The Relationship between Temperature and Performance of Solar
Desalination Plants
Ahror Jafarov
1a
and Zaynalobudin Kobuliev
2b
1
Technological University of Tajikistan, 63/3, Nemat Karabaev street, Dushanbe, Tajikistan
2
Institute of Water Problems, Hydropower and Ecology of the National Academy of Sciences of Tajikistan, 12, Parvin
street, Dushanbe, Tajikistan
Keywords: Temperature Regime, Thermal Resistance, Thermal Conductivity, Thermal Effect, Solar Radiation,
Condensation, Heat Exchange, Heat Flux, Recuperation.
Abstract: This article considers the analysis of studies on increasing the productivity of solar desalination plants through
the rational use of falling solar energy on the surface of installations, as well as the dependence of the
efficiency of solar desalination plants on the parameters of external thermal effects and determining the
temperature regime of these installations. To determine the temperature regime of the desalter, a calculation
method was applied based on finding the temperature functions in the form of Fourier series. It has been
established that the heat transferred by radiation from the surface of the water to the surface of the transparent
coating can be reduced by installing additional transparent screens between the evaporating zone of the
desalter and its roof. This technical solution made it possible to increase the productivity of sloped-stepped
type installations by 1.5 times in comparison with single-layer glazing.
1 INTRODUCTION
According to the annual addresses of the Founder of
Peace and National Unity Leader of the Nation,
President of the Republic of Tajikistan Emomali
Rahmon to the Majlisi Oli of the Republic of
Tajikistan, hydropower comprises for 98% of
electricity production in Tajikistan. This has become
the basis for Tajikistan to be on the 135th place in
terms of greenhouse gas emissions into the
atmosphere on a global scale, which is assessed as a
valuable contribution of the Republic of Tajikistan to
the solution of global problems of mankind.
The value of this indicator shows that on a
regional scale, the specific quantitative characteristics
of greenhouse gas emissions in Tajikistan is the
smallest indicator for each person, which is
considered Tajikistan's contribution to improvement
and enhancement of the ecological situation in the
region and, particularly, the planet. This helps to
achieve widespread use of renewable energy sources
(RES), first of all, hydropower. It was also noted that
the vast use of renewable energy sources, especially
a
https://orcid.org/0000-0003-1105-068X
b
https://orcid.org/0000-0003-0272-0792
water resources, may explore one of the main sources
of "green energy" generation and the development of
a "green economy".
In connection with the statements made above and
according to the main actions, in order to achieve the
set strategic goals of the National Development
Strategy of the Republic of Tajikistan for the period
up to 2030 and its initial stage. The initial stage is
included in the Medium-Term Development Program
of the Republic of Tajikistan for 2016-2020, which
indicated that to ensure energy security, as well as
efficient use of electricity, it is necessary to diversify
generating energy sources with the development of
hydropower resources, both large and small rivers,
the development of existing capacities in the oil and
gas and coal sector, the exploration and development
of new fossil fuel deposits, the creation and provision
of technical capabilities with the purpose of using
non-traditional (renewable) energy sources (solar,
wind, biological, geothermal), modernization and
rehabilitation of existing ones, as well as the
construction of new hydroelectric power plants
(HPPs) and thermal power plants (TPPs).
Jafarov, A. and Kobuliev, Z.
The Relationship between Temperature and Performance of Solar Desalination Plants.
DOI: 10.5220/0011367600003350
In Proceedings of the 5th International Scientific Congress Society of Ambient Intelligence (ISC SAI 2022) - Sustainable Development and Global Climate Change, pages 525-533
ISBN: 978-989-758-600-2
Copyright
c
2022 by SCITEPRESS Science and Technology Publications, Lda. All rights reserved
525
The above-mentioned statement will serve as the
reason to consider the research topic relevant and
timely. The aim of the research is the rational use of
solar energy through the development of theoretical
and applied models and the improvement of low-
potential solar installations in the climatic conditions
of the Republic of Tajikistan.
To achieve the goal, the following tasks were set
and solved:
- Assessment of the state and development of the
use of non-traditional energy sources in Central Asia,
including in Tajikistan.
