Air bubbles and water droplets entrainment and removal in turbulent water flows/Oro burbuliuku ir vandens laseliu itraukimas ir ismetimas turbulenciniuose vandens srautuose.
Vaideliene, A. ; Vaidelys, V.
1. Introduction
Anthropogenic activities are making considerable influence on the
character of natural processes taking place in atmosphere as well as in
open water reservoirs. With the continuous extension of manufacturing
activities, the anthropogenic factor has an increasing impact on global
environment, including both air and water pollution. The challenge we
face is to evaluate and determine the maximal anthropogenic impact that
the environment, i.e. water and atmosphere, can still be subjected to
the level it can resist trough self-purification. Such an objective can
not be achieved without investigation of the pure physical processes,
which take place in interfaces between open water and atmosphere [1-4]
as well as between separate deep water layers. Both interfaces are of
significant importance for the water quality [5-7] of open water bodies.
Usually those interfaces are considered separately one from another.
Some references [8-11] specify that physical processes at the open
water-air interfaces are stronger determinants of water quality than
those taking place in deep water. Therefore the consideration of the
present paper is focused on the open water-air interface. The above
mentioned physical phenomena are fully determined by diffusion based
processes such as an aeration and reaeration or evaporation and
adsorption processes [12-15]. Moreover, those processes can be regarded
as separate cases of diffusion itself, where the character of processes
rate is determined by ambient properties and their boundary conditions.
Investigation and evaluation of those properties and boundary conditions
in various specific cases obviously is a pure physical problem [16-18].
The right solution can be achieved only under the investigation of this
problem related to diffusion process and its mathematical description.
Determined significant dependences between the processes parameters
allow to simulate the process mathematically and give practically useful
tool for environmental engineering.
On the background of above mentioned considerations can be
concluded that the investigation of diffusion processes on the air-water
interface should be based on the classical theory of diffusion [19-22].
On the other hand, despite of common general diffusion process features,
air-water interface has its own specific behaviour [23-25]. The factor
determining this behaviour first of all is specific boundary conditions
on the air-water interface. These specific boundary conditions are:
roughness of water surface, due to it higher friction between air and
water, kinetics of the streams rising from deep layers to the surface,
etc. One of the most important factors making influence on diffusion
processes is mass transfer over the weirs and through the hydro power
plants turbines [26-28]. This falling water from weirs or flow through
hydro power plants turbines is so called "white water"
phenomenon. This water consists of air bubbles and water droplets mixed
together in the water surface.
The goal of this paper is the mathematical simulation of physical
mechanism of air bubbles entrainment and removal of water drops
processes evaluating water turbulence generated by wears and hydro power
stations.
2. Structural development of air and water dynamic mixing under
conditions of falling water
2.1. Hydropower plants and weirs influence on bubbles entrainment
After weirs the water has falling stream or jet shape. As it's
known, under these conditions the local aeration is taking place and the
air bubbles are entrained into the water due to jet impact to the water
lower stream (Fig. 1).
[FIGURE 1 OMITTED]
Often in the literature such an air bubbles and a water droplets
mixing is known as a "self-aerated process". If to be more
exact should be noticed that there are two processes: one when the water
falls through the wear free and the next--when flow impacts in to the
water or when the water forces through hydropower stations turbines. In
the latter case the jet forms under the water and air bubbles are
entrained in to the water as well as small water droplets compose. The
air bubbles and water droplets mixing together form a compound layers.
Researchers started to investigate this phenomenon only in the middle of
the 20 century. The first were Straub and Anderson [29] and Wood [30].
Straub and Anderson described a self-aeration process in the open
channel water flows. Wood and Chan son were first who measured
concentration and the rising rate of air bubbles. Later Chanson, Toobes,
Gonzalez continued the investigation. These authors investigated only
air bubbles entrainment into the water as a diffusion phenomenon, though
did not investigate and did not describe mathematically dynamical mixing
of air bubbles and water droplets. McKeogh first proved that jet's
conditions at the moment of air entrainment can be described as a
function of jet's turbulence [31]. Turbulent air bubbles diffusion
appears under falling down jet conditions. This process is also known as
advective diffusion [32-35]. This term denotes the movement of air
bubbles from domains with higher spatial gas concentration to domains
with lower concentration. The mixing of bubbles stimulates this process.
2.2. Entrainment--removal process in the air-water interface
The exchange of gases in the interface between the air and the
water may be regarded as limited molecular diffusion. The simplest model
of air-water kinetic exchange on liquid side at the boundary between the
two air and water phases is shown in Fig. 2.
[FIGURE 2 OMITTED]
With the water streaming over weirs, dams or through hydro
turbines, the peculiar entrainment removal processes are taking place in
the air-water interface (Fig. 3), generating air and water bubbles
within the zone of falling jet. Thus, the layers with mixed air and
water bubbles are formed. These layers are shown in Fig. 4 .
