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International Journal of Civil Engineering and Technology (IJCIET)
Volume 10, Issue 06, June 2019, pp. 324-335, Article ID: IJCIET_10_06_032
Available online at http://www.iaeme.com/ijciet/issues.asp?JType=IJCIET&VType=10&IType=6
ISSN Print: 0976-6308 and ISSN Online: 0976-6316
© IAEME Publication
INFLUENCE OF INFLOW-OUTFLOW SYSTEMS
FOR NATURAL MIXING IN A CIRCULAR TANK
Zahiraniza Mustaffa*, Syed Muzzamil Hussain Shah, Wan Norgayah Wan Mohd Noor
and Ebrahim Hamid Hussein Al-Qadami
Department of Civil and Environmental Engineering, Universiti Teknologi PETRONAS,
32610, Seri Iskandar, Perak, Malaysia
Marlinda Abdul Malek
Institute of Sustainable Energy (ISE), Universiti Tenaga Nasional, 43000, Selangor, Malaysia
*Correspondence Author
ABSTRACT
A tank that is normally equipped with an inlet and outlet system would exhibit
different response in the mechanics of inflows and outflows. This then allows natural
mixing to take place. An effective natural mixing would then be defined when the
natural flow processes taken place in the tank would somehow clean the storage water
to the most optimum level. This paper presents the influence of inflow and outflow
orientation in creating an effective natural mixing inside of a tank. The study involves
the response of different inlet-outlet configuration systems in imitating natural
cleaning. The cleaning herein is defined through mixing process taken place in the
tank. A circular tank which may be translated as a retention pond in real life was
filled with clay (kaolin), replicating a turbid storage. The cleanliness through mixing
was measured by means of Total Suspended Solid (TSS) test. With this regards, nine
different inflow-outflow orientations were tested. It was noticed that the lowest level of
inflow (I3) and highest level of outflow (O1) gave the best results in producing effective
natural mixing. On the other hand, poor mixing was noticed when the configuration of
the inlet and outlet were kept in series.
Key words: circular tank; inflow-outflow configuration; mixing; TSS; kaolin
Cite this Article: Zahiraniza Mustaffa, Syed Muzzamil Hussain Shah, Marlinda
Abdul Malek, Wan Norgayah Wan Mohd Noor and Ebrahim Hamid Hussein Al-
Qadami, Influence of Inflow-Outflow Systems for Natural Mixing in a Circular Tank,
International Journal of Civil Engineering and Technology 10(6), 2019, pp. 324-335.
http://www.iaeme.com/IJCIET/issues.asp?JType=IJCIET&VType=10&IType=6
1. INTRODUCTION
A stormwater retention pond is used to store excess stormwater runoff for a certain period of
time before releasing it to the environment. This is to prevent flood from occurring especially
at the urban areas due to poor drainage system. The importance of a retention pond is that it
reduces flood peak discharge by temporary storing the excess water which is then gradually
Influence of Inflow-Outflow Systems for Natural Mixing in a Circular Tank
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released. The stormwater runoff is temporarily stored in a retention pond before distributing
to the nearby rivers. In other words, the retention pond dampens the flow of the stormwater
runoff before going to the river.
The retention pond is also designed with an inlet and outlet system that can produce
natural mixing inside the pond. Natural mixing describes the transport of sediments within a
water body through longitudinal, transverse, and vertical movements. Thus, it allows natural
behavior of the water in breaking the trapped or unwanted particles within the water body.
When a storage tank is highly contaminated for not being able to flow (static condition), thus
pollutions may occur in the tank. There should be some kind of natural processes to take place
within this water body, without much technical efforts being put in place to clean these
storage tanks. As such, natural mixing seems to be favorable and economical from the
environmental point of views.
By far, there has not been any written procedure that explains which inflow and outflow
orientation is best in producing effective natural mixing. The mixing that occurs inside the
pond is one of the critical components of a distribution system and can pose significant
challenges [1]. There are studies regarding enhanced mixing in a retention pond for example
by using a RainJet which is a man-made device [2], however, studies on the inflow and
outflow mechanism and how it affects the mixing characteristics into a retention pond which
is a natural event are sparse. By creating a natural mixing occurrence in the retention pond
with the purpose of cleaning or reducing the sediments in the pond, the results gained would
be beneficial to the authorities involved because it would be environmentally friendly and
relatively cheap which would be practical for implementation. Although there is an Urban
Stormwater Management Manual for Malaysia (MSMA 2nd
Edition) which is provided by the
Department of Irrigation and Drainage (DID), Government of Malaysia, but MSMA does not
properly describe the effect of mixing characteristics of inflows (stormwater) into a retention
pond.