- Analysis of existing methods for determining the
formation of the process of heat exchange of
constructions, under the influence of solar thermal
effects and their improvement;
- Technical and economic justification and
practical implementation of low-grade solar
installations and developed models for the use of
renewable energy sources in the conditions of the
Republic of Tajikistan.
The scientific novelty of the obtained results
consists of determining the temperature regime of
closed volumes and channels with a coolant under
periodic fluctuations in the parameters of the thermal
effect and a developed model for regulating the
temperature regime of a homogeneous structure
under periodic fluctuations in the temperature of the
medium on its lateral surface, on the basis of which
the calculated parameters of the thermal
characteristics of the coolant in duct exposed to the
thermal effect of the environment with periodically
changing temperature.
The practical significance lies in the fact that the
thermal state of structures in a closed volume is
determined in the absence and presence of sources
and sinks of heat and filtration of outdoor air, as well
as an algorithm for calculating and controlling the
parameters of the temperature state of structures of
solar desalination plants has been developed.
The researches were conducted and completed
using the current regulatory methods for studying the
physicochemical and biotechnological properties of
low-grade solar installations (Sokolov and Hershgal,
1990; Le Pierrèset et al., 2003; Ma et al., 2018; Zhu
et al., 2019). In the processing stage, a mathematical
and statistical technique was used to process
experimental data. For the theoretical part, there were
used analytical and numerical methods to solve the
problem of heat and mass transfer, regarding the
research objects (Safarov et al., 2003).
The authors contribution in this study is to
conduct joint research, starting with the formulation
of the research objectives, methodological support for
their solutions and the analysis of the results of
monitoring the water interrogation process obtained
by the authors. The research mainly relies on the
results of researches conducted by the authors over
the last years on the problems of rational use of water
resources.
The 21st century will be characterized by a further
exacerbation of the shortage of fresh water on a global
scale. At the same time, it is noted that two-thirds of
drinking water is consumed for the implementation of
agro-technical activities (for example, for irrigation
and growing crops). The problem of desalination of
sea and ocean water is aggravated by the fact that the
world's population is growing rapidly (more than 80
million people per year) and by 2025 at least 2 billion
people on the planet will systematically face an acute
shortage of fresh water (Ruy et al., 2007).
It is also necessary to note that fresh water is used
in different ways by the population of different
countries. So, the water consumption in the homes of
US residents is on average about 380 liters per person
per day, while millions of people on the planet
(especially in underdeveloped countries) use about 19
liters of water per day, and 46% of the world's
inhabitants do not access to the supplied running
water. All this indicates that there is a problem with
fresh water, the demand for water will only start to
grow. Therefore, people need to take care not only of
water supplies, but also learn to rationally use
precious moisture with care (Ruy et al., 2007).
In recent years, the problem of the shortage of
fresh water has become more and more urgent for
many regions of the world. As a result of
desertification of large areas, pollution of water
bodies and an increase in water consumption, there is
already a shortage of drinking water for 1.2 billion
people. It becomes obvious that in the future
humanity will face a global catastrophe of lack of
drinking water. In such conditions, it is important to
develop not only methods for the efficient use of
water resources, but also projects for the purification
and desalination of sea water.
2 EXTERNAL THERMAL
INFLUENCE PARAMETERS
The external thermal impact on constructions located
in the open area is manifested in the form of
convective heat fluxes during heat exchange with the
outside air, radiant heat fluxes during heat exchange
with the atmosphere, the surface of the Earth and the
surrounding objects, as well as solar irradiation.
ISC SAI 2022 - V International Scientific Congress SOCIETY OF AMBIENT INTELLIGENCE
526
It is known that the outside air temperature
changes over time in all regions of the Earth, and the
temperature changes have a periodic oscillatory
