Solar Water Purification Project For Mechanical Engineering

PREFACE
In Final year of Mechanical Engineering every student has undertaken one major project .
While selecting the subject or project, the following characteristics should be kept in mind.
1. It should test the skill attitude and the group range of knowledge of every student.
2. It should consider the local , social and industrial people and try to the fulfill it.
3. Preference should be given to the student and selection of project should match their
program me performance considering all their ability to works.

CONTENTS
Index of Report
Abstract
Nomenclature
List of tables
List of charts
Chapter-1 Introduction
1.1 Introduction
1.2 Principle
1.3 Types of Solar Still
1.4 Application
1.5 Scope of Work
1.6 Organization
Chapter-2 Literature Review
2.1 Introduction
2.2 Literature Review
2.3 Concluding Remark
Chapter-3 Theoretical Analysis
3.1 Introduction
3.2 Theoretical Analysis
3.3 Equations
3.4 Parameter
3.5 Dimensions
3.6 Various Losses
3.7 Various Formulas
3.8 Comparison
Chapter-4 Experimental Set-up and Planning of Experiment
4.1 Introduction
4.2 Material Selection
4.3 Requirement of m/c tools and Measuring Equipments

4.4 Experimental setup
Chapter-5 Costing
5.1 Defination
5.2 Aim of Costing
5.3 Purchase material and Labour cost
5.4 Final cost of BTSS
Chapter-6 Results and Discussion
6.1 Introduction
6.2 Results and Discussion
Chapter-7 Conclusion
7.1 Future Scope of Work
7.2 Conclusion
1. Appendix
2. References

NOMENCLATURE
Symbols Descriptions Units
H Heat transfer Coefficient W/m2
Ha Convective heat transfer coefficient W/m2
Q heat transfer in. W/ m2
T Temperature of the body in K
Q Rate of heat transfer KJ/sec.
M mass flow rate kg/sec
Cp specific heat KJ/Kg.K
ΔT Temperature Difference K
U The overall heat transfer coefficient W/m2.K
As Surface area m2
K Conductivity W/m.K
Ts Temperature of the surface fluid in K
Ta Ambient temperature in K
Tt Top cover temperature𝛿 K
V Velocity of wind m/s
L Length of tube m
D Diameter of tube m
𝜗 Kinematic viscocity m2/sec
Greek Symbols
σ The Stefan-Boltzmann Constant =
5.6703 X 10-8 W/ m2 k4
W/ m2 k4
ρ Density Kg/m3
Є Emissivity
𝛿 Insulation thickness m
Suffix
W BTSS wall, wind Velocity
H Hot
C Cold
A Ambient
F Fluid
R Radiation
0 Out side

CHAPTER 1: INTRODUCTION
1.1 INTRODUCTION
Clean drinking water is a basic human need. Many people, especially in developing
countries, do not have access to clean drinking water. Water that is dirty or salty is undrinkable,
and untreated water that looks clean is likely to have bacteria and organisms that cause sickness
and disease.
We are selecting this project for water purification by solar energy. Solar energy is non
conventional energy so it’s cheap. Also an availability of water purifier in market is very costly
compare with solar still. Solar still are useful to convert radiation energy of sun in easily.
Several kinds of very practical solar energy systems are in use today. They also illustrate
the two basic methods of harnessing solar energy: solar thermal systems, and solar electric
systems. The solar thermal systems convert the radiant energy of the sun into heat, and then use
that heat energy as desired.
A solar still is a device that produces clean, drinkable water from dirty water using the
energy from the sun.
Solar still uses the heat of the sun directly in a simple piece of equipment to purify water.
The equipment, commonly called a solar still, consists primarily of a shallow basin with a
transparent glass cover. The sun heats the water in the basin, causing evaporation. Moisture rises,
condenses on the cover and runs down into a collection trough, leaving behind the salts,
minerals, and most other impurities, including germs.
Solar stills are used in cases where rain, piped, or well water is impractical, such as in
remote homes or during power outages. It is targeted areas that frequently lose power for a few
days; solar distillation can provide an alternate source of clean water.
Although it can be rather expensive to build a solar still that is both effective and long-
lasting, it can produce purified water at a reasonable cost if it is built, operated, and maintained
properly.
Here focuses mainly on small-scale box-type solar stills as suppliers of potable water for
families and other small users.