Under particular conditions the similar mixtures of bubbles can be
formed in lakes, large dams and oceans. In these cases breaking waves
(wave breaking initiated at certain wind speeds) influence turbulent
diffusion of air (oxygen and C[O.sub.2]) and form water microlayers in
the interface [36-39]. The following sections deal only with processes
influenced by the turbulence of water falling from the weirs or forcing
through hydropower plants.
[FIGURE 3 OMITTED]
[FIGURE 4 OMITTED]
3. Equations describing air bubbles and water droplets entrainment
and removal in the open channel
The supercritical flows induce a visual impression of "white
water". Such flows appear in the channels where the turbulence is
sufficient for air bubbles entraining into the flow.
As it is shown in Fig. 4 two fluxes come in to the water interface:
water droplets flux and air bubbles flux. We suggest the following
expressions of kinetic equations as a suitable for use in this case
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII] (1)
where [MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII] is
concentration of water droplets, [c.sub.air] is concentration of air
bubbles, t is time. [[chi].sub.12] and [[chi].sub.21] are entrainment
rates of water droplets and air bubbles respectively, which are
expressed as [MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII], where
[[alpha].sub.12] and [[alpha].sub.21] are sticking coefficients of water
droplets and air bubbles to the surface respectively, which range from 0
to 1 and [MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII] and
[i.sub.air] are the relative water droplets and air bubbles fluxes to
the surface respectively.
Solution of differential Eq. (1), gives the following dependences
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII] (2)
During entrainment process the upper layer gets in contact with air
and concentration of air bubbles and water droplets changes. Proposed
Eq. (1) describes character of this change. However, the process of
water droplets removal from the surface is not involved in Eq. (1).
Evaluating removal process the Eq. (1) takes the following form
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII] (3)
where [MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII] and
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII] are relative
concentrations in first and second monolayer; [w.sub.12] and [w.sub.21]
are removal rates of water droplets and air bubbles respectively;
[v.sub.r] is the total removal rate.
Two first components of Eq. (3) describe removal rate of air
bubbles or water droplets from the surface monolayer and next two
components describe entrainment rate of air bubbles or water droplets.
Constituents with sign minus give the removal rate of air bubbles and
water droplets from the surface monolayer and the constituents with sign
plus give the entrainment rate of air bubbles and water droplets into
the surface monolayer as a result of the entrainment of relocated
bubbles also as a result of the arrival of air bubbles and water
droplets from the next monolayer.
The monolayer approach of dynamic mixing process was used. Eq. (3)
expresses this process. The variations of surface concentration in the
second layer must be known for solving this equation. The mixing of
water and air bubbles between the layers takes place because of
continuous entrainment and removal. In case when due to entrainment and
removal air and water particles move from K layer to K - 1 or K + 1,
this concentration rate can be expressed as follows
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII] (4)
where [v.sub.e] is the total entrainment rate.
It can be proved that Eq. (4) has the form of diffusion equation with moving boundary. After simple mathematical rearrangements Eq. (4)
can be converted into the following form
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII] (5)
where [D.sup.*] is effective diffusion coefficient, [v.sub.x] is
surface movement velocity.
Bubbles exchange between air and water usually takes place in the
upper layers. In the case which we investigated the element composition
of air bubbles and water droplets was changeable also in lower layers.
4. Results and discussions
As Fig. 5 illustrates, air bubbles are entrained in to the water at
the zone of falling water. The size and number of bubbles pooled in to
water depends on weir high and on velocity of jet at the moment when the
jets hit at the surface of the water. Jet hit to the water splashes
small water droplets, which mix with the air bubbles together and makes
mixed air-water layers. We simulated air bubbles and water droplets
entrainment and removal processes with Eq. (4). Also we calculated
Reynolds and Froude numbers according the following formulas
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII] (6)
where [[rho].sub.w] is density of the water (kg/[m.sup.3]), v is
jet impact velocity, [d.sub.1] is jet thickness at impact (m),
[[mu].sub.w] is dynamic viscosity of the water (N s/[m.sup.2]), g is
gravity constant (m/[s.sup.2]).
For the simulation we used experimental data published by
H.Chanson, T. Brattberg [40], F.Murzyn, H.Chanson [41] and L.Toombes,
H.Chanson [42], H.Chanson C.A.Gonzalez [43]. These authors obtained
experimental data in artificial channel made for special purpose of
their experiment. They determined concentration of air and water bubbles
by means of conductivity measuring in different zones of the channel
with changing height of weir, flow velocity and horizontal distance from
weir to bubbles zone (Fig. 5). Determination of bubbles concentration
was based on the feature, that conductivity in air burbles zone and in
water bubbles zone differs thousands times.
[FIGURE 5 OMITTED]
Entrainment and removal processes take place at the moment of
interaction. We described this process with Eq. (1) and solution of this
equation with Eq. (2). Fig. 6 illustrates the solution equations
calculated for different initial concentrations. The range of initial
water droplets relative concentration we assumed from 0.01 to 0.3 and
air bubbles initial concentration from 0.7 to 0.99 (Fig. 6).