nature. Like any oscillatory process, temperature
changes are characterized by periods and amplitude
of fluctuations. The period of temperature
fluctuations outside the air is the time interval during
which there is one complete oscillation. In
hydrometeorology it is accepted to distinguish
annual, monthly and daily fluctuations of outdoor air
temperature with a period of change of one year, one
month and one day, respectively. The amplitude of
temperature fluctuations is the largest deviation from
the average value for the period of fluctuations. The
amplitude of outside air temperature fluctuations, as
well as its average values for the period of
fluctuations, depends on the geographical location of
the area on the earth's surface.
Numerous observations of changes in outdoor air
temperature (Gidrometeoizdat, 1966) show that the
daily amplitude of temperature fluctuations in
summertime for almost all localities is significantly
greater than the amplitude of temperature fluctuations
in wintertime. Maximum air temperatures are
observed in July and minimum air temperatures in
January. Temperature fluctuations of recurring
pattern in summer and winter can be repeated for 5-
10 days, i.e. repeatedly. It is important because the
temperature fluctuations of environment repeatedly
repeat the temperature state of bodies in it gets the
established periodical character (Lykov, 1967) that
allows to consider a heat transfer in elements of
constructions exposed to external thermal influence
as quasi-stationary process with the established
periodical character of temperature and heat flows
changes.
Constructions located in open areas, in addition to
heat exchange with the outside air, are exposed to
solar radiation. The total impact of solar radiation on
the surfaces of constructions consists of direct
irradiation (direct solar radiation) and irradiation by
the atmosphere scattering the sun's rays (scattered
radiation).
Thermal influence of solar rays on surfaces of
constructions is characterized by solar radiation
intensity which is the quantity of heat referred to unit
of time and unit of the irradiated surface area, and
changes in the same units as heat flux density
(W/m2).
The path the sun's rays take in the atmosphere
increases as the Sun approaches the horizon line. The
intensity of solar radiation reaching the Earth's
surface decreases sharply. When the height of the Sun
above the horizon h is less than 5°, the thermal impact
of solar radiation can be ignored.
For values h more than the intensity of direct
solar radiation on the surface, perpendicular to the
direction of the rays, is approximated by the
simplified formula of Kastrov-Savinov (Kiteyev,
1962).
𝐼
пр
= 1360
𝑠𝑖𝑛
𝑠𝑖𝑛ℎ +
1−𝑝
𝑝
Вт/м
𝟐
(1)
where h is the height of the Sun, deg;
p - atmospheric transparency coefficient, varying
from 0.7 to 0.8.
The height of the Sun h is calculated by the
formula
h = arc sin (sin φ sinδ + cos φ cos δ cos γ) (2)
where φ - geographic latitude, deg;
δ - declination of the Sun (deg.) depending on the
time of the year (from -23.4° in December to 23.4° in
June);
γ - hour angle in degrees, determined by the ratio
γ = 15(τ1-12), (3)
where τ1 - local time, h.
Due to the refraction of light in the atmosphere,
the apparent height of the Sun slightly differs from
the actual height, especially at sunrise and sunset.
However, this phenomenon is neglected when
calculating the thermal effects of solar radiation.
Intensity of direct solar radiation on flat horizontal
and vertical surfaces of constructions is defined by
dependences
𝐼
пр.г
=𝐼
пр
sin;
(4)
𝐼
прв
=𝐼
пр
cossin
|
𝛼−𝑥
|
(5)
where x is the angle determining the position of
the vertical surface relative to the meridian;
α is the azimuth of the Sun, calculated by the ratio
cos α = sinφ cos т - cos φ sin т cos А
0
(6)
The intensity of total solar radiation is defined as
the sum of direct and scattered radiation. The
dependence of the intensity of scattered solar
radiation affecting the horizontal surface under a
cloudless sky as a function of angle h is as follows:
The Relationship between Temperature and Performance of Solar Desalination Plants
527
h
0
10 20 30 40 50 60 70
1
рr
31,4 43,1 52,4 60,5 65,2 67,5 68,6
The intensity of scattered solar radiation for
vertical surfaces is determined by the approximate
dependence
𝐼
пр
=0,5 𝐼
рг
(7)
The scattering that the sun's rays pass through the
atmosphere varies depending on the position of the
Sun in relation to the horizon line, which is the reason
for the periodic change in the intensity of solar
radiation reaching the Earth and affecting the surfaces
of various constructions.
More complete data on measurements of solar
radiation intensity for different times of the year and