Herein an experiment was conducted in the Hydraulics Laboratory of Universiti
Teknologi PETRONAS, Malaysia involving mixing of flows in a circular tank, which may in
certain context acts as a retention pond having geometrically similar shape to that of the tank.
However, the experimental study was tested under a range of inflows from 0.0001305 to
0.0001341 m3/s in identifying the best inlet-outlet configuration, with the intention to produce
the most effective natural mixing through the measurement of TSS removal.
Hypothetically, by logic people assume that a particular configuration of the inlet and out
orientation can ensure effective natural mixing, however, such hypothesis has never been
experimentally justified. Therefore, the technical results attained herein through experimental
investigations would support whether such assumptions made by the people are true or untrue.
2. LITERATURE REVIEW
A retention pond is a basin that is designed to provide stormwater reduction and catch runoff
water from higher elevation areas [3]. Figure 1 shows the mechanism of the stormwater runoff
entering the retention pond before going to a river through a pipe, whereas Figure 2 shows a
simple case of inlet stormwater without unit for remediation.
Zahiraniza Mustaffa, Syed Muzzamil Hussain Shah, Marlinda Abdul Malek,
Wan Norgayah Wan Mohd Noor and Ebrahim Hamid Hussein Al-Qadami
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Figure 1. Mechanism of stormwater runoff.
Figure 2. Simplest case of inlet stormwater without unit for remediation [4].
A retention pond is also similar to a wet-detention pond because it retains water at a
certain level inside the pond. The design of a retention pond or a wet-detention pond is
provided in the MSMA, Malaysia. Based on this, the design criteria of a detention pond that is
not classified as dams must be designed with the following aspects which have been lined by
pond water depth, embankment top widths, side slopes, bottom grades and freeboard [5]. An
example of typical detention ponds in Malaysia from MSMA are highlighted in Figure 3.
Figure 3. Typical detention ponds [5].
Other than catching runoff from higher elevation areas and to retain stormwater, the
retention pond also has other advantages and disadvantages of its own. Table 1 summarizes
some of the advantages and disadvantages of a retention pond.
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Table 1. Advantages and disadvantages of a retention pond.
Advantages Disadvantages
Can cater for all storms.
Good removal capability of urban
pollutants.
Can be used where groundwater is
vulnerable, if lined.
Good community acceptability.
High potential ecological, aesthetic
and amenity benefits.
May add value to local properties.
No reduction in runoff volume.
Anaerobic conditions can occur without
regular inflow.
Land take may limit use in high density
sites.
May not be suitable for steep sites, due to
requirement for high embankments.
Colonization by invasive species could
increase maintenance.
Perceived health and safety risks may
result in fencing and isolation of the pond.
The way how mixing mechanism occur plays a vital role for natural cleaning of a
retention pond. Mixing occurs when the initial energy of an inflow into a reservoir pushes the
more stationary lake water ahead of it. The inflow continues to push the lake water ahead until
the initial momentum is substantially dissipated by river bottom shear forces and by the
pressure gradient across the interface between the water masses. The turbulent kinetic energy
of the inflow is usually sufficient to keep the water completely mixed vertically to prevent the
settling of some materials [6]. Figure 4 shows a plunge point and separation point move
upstream and downstream defining the transition zone.
Figure 4. Pooling and mixing at the plunge point [6].
There are numerous parameters that could affect the mixing process. Since it is the study
of fluids in motion, therefore focus has been given at the ways different forces affect the
movement of liquids [7]. For instance, the flow velocity which is a vector quantity refers to the
rate at which an object changes its position or in easier term it is the speed with direction [8].
Turbidity is the cloudiness or haziness of a fluid caused by suspended solids that are generally
invisible to the naked eye. Fluids can contain suspended solid matter consisting of particles of
many different sizes. While some suspended material will be large enough and heavy enough
to settle rapidly to the bottom of the container if a liquid sample is left to, very small particles
will settle only very slowly or not at all if the sample is regularly agitated or the particles are
colloidal. These small solid particles cause the liquid to appear turbid [9]. Sedimentation is the
natural process in which materials such as stone and sand is carried to the bottom of a body of
water and forms a solid layer. This is due to their motion through the fluid in response to the
forces acting on them. These forces can be due to gravity, centrifugal acceleration or
electromagnetism. When rain or snow falls onto the earth, it moves according to the laws of
gravity. A ration of the precipitation seeps into the ground to replenish groundwater.
