.
van Zyl
J. E.
,
Alsaydalani
M. O. A.
,
Clayton
C. R. I.
,
Bird
T.
&
Dennis
A.
2013
Soil fluidization outside leaks in water distribution pipes – preliminary observations
.
Proc. Inst. Civ. Eng Water Manage.
166
(
10
),
546
555
.
doi:10.1680/wama.11.00119
.
Walski
T.
,
Bezts
W.
,
Posluzny
E.
,
Weir
M.
&
Whitman
B.
2006
Modelling leakage reduction through pressure control
.
J. Am. Water Works Assoc.
98
(
4
),
147
152
.
doi:10.1002/j.1551-8833.2006.tb07642.x
.
Yong
R. N.
,
Nakano
M.
&
Pusch
R.
2012
Environmental Soil Properties and Behaviour
.
CRC Press
,
New York, NY
.
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