any regions of the USSR are given in the reference
book on the climate of the USSR (Gidrometeoizdat,
1966), which summarizes the results of observations
of changes in the outside air temperature in the
territory of the Tajik SSR.
3 METHODOLOGIES
The main method of obtaining fresh water is based on
the heating and evaporation of salt water, its
subsequent condensation on the surface of the heat
exchanger and removal of the brine, which remains
after heating the mixture with a high salt content. Any
heat carrier that produces a sufficient amount of
energy can serve as a source of heat for the
desalination plant. There are installations based on
fossil fuels, chemical sources and fuel cells, with
electric heating and even on the basis of nuclear fuel.
Due to the fact that the greatest shortage of fresh
water is observed in regions of the world with
increased solar radiation, solar desalination plants are
of particular interest. Solar collector desalination -
plant for desalination of water by the method of
thermal distillation. The main advantages of solar
desalination plants are due to the energy source,
namely the absence of the need for fuel supplies,
environmental friendliness, and affordability.
There are two main technologies for desalination
of water, widely used in the world: a method based on
a change in the phase state of a substance (thermal
method), and membrane, which can be provided by
several methods.
Phase change technology includes:
- multistage distillation;
- highly efficient distillation;
- steam pressure: thermal and mechanical
compression of steam;
- other processes including distillation,
humidification, dehumidification using solar
installations.
Membrane technologies, in addition to membrane
distillation, include two main processes: reverse
osmosis and electrodialysis. These two technologies
use membranes to remove salts from water.
Both processes require a lot of energy to
overcome the existing osmotic pressure between
fresh and salt water. Electrodialysis technologies, as
a rule, are used only for brackish waters, in which
salts from the water stream are attracted by
membranes and pass through them under the action
of an electric current.
Despite significant advances in the use of solar
energy for desalination of salt water, the problem of
creating optimal methods for desalination of water
and the theory of their calculation is still unresolved.
(Achilov, 1976; Kolodin, 1981; SNiP, 1983; Baum,
1985)
To measure the impact of the climatic parameters
of the outside air and solar radiation, we can use the
reference data of the place of the experiment.
(Gidrometeo-Izdat, 1990; Dorvlo and Ampratwum,
1998; Stathopoulos and Zacharias, 2004; Hasni et al.,
2012; Smirnov, 2013; Adeala et al., 2015). The solar
desalination process generally proceeds as follows.
Before starting work, the solar water-maker,
which is a "hot box" in design, is filled with salt
water. Solar energy passes through the transparent
coating of the desalter almost completely (up to 90%)
and is absorbed by the surface of the salt water, which
heats up and evaporates.
Next, the saturated steam-air mixture comes into
contact with the colder transparent wall of the
desalter, and water vapor condenses on its surface. As
it accumulates, fresh water condensate is discharged
from the installation, and the desalter is replenished
with a new portion of salt water. The desalination
process is carried out continuously until the end of the
effect of solar radiation on the design of the
desalination plant.
The performance of solar plants is a function of
the salt water and condensation surface temperatures,
which in turn depend on the outside temperature and
the intensity of solar radiation. Since the parameters
of the external thermal effect, to which the desalter is
exposed, change during the daylight hours over a
fairly wide range, the temperature regime and
productivity of the installation are impermanent.
To measure the temperature regime of the
desalter, let us consider a calculation method based
ISC SAI 2022 - V International Scientific Congress SOCIETY OF AMBIENT INTELLIGENCE
528
on finding the temperature functions in the form of
Fourier series.
Assuming that the water temperature has
insignificant volume fluctuations, and the thermal
resistance of the transparent wall, through which the
heat flux from solar radiation enters the desalination
tank, it is possible to record the heat balance
equations for water and the transparent wall of the
desalination tank (Kutateladze, 1979; Brdlik, 1983;
Baum, 1985; Timakova, 2006; Nokali, 2007;
Temerov, 2008; Usmanov, 2019):
𝐶
в
𝜌
в
𝛿
в
𝑑𝑡
в
𝑑𝜏
=𝜀
в
𝛽
с
𝐼
с
−𝐾
тс
𝑡
в
−𝑡
ус
−𝐾
ти
𝑡
в
−𝑡
у
и
,
(1)
𝐶
в
𝜌
в
𝛿
в