1.2 PRINCIPLE
A solar still operates on the same principle as rainwater: evaporation and condensation.
The water from the oceans evaporates, only to cool, condense, and return to earth as rain. When
the water evaporates, it removes only pure water and leaves all contaminants behind. Solar still
mimic this natural process.
Solar still has a top cover made of glass, with an interior surface made of a waterproof
membrane. This interior surface uses a blackened material to improve absorption of the sun's
rays. Water to be cleaned is poured into the still to partially fill the basin. The glass cover allows
the solar radiation (short-wave) to pass into the still, which is mostly absorbed by the blackened
base. The water begins to heat up and the moisture content of the air trapped between the water
surface and the glass cover increases. The base also radiates energy in the infra-red region (long-
wave) which is reflected back into the still by the glass cover, trapping the solar energy inside the
still (the "greenhouse" effect). The heated water vapor evaporates from the basin and condenses
on the inside of the glass cover. In this process, the salts and microbes that were in the original
water are left behind. Condensed water trickles down the inclined glass cover to an interior
collection trough and out to a storage-bottle.
The still is filled each morning or evening, and the total water production for the day is
collected at that time. The still will continue to produce pasteurized after sundown until the water
temperature cools down. Feed water should be added each day that roughly exceeds the distillate
production to provide proper flushing of the basin water and to clean out excess salts left behind
during the evaporation process.
Fig.1.1: principle of box type solar still

1.3 COMPARISON BETWEEN SOLAR STILL AND SOLAR COOKER
 The reflection losses from water and basin above in the still and cooker.
 Single glass cover of still has more loss of heat; hence the cooker has two layer of glass
cover, which reduces the heat loss from surface. The cooker can be used for
pasteurization of water by keeping water in a box.
 The solar still gives continue supply of water, but cooker can be used for both the
purpose by few changes.
 The green house effect is used as basic principle in both cooker and still, but the cooker is
proved more efficient to absorb heat of solar energy and maintain it for long time.
 The temperature raised in solar cooker is higher due to its well insulated cover design and
arrangement of reflector glass.
 Usually the solar still is bigger than solar cooker, the outer surface of the glass is more
exposed to air causing more surface heat loss.
1.4 TYPES OF SOLAR STILLS
There are several different types of solar stills.
Pit Type
The most basic is the pit type, which is most appropriate for emergency survival situations
because it has a very low productivity. See Figure 1.2 for a diagram of the pit still.
Fig.1.2: Diagram of a pit type solar still.
Box Type

The basin or box still is the most complex type. There are many different variations, but the two
main categories of basin stills are single and double sloped. Figure 2 shows a picture of a single
sloped basin still and Figure 3 shows the double sloped still.
Fig.1.3: Diagram of a single sloped box Solar still
Double Slopped Still
The double sloped basin still is a similar but has two sloped pieces of glass rather than one.
Fig.1.4: Diagram of a double sloped basin Solar still
The benefits of the basin solar still are that it can produce several liters of water per
square meter of still, per day. With an upfront capital cost to invest in good materials, this still
can be built sturdy enough to operate faithfully with an efficiency of 30-60% for as long as 20
years.

Concentrating Collector Still
A concentrating collector still, as shown in Figure, uses parabolic mirrors to focus
sunlight onto an enclosed evaporation vessel. This concentrated sunlight provides extremely high
temperatures which are used to evaporate the contaminated water. The vapor is transported to a
separate chamber where it condenses, and is transported to storage. This type of still is capable of
producing from .5 to .6 gallons per day per square foot of reflector area. This type of output far
surpasses other types of stills on a per square foot basis. Despite this still's outstanding
performance, it has many drawbacks; including the high cost of building and maintaining it, the
need for strong, directs sunlight, and its fragile nature.
Fig.1.5: Diagram of concentrating collector Solar still
Multiple Tray Tilted Still
A multiple tray tilted still (Figure 1.6), consists of a series of shallow horizontal black
trays enclosed in an insulated container with a transparent top glazing cover. The vapor
condenses onto the cover and flows down to the collection channel for eventual storage.
This still can be used in higher latitudes because the whole unit can be tilted to allow the
sun's rays to strike perpendicular to the glazing surface. The tilt feature, however, is less
important at and near the equator where there is less change in the sun's position over the still.