As are can see from Fig. 6, with water and air sticking to the
surface probabilistic coefficients [[alpha].sub.12] = 0.8 and
[[alpha].sub.21] = 0.2 respectively air bubbles and water droplets
concentration dependence on time changes according exponential law.
Asymptotes values of all curves are equal to probabilistic sticking
coefficients. The shape of curves depends on initial concentration of
air bubbles and water droplets.
[FIGURE 6 OMITTED]
As was mentioned above, the process of air bubbles and water
droplets entrainment and removal takes place not only in surface layers,
but also in deeper layers. We described this process with Eq. (4). Fig.
7 illustrates air and water bubbles concentration dependences on weir
height, evaluating deeper layers.
[FIGURE 7 OMITTED]
The extreme points in the curves of Fig. 7 can be explained as
follows: with the water flow trough the weir or trough hydro turbine the
submerged jet forms (Fig. 8); this jet spreads in the surrounding liquid
and at that same time loses its velocity.
Due to jet and surrounding liquid particles velocity transverse
pulsation air bubbles are entrained into the jet. Jet velocity
distribution is depicted in cross-sections a-a and b-b. Central initial
velocity [v.sub.1] is constant. Initial sector of the jet is between
cross-sections a-a and b-b. Maximum air bubbles concentration is in the
centre of the jet while the minimum concentration is at the jet and
surrounding liquid interface. Beyond this interface the recirculation zone forms. As can be seen from Fig. 7 at the y = 0.026 air bubbles
concentration is maximum, therefore can be concluded that this point
coincides the jet centre. Point y = 0.0325 coincides boundary between
jet and surrounding water, because at this point air bubbles
concentration is minimum. Further air bubbles concentration increases
until reaches 1. With y > 0.0325 recirculation zone begins. Naturally
that water drops concentration run has opposite character.
[FIGURE 8 OMITTED]
With the weir height growth the absorption of air bubbles into
water grows till reaching maximal air bubbles concentration. Depending
on distance [x.sub.1] and [d.sub.1] (Fig. 5) and on weir height breaking
points of the curves change their position (Figs. 7 - 11).
[FIGURE 9 OMITTED]
As can be seen from Figs. 7 and 9 the curves in these figures are
different. The reason was that these curves were calculated not for two
air and water layers like in Fig. 6, but for many layers. Fig. 9 shows
entrainment curve for [x.sub.1] = 1.0 m and [d.sub.1] = 0.0245 m
(experimental data were taken from [44]). Initial air bubbles
concentration equals zero. With the weir height growing air bubbles
concentration remains uniform and at y = 0.02 m starts to change. The
points y = 0.032 and y = 0.04 are the points of breaking of the curves.
Therefore depending on initial conditions and the number of taken
layers entrainment and removal curves can be expressed from exponential
dependence curves with breaking points and points of maximums and
minimums (Figs. 7 - 11). Peak maximum on the air bubbles curve
correspond water bubbles minimum on the water bubbles curve and vice
versa. The curves simulated by us coincide with experimental data [44].
As it can be seen from Fig. 10 each air bubbles and water drops curve
have maximum and minimum. All these maximums and minimums well coincide
with experimentally obtained maximums and minimums [42].
[FIGURE 10 OMITTED]
[FIGURE 11 OMITTED]
As it can be seen from Fig. 11 air and water curves have two
extreme points.
Air bubbles and water drops rising rate, size and frequency depend
on jet velocity at the moment of jet hit at the water surface. A bubble
rising frequency depends on the distance from weir to jet hit point.
With the jet hit at the water surface air bubbles are pooled into the
water. Some delay in creating air bubbles process appears and it
increases with the distance. This delay explains the character of
frequency dependence on distance.
5. Conclusions
1. Water turbulence highly influences processes of air bubbles and
water droplets diffusion. These processes can be described by
mathematical equations.
2. The bubbles and droplets created in the falling water flow
stimulate the processes of air and water entrainment and removal.
3. Initial conditions of air bubbles and water droplets entrainment
and removal processes determine run of proposed simulation equations
solutions curves.
4. Good coincidence of theoretical and experimental results was
achieved with more than two air-water layers on the air-water interface.
http://dx.doi.org/ 10.5755/j01.mech.18.1.1282
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A. Vaidelien, Kaunas University of Technology, Studentu 50, 51368
Kaunas, Lithuania and Lithuanian Energy Institute, Breslaujos 3, 44403
Kaunas, Lithuania, E-mail: avaidel@mail.lei.lt
V. Vaidelys, Kaunas University of Technology, Studentu 50, 51368
Kaunas, Lithuania, E-mail: vytautas.vaidelys@ktu.lt
Received March 17, 2011
Accepted February 09, 2012