с

=
𝐴
в
𝐼
с
−𝐾
п
(
𝑡
в
−𝑡
с
)
𝛼
н
(
𝑡
с
−−𝑡
н
)
,
(2)
here Cc, ρc, δc - specific heat, density and
thickness of the transparent wall of the desalter; Cв,
ρв, δв - specific heat, density and thickness of the
water layer; Ас, βс - absorption and throughput
capacity of the transparent wall of the desalter; Кп -
heat transfer coefficient from water to transparent
wall; Ктс, Kти - heat transfer coefficients of the
transparent wall and insulation of the desalter; α_н-
total heat transfer coefficient of the desalter; - the
intensity of solar radiation on the surface of the
transparent wall; tc, tв, respectively, the
temperatures of the transparent wall, water and
outside air; τ - time.
Since the daily changes in the temperature of the
outside air and the intensity of solar radiation are
periodic in nature, and the thermal capacity of the
installation is relatively small, it seems possible to
look for the dependences of the temperatures tc and
tв on time in the form of harmonic Fourier:
𝑡
с
=𝑡
с
+
𝑥
𝑐𝑜𝑠𝑘

+

+𝑦
𝑠𝑖𝑛𝑘

,
(3)
𝑡
в
=𝑡
в
+
𝜇
𝑐𝑜𝑠𝑘

+

+𝜂
𝑠𝑖𝑛𝑘

,
(4)
where the average values of temperatures tc0, tв0
and the coefficients of the series xk, yk, μ_k, η_k
should be determined during the solution; the value k
= 1, 2, 3 ... is an integer variable; z - period of change,
equal to 24 hours.
To find a solution to equations (1) and (2) in the
form (3) and (4), series (3) and (4) are conveniently
written using a complex number i:
𝑡
=𝑡

+𝜃

𝑒


,
(5)
𝑡
в
=𝑡
в
+𝜃
в
𝑒


,
(6)
where θ_ck, θ_vk are the amplitude-phase
characteristics of the simple harmonic components of
the temperatures of the transparent wall and water.
The amplitude-phase characteristics are related to the
coefficients of the series (5) and (6):
𝜃

=𝑥
−𝑖𝑦
,
(7)
𝜃
в
=𝜇
−𝑖𝜂
.
(8)
As already noted, the outside air temperature and
the intensity of solar irradiation can also be
represented in the form of Fourier series:
𝑡
н
=𝑡
н
+
𝛼
𝑐𝑜𝑠𝑘

+

+𝑏
𝑠𝑖𝑛𝑘

,
(9)
𝐼=𝐼
+
𝐶
𝑐𝑜𝑠𝑘

+

+𝑑
𝑠𝑖𝑛𝑘

;
(10)
where the average values of tн0, I0 and the
coefficients of the series ak, bk, ck, dk are determined
by harmonic analysis of daily fluctuations in the
outside air temperature and the intensity of solar
radiation. By analogy with relations (5) - (8), we have
𝑡
н
=𝑡
н
+𝜃
н
𝑒


,
(11)
𝐼=𝐼
+𝜃
𝑒


,
(12)
𝜃
н
=𝑎
−𝑖𝑏
,
(13)
𝜃
=𝑐
−𝑖𝑑
.
(14)
Let us determine the time derivatives of
temperatures tc and tв from equations (5) and (6):
The Relationship between Temperature and Performance of Solar Desalination Plants
529
𝑑𝑡
𝑑𝜏
=𝑘
2𝜋𝑖
𝑧

𝜃

𝑒

,
(15)
𝑑𝑡
в
𝑑𝜏
=𝑘
2𝜋𝑖
𝑧

𝜃
в
𝑒

,
(16)
Substituting relations (5), (6), (11), (12), (15), (16)
into equations (1) and (2), separating constant and
variable components in them, we obtain equations for
constant and variable components heat flows:
- for constant components
𝐴
с
𝑇
+𝐾
п
(
𝑡
в
−𝑡
с
)
−𝛼
н
(
𝑡
с
−𝑡
н
)
=0;
(17)
𝜀
в
𝐼
𝐼
𝐾
+𝐾
д
(
𝑡
в
−𝑡
н
)
=0;
(18)
- for k-x simple harmonic components of heat flux
densities
С
𝜌
𝛿
𝑘

𝜃

𝑒

=
𝐴
𝜃
𝑒

+𝐾
п
(
𝜃
в
−𝜃

)
* 𝑒

+𝛼
н
(
𝜃
н
−𝜃

)
𝑒

;
(19)
С
в
𝜌
в
𝛿
в
𝑘

𝑖𝜃

𝑒

=
𝜀
в
𝑇
𝜃
𝑒

+
+(𝐾
+𝐾
д
)
(
𝜃
н
−𝜃
в
)
𝑒

;
(20)
From equations (17) and (18) we determine the
constant components of the desired temperatures
𝑡
в
=𝑡
н
+
𝜀
в
𝑇
в
(𝐾
+𝐾
д
)
𝐼
;
(21)
𝑡