Zahiraniza Mustaffa, Syed Muzzamil Hussain Shah, Marlinda Abdul Malek,
Wan Norgayah Wan Mohd Noor and Ebrahim Hamid Hussein Al-Qadami
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However, most of it flows downhill as runoff. Runoff is extremely important because it keeps
rivers and lakes full of water, but it also changes the landscape by the action of erosion.
Runoff occurs during storms, and much more water flows into the rivers during storms. The
Total suspended solids (TSS) are from the influence of suspended particles in a water body
causing its turbidity and transparency [10]. The TSS are present in water that can be trapped
by a filter. It includes varieties of materials which makes it a problem when it is highly
concentrated.
The mixing mechanism varies based on the pond types and shapes as well as their
conditions. Herein the mixing characteristic in a lake, rectangular and circular tank have been
lightly discussed as shown in Table 2.
Table 2. Mixing Mechanism.
Mixing Characteristics Remarks / Outcome
Figure 5. Schematic of the Mixing
Processes in a Lake [11].
Wind is responsible for waves and
currents which is the dominant
energy for mixing.
Boundaries are vital due to the
shear that develops between the
ambient flow and non-slip
condition.
Inflow and outflow create kinetic
energy.
Figure 6. Mixing in a Rectangular Tank
[2].
The RainJet ensures that the side
walls and the center area of the
tank floor are kept free from
deposits due to the mixing force
provided by the installed
equipment.
Figure 7. Mixing in a Circular Tank [2].
RainJet will start building the
inertia of the circular movement
which will clean the stormwater
tank.
3. MATERIALS AND METHODS
The typical concrete design for a retention pond is usually rectangular and circular. However,
to achieve the significant degree of control over pond shape and dimensions is hard because
of the needs of taking the natural topographic of the site into considerations. In order to
choose the suitable shape of the tank to replicate pond condition for the experiment, Table 3
shows the advantages and disadvantages of a rectangular and a circular tank.
Influence of Inflow-Outflow Systems for Natural Mixing in a Circular Tank
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Table 3. Advantages and disadvantages of a retention tank.
Type of Tanks Advantages Disadvantages
Figure 8. Rectangular Tank.
Better use of land. Problems with removal
of waste, difficult to
clean and poor mixing
especially at the corner
of the tank.
Figure 9. Circular Tank.
Good mixing of the water, high
ratio of tank volume and can be
used to rapidly concentrates and
remove settleable solids.
Poor use of land area.
The experiment was carried out using a circular tank made of plastic with the volume of
300 L. The water was always kept at 250 L at the beginning of the experiment, then one litre
of kaolin was added and mixed inside the tank. The inlet-outlet configurations were designed
based on the selections shown in Table 4. Once the inlet-outlet configuration was chosen in
the circular tank, inflow was released into the tank and the time was measured for a period of
90 min. The first sample was taken at the outlet of the tank, then the second sample was taken
at the collection point X inside of the tank. The side and plan views of the circular tank are
shown in Figure 10 and 11, respectively. Samples were taken at every 15 minutes interval.
The samples were then brought for TSS testing.
Table 4. Different combinations of inlet-outlet configurations.
No. Inlet-outlet Configuration
1. I1,O1
2. I1,O2
3. I1,O3
4. I2,O1
5. I2,O2
6. I2,O3
7. I3,O1
8. I3,O2
9. I3,O3
Zahiraniza Mustaffa, Syed Muzzamil Hussain Shah, Marlinda Abdul Malek,
Wan Norgayah Wan Mohd Noor and Ebrahim Hamid Hussein Al-Qadami
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Figure 10. Side view (a) Schematic diagram of circular tank and (b) Experimental set-up (not to
scale).
Figure 11. Plan view (a) Schematic diagram (b) Experimental set-up (not to scale).
4. RESULTS
Sample were collected from the inside (collection point X) and outside (outlet) of the tank.
The samples were taken at the lowest point inside of the tank, however it does no reach the
bottom of the tank. This was due to decrease of water level based on its respective outlet and
to maintain the position where the samples were taken. Samples were also taken from outside
of the tank as it indicates the amount of solids that were able to reduce. The graph for the
amount of TSS attained both from the collection point X and the outlet for few configurations
have been discussed as shown in Figure 12, 13 and 14, respectively.
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Figure 12. Graph of TSS vs time for I1O1.
Figure 13. Graph of TSS vs time for I2O1.
Figure 14. Graph of TSS vs time for I3O1.