Even though efficiencies of up to 50 percent have been measured, the practicality of this design
remains doubtful due to:
the complicated nature of construction involving many components;
Increased cost for multiple trays and mounting requirements.
Fig.1.6: Diagram of Multiple Tray Tilted Still
Tilted Wick Solar Still
A tilted wick solar still draws upon the capillary action of fibers to distribute feed water
over the entire surface of the wick in a thin layer. The water is then exposed to sunlight. (See
Figure)

Fig.1.7: Diagram of Tilted Wick Solar still
A tilted wick solar still allows a higher temperature to form on this thin layer than can be
expected from a larger body of water. This system is as efficient as the tilted tray design, but its
use in the field remains questionable because of:
Increased costs due to mounting requirements and essential insulation;The need to
frequently clean the cloth wick of built-up sediments, highlighting the need for an
operable glazing cover;
The need to replace the black wick material on a regular basis due to sun bleaching and
physical deterioration by ultra-violet radiation;
Uneven wetting of the wick which will result in dry spots, leading to reduced efficiency;
and
The unnecessary aspect of the tilt feature except where it is required higher latitudes.
1.5 PASTEURIZATION
What is the Pasteurization process?
Definition
Pasteurization is the cleansing process through which each particle of a food or drink is
heated to a certain temperature for a specific amount of time. Throughout this process the
temperature of the product and time-length are closely monitored to prevent contamination.
Pasteurization is a process of heating water, usually liquid, to a
specific temperature for a definite length of time, and then cooling it immediately. This
process slows microbial growth in water.

Pasteurization is not intended to destroy all pathogenic micro-organisms in the food or liquid.
Instead, pasteurization aims to reduce the number of viable pathogens so they are unlikely to
cause disease (assuming pasteurization product is stored as indicated and consumed before its
expiration date).
As water heats in a solar cooker, temperatures of 56° C and above start killing disease-
causing microbes. Water can be made safe to drink by heating it to this lower temperature only
66° C instead of 100° C (boiling) presents a real opportunity for addressing contaminated water
in developing countries.
To pasteurize water, heat it in the solar box to at least 65 degrees C (150 F) and keep the
water at that temperature or above for at least 30 minutes. If no thermometer is available, heat
until bubbles are rising from the bottom steadily. Natural waxes, such as beeswax, can be used to
indicate pasteurization temperature.
Solar conditions, weather conditions, latitude and box efficiency are all variables that affect
the ability of solar boxes to pasteurize water. As a general guideline, 4 liters of water can be
pasteurized in about 3 hours on a day with strong sunlight and the sun high in the sky. The
plastic- or glass-covered.
Purpose
The pathogens contained in water were discovered to transmit tuberculosis, scarlet fever,
diphtheria and a number of other diseases.
1. The first purpose of pasteurization is to kill these harmful pathogens to make water
safe for human consumption.
2. The second purpose of pasteurization is to extend the self-life of consumable water.
1.6 APPLICATIONS
The energy from the sun used to distill water is free. But the cost of building a still makes
the cost of the distilled water rather high, at least for large-scale uses such as agriculture and
flushing away wastes in industry and homes. Consequently, the solar still is used principally to
purify water for drinking and for some business, industry, laboratory, and green-house
applications. It also appears able to purify polluted water.
 Solar distillation can be a cost-effective means of providing clean water for drinking,
cooking, washing, and bathing--four basic human needs.
 It can improve health standards by removing impurities from questionable water supplies.
 It can help extend the usage of existing fresh water in locations where the quality or
quantity of supply is deteriorating.

 Where sea water is available, it can reduce a developing country's dependence on rainfall.
 Solar stills, operating on sea or brackish water, can ensure supplies of water during a time
of drought.
 Solar distillation generally uses less energy to purify water than other methods.
 Solar distillation will permit settlement in sparsely-populated locations, thus relieving
population pressures in urban areas.
1.7 SCOPE OF WORK
We have study the how the solar still works and also it is practically possible or not. Also
we have calculates its efficiency. Solar still is to make water pasteurized by using the solar
radiation energy. The solar energy is non convectional energy which easily available
everywhere. In this chapter we are also analyze or evaluated its design by using the commercial
solar cooker convert in to the solar still.
CHAPTER 2: LITERATURE REVIEW
2.1 INTRODUCTION
This chapter is consist of Literature review of the box type solar still. Which gives a base
to present this work with reference to various research papers the study and ideology to design
the equipment is considered. The following Literature surveys focuses on the solar still but also
includes other renewable energy sources. The Solar still papers gives insight how far the field is
developed.
2.2 LITERATURE REVIEW
1. A.Mahesh, C.E. Sooriamoorthi, A.K.Kumaraguru,Department of Solar Energy, School of
Energy, Environment and Natural Resources, Madurai Kama raj University, (University with
Potential for Excellence) performed and experiment, that solar still is tested for the various input
water depths like 0.5,1.0,1.5,2.0,2.5,3.0 cm. And also the second experiment is conducted using
tap water, sea water, and dairy water’s samples were preheated at two different temperatures of
25 0C and 65 0C respectively.
From this experiment they concluded the tap water showed the maximum rate of
efficiency with a depth of 1.5cm compare to that of the other water depths.
And the other experiment with different