=
𝐴
с
𝐼
+𝐾
п
𝑡
в
+𝛼
н
𝑡
н
𝐾
п
+𝛼
н
.
(22)
Making a cancellation by e ^ (k ^ (2πτ / z i)) from
equations (19) and (20), we determine the
dependences for finding the amplitude-phase
characteristics of the k-x components of the desired
temperatures:
𝜃
в
=
𝜀
в
𝑇
в
𝜃
+(𝐾
+𝐾
д
)𝜃
н
С
в
𝜌
в
𝛿
в
𝑘
2𝜋
𝑧
𝑖+(𝐾
+𝐾
д
)
;
(23)
𝜃

=
𝐴
𝜃
+𝐾
п
+𝜃
в
+𝛼
н
𝜃
н
С
𝜌
𝛿
𝑘
2𝜋
𝑧
𝑖+𝐾
п
+𝛼
н
.
(24)
The values θ_ink and θ_ck are generally complex
numbers. Using relations (7) and (8), we obtain the
dependences for determining the coefficients of the
Fourier series:
𝑥
=𝑅𝑒
(
𝜃

)
;𝑦
=−𝐼
(
𝜃

)
,
(25)
𝜇
=𝑅𝑒
(
𝜃
в
)
;𝜂
=−𝐼
(
𝜃
в
)
,
(26)
where Re (θ_ck), Re (θ_vk) - real parts of
complex numbers;
I_m (θ_ck), I_m (θ_vk) are the coefficients of the
imaginary parts of the complex numbers θ_ck and
θ_vk.
Correlations (23) and (24) are algebraic
expressions and make it easy to determine the
amplitude-phase characteristics, and hence the
coefficients of the Fourier series. Rows (3) and (4)
should have as many components as are contained in
the external thermal effect. As already noted, the
outside air temperature and the intensity of solar
radiation are well described by the first three
harmonic components, therefore, dependencies (23)
and (24) will also contain three harmonic
components.
The outlined method was used to determine the
temperature regime of solar desalination plants of
inclined-step type by analogy with previous studies
(Garg, 1987; Hamed et al., 1993; Roca, 2008; Al-
Othman, 2018; Zheng et al., 2021).
4 RESULTS AND DISCUSSION
The results of temperature calculations based on the
obtained dependences and experimental data (see
Figure), Coinciding with an error not exceeding 7-
10%, allow us to assess the validity of the described
method for calculating the temperature regimes of
solar desalination plants and the possibility of its
application to analyze the operation of various low-
potential plants.
Note that the greatest difficulty in calculating the
temperature regime of a solar desalter is the
determination of the heat transfer coefficients in the
inner volume of the desalter, since heat transfer
occurs simultaneously when there is convection,
radiation and phase transformations on the heat
exchange surfaces.
ISC SAI 2022 - V International Scientific Congress SOCIETY OF AMBIENT INTELLIGENCE
530
It is important to describe the total coefficients of
the fluxes using the method of successive
approximations, since the convective and radiant
components of heat fluxes are functions of the
temperatures of the heat exchange surfaces, which are
determined in the process of thermal engineering
calculation of the desalter.
Figure 1: Temperature range of solar desalination plant: 1 -
water temperature; 2 - temperature of the transparent
coating; a - calculation; b - experiment.
Research analysis on increasing the productivity
of solar desalination plants (Achilov, 1976; Baum,
1985) shows that the improvement of their designs is
possible through the most rational use of incident
solar energy while minimizing some energy losses.
Thus, the heat transferred by radiation from the
surface of the water to the surface of the transparent
coating can be reduced by installing additional
transparent screens between the evaporating zone of
the desalter and its roof, by analogy with work
(Timakova, 2006; Temerov, 2008; Prakash, 2019).
This technical solution makes it possible to increase
the productivity of inclined-step type installations by
1.5 times in comparison with single-layer glazing.
Solar absorption and reflection of energy from the
transparent wall and the condensate layer, which
make up to 20% of the incident energy (Baum, 1985),
can be reduced by applying an interference layer to
the roof material (Brdlik, 1983) and organizing film
condensation, which eliminates reflection from
condensate droplets. In this respect, clean degreased
glass is a fairly acceptable structural material, but it is
fragile.
As a material with acceptable optical and strength
properties, it is possible to recommend a lavsan film
coated with polyvinyl spirit, which increases its
wettability. However, such a film is not strong
enough and after some time is partially washed off,
therefore, the problem of creating strong materials