Among the samples collected from the collection point X and the outlet, it was noticed
that the amount of TSS collected from the collection point X for all the cases was high. Table
5 shows the percentage difference for all the configurations so that the most effective inlet-
outlet orientation can be classified.
0.00
0.10
0.20
0.30
0.40
0.50
0.60
0.70
0.80
0.90
0 20 40 60 80 100
TS
S, m
g/
L
Time, min
CollectionPoint X
Outlet
0.00
0.10
0.20
0.30
0.40
0.50
0.60
0.70
0.80
0.90
0 20 40 60 80 100
TS
S, m
g/
L
Time, min
CollectionPoint X
Outlet
0.00
0.10
0.20
0.30
0.40
0.50
0.60
0.70
0.80
0.90
0 20 40 60 80 100
TS
S, m
g/
L
Time, min
CollectionPoint X
Outlet
Zahiraniza Mustaffa, Syed Muzzamil Hussain Shah, Marlinda Abdul Malek,
Wan Norgayah Wan Mohd Noor and Ebrahim Hamid Hussein Al-Qadami
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Table 5. Percentage difference for collection point x and outlet.
Outlet Inlet
I1 I2 I3
O1 276% 201% 365
O2 72% 369% 0.43%
O3 49% 28% 3.10%
From the above table, a noticeable difference can be seen between the samples collected
from the collection point X and the outlet. However, it can be said that for configuration I3O2,
a difference of only 0.43% was noticed, whereas the maximum difference of 369% was found
for the configuration I2O2.
The time interval used for the experiment was 15 minutes for the duration of 90 minutes.
There was a significant decrease shown at the first 45 to 60 minutes duration for most of the
experiments where the readings start to become constant. The mixing characteristics obtained
for several combinations are further discussed in the following section. The mixing for I1O1,
I1O2 and I1O3 has been shown in Figure 15, whereas the mixing effective region during these
configurations has been highlighted in Table 6. The mixing for I2O1, I2O2 and I2O3 has been
shown in Figure 16, whereas the mixing effective region during these configurations has been
highlighted in Table 7. Similarly, the mixing for I3O1, I3O2 and I3O3 has been shown in Figure
17, whereas the mixing effective region during these configurations has been highlighted in
Table 8.
Figure 15. Graph of TSS vs time for I1O1, I1O2 and I1O3.
Table 6. Mixing effective region for I1O1, I1O2 and I1O3.
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Figure 16. Graph of TSS vs time for I2O1, I2O2 and I2O3.
Table 7. Mixing effective region for I2O1, I2O2 and I2O3.
Figure 17. Graph of TSS vs time for I3O1, I3O2 and I3O3.
Zahiraniza Mustaffa, Syed Muzzamil Hussain Shah, Marlinda Abdul Malek,
Wan Norgayah Wan Mohd Noor and Ebrahim Hamid Hussein Al-Qadami
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Table 8. Mixing effective region for I3O1, I3O2 and I3O3.
Table 6, 7 and 8 shows the observation (schematic view) and the actual view (plan view)
of mixing inside the tank. Through observation, it was found out that the mixing occurred
similarly to what the arrow is shown in the schematic view. The graph for I1 shows that O1
showed poor mixing because of its low TSS value compared to O2 and O3. On the other hand,
O2 showed best effective mixing throughout the period of 90 minutes. Similarly, the graph for
I2 shows that O2 showed poor mixing because of its low TSS value compared to O1 and O3.
However, O1 showed best effective mixing throughout the period of 90 minutes. Lastly, the
graph of I3 shows that O3 showed poor mixing because of its low TSS value compared to O1
and O2. However, O1 showed the best effective mixing throughout the period of 90 minutes.
5. CONCLUSIONS
The research that has been carried out highlights that effective natural mixing does happen in
the circular tank under different configurations. Different choice of inflows and outflows
come out with different TSS results. Thus, it can be observed that which particular
configuration is the best by having the highest TSS values. The most effective mixing
occurred when the configuration was set to I3-O1, while the least effective mixing occurred
when the configuration of the inlet and outlet were kept in series, for instance, I1-O1, I2-O2 and
I3-O3.
ACKNOWLEDGMENTS
This research was supported by Universiti Teknologi PETRONAS (UTP) Internal Grant
(URIF 0153AAG24), the Technology Innovation Program (Grant No.: 10053121) funded by
the Ministry of Trade, Industry & Energy (MI, Korea) and the iRMC Bold2025, Universiti
Tenaga Nasional, Malaysia (Grant Code: RJO 1043 6494).
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Influence of Inflow-Outflow Systems for Natural Mixing in a Circular Tank
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