that are well wetted and sufficiently well to transmit
solar energy remains one of the urgent problems at
the present time.
A promising direction in increasing the
productivity of solar desalination plants is the use of
recuperation of the heat flux supplied to the
condensation surface due to a phase transition, which
is removed by convection and radiation into the
environment and thus becomes the most significant
loss of energy. Known technical solutions for the use
of this heat flux for heating desalinated water (SNiP,
1983; Slesarenko, 1991; Smirnov, 2013), for
example, adding to the design of the desalinator
(Achilov, 1976) just one additional layer of the
condenser-evaporator. At the same time, an increase
in its productivity was established by almost 40%.
The heat flow, which is removed by the flowing
hot distillate, also refers to significant heat loss and
can be largely recovered. So, a heat exchanger can be
connected to the distillate drain line, in which the
water supplied to desalination will be preheated.
Thus, an increase in the performance of solar
desalination plants can be achieved by recovering
heat and minimizing heat losses that cannot be
recovered.
5 CONCLUSIONS
1. To determine the temperature regime of the
desalter, a calculation method was applied based on
finding the temperature functions in the form of
Fourier series.
2. The outlined method is applied to determine the
temperature regime of inclined-step type solar
desalination plants. The results of temperature
calculations based on the obtained dependences and
experimental data, which coincided with an error not
exceeding 7-10%, make it possible to assess the
legality of the described method for calculating the
temperature regimes of solar desalination plants and
the possibility of its application to analyze the
operation of various low-potential plants.
3. One of the promising areas for increasing the
productivity of solar desalination plants is the use of
recuperation of the heat flow supplied to the
condensation surface due to the phase transition,
which is removed by convection and radiation into
the environment and thus becomes the most
significant loss of energy. Known technical solutions
for the use of this heat flux for heating desalinated
water by adding one additional layer of the
condenser-evaporator to the design of the desalinator,
in which an increase in its productivity is established
by almost 40%.
The Relationship between Temperature and Performance of Solar Desalination Plants
531
4. Analysis of studies on increasing the
productivity of solar desalination plants shows that
the improvement of their designs is possible through
the most rational use of falling solar energy while
minimizing some energy losses. Thus, the heat
transferred by radiation from the surface of the water
to the surface of the transparent coating can be
reduced by installing additional transparent screens
between the evaporating zone of the desalter and its
roof. This technical solution made it possible to
increase the productivity of the inclined-step type
installations by 1.5 times in comparison with single-
layer glazing.
REFERENCES
Achilov B.M., Zhuraev T.D., Shadyev O.Kh., 1976. Solar
water makers and refrigerators. –Tashkent: Fan, 1976.
–104 p.
Adeala, A. A., Huan, Z., & Enweremadu, C. C. 2015.
Evaluation of global solar radiation using multiple
weather parameters as predictors for South Africa
provinces. Thermal Science, 19(suppl. 2), 495-509.
Al-Othman, A., Tawalbeh, M., Assad, M. E. H., Alkayyali,
T., & Eisa, A., 2018. Novel multi-stage flash (MSF)
desalination plant driven by parabolic trough collectors
and a solar pond: A simulation study in UAE.
Desalination, 443, 237-244.
Baum V.A., Bayramov R., Rybakova L.Ye. and other 1985.
Use of solar energy. - Ashgabat: Ylym, 1985. -280 p.
Brdlik P.M., 1983. Heat transfer of a horizontal isothermal
cylinder under natural convection // High Temperature
Thermal Physics (TVT). -1983. - Vol. 21. - Iss. 4.
S.701-706.
Dorvlo, A. S., & Ampratwum, D. B. 1998. Summary
climatic data for solar technology development in
Oman. Renewable Energy, 14(1-4), 255-262.
Garg, H.P., 1987. Solar desalination techniques. In Physics
and Technology of Solar Energy (pp. 517-559).
Springer, Dordrecht.
Gidrometeo-Izdat, 1990. Scientific and applied reference
book on the climate of the USSR. -L.: Gidrometeo-
Izdat, 1990. -579 p.
Hamed, O. A., Eisa, E. I., & Abdalla, W. E. (1993).
Overview of solar desalination. Desalination, 93(1-3),
563-579.
Handbook on the Climate of the USSR. L.:
Gidrometeoizdat, 1966.
Hasni, A., Sehli, A., Draoui, B., Bassou, A., & Amieur, B.
(2012). Estimating global solar radiation using artificial
neural network and climate data in the south-western
region of Algeria. Energy Procedia, 18, 531-537.
Kannan, A., 2019. Off-grid solar thermal water heating
system using phase-change materials: design,
integration and real environment investigation. Applied
energy, 240, 73-83.
Kiteyev B. N. 1962. Thermal effect of solar radiation on
railcars. М.: Transzheldorizdat.
Kolodin M., 1981. Water and deserts. 1981. M.: Mysl,
107 p. –S.62-104.
Kutateladze S.S., 1979. Foundations of the theory of heat
transfer. 1979. –M.: Atomizdat, –416 p.
Le Pierrès, N., Stitou, D., Mazet, N., & Spinner, B. 2003.
Ideal Process conceptual design based on the exergetic
analysis. New coupling of thermochemical dipoles for
cold production from low grade heat. International
journal of energy, environment, economics, 12(3), 105-
115.
Lykov A. V. 1967. The theory of heat conduction. Moscow:
Higher School.
Ma, W., Liu, T., Min, R., & Li, M. 2018. Effects of physical
and chemical properties of working fluids on
thermodynamic performances of medium-low
temperature organic Rankine cycles (ORCs). Energy
Conversion and Management, 171, 742-749.
Nokali, 2007. // Power Electronics, 2007. ICPE'07. 7-th
International Conference on Daegu: IEEE, 2007. -рр.
59-61.
On the state of the world's water resources: a review of the
UN report. UNESCO, Paris, France, 2012 / per. "The
whole world", M., 2013. -36 p. /
https://elar.urfu.ru/bitstream/10995/63826/1/ere_2015
_165.pdf
Prakash, J., Roan, D., Tauqir, W., Nazir, H., Ali, M., &
Kannan, A. 2019. Off-grid solar thermal water heating
system using phase-change materials: design,
integration and real environment investigation. Applied
energy, 240, 73-83.
Roca, L., Berenguel, M., Yebra, L., & Alarcón-Padilla, D.
C. 2008. Solar field control for desalination plants.
Solar Energy, 82(9), 772-786.
Ruy, S., 2007. Thermal analysis of PT IGBT by using
ANSYS / S. Ruy, D. Han, H. Ahn, M.El. Nokali //
Power Electronics, 2007. ICPE'07. 7-th International
Conference on Daegu: IEEE, 2007. -рр.59-61.
Safarov M.M., Naimov A.A., Kobuliev Z.V., 2003.
Automatization systems for definitions heat
conductivity solids materials. Method monotonous
regite // ITCC 27 and ITES15. -USA, Oak Ridje. 26-29
October 2003. –рр.342-348.
Slesarenko V.N., 1991. Desalination of sea water. 1991. -
M.: Energoatomizdat, - 278 p.
Smirnov, R.V., Bakhvalov Yu.A., 2013, Mathematical
modeling of heat exchange processes in energy-saving
solar installations (Electronic resource). Engineering
Bulletin of the Don, №3. - Access mode:
http://www.ivdon.ru/magazine/archive/n3y2013/1782.
- Language. Russian
SNiP 2.01.01-82., 1983. Construction climatology and
geophysics. 1983. -M., - 105 p.
Sokolov, M., & Hershgal, D. 1990. Enhanced ejector
refrigeration cycles powered by low grade heat. Part 1.
Systems characterization. International Journal of
refrigeration, 13(6), 351-356.
ISC SAI 2022 - V International Scientific Congress SOCIETY OF AMBIENT INTELLIGENCE
532
Stathopoulos, T., Wu, H., & Zacharias, J. 2004. Outdoor
human comfort in an urban climate. Building and
Environment, 39(3), 297-305.
Temerov A., Yungerman M., 2008. Great desalination //
Around the world. -2008. -No. 5 (2812). –S.144-152.
Timakova O.V., 2006. Autonomous system of solar heating
and hot water supply using accumulation based on
substances with phase transitions // Avtoref. diss. Cand.
tech. sciences. -M., 2006. -20s.
Usmanov F.B., Kakhkhorov Kh.A., 2019. Temperature
regime and mathematical model of heat transfer in the
solar chamber // Wschodnioeuropejskie Czasopismo
Naukowe (East European Scientific Journal). -No.10
(50). –S.54-58.
Zheng, Y., Gonzalez, R. A. C., Hatzell, K. B., & Hatzell,
M. C. 2021. Large-scale solar-thermal desalination.
Joule, 5(8), 1971-1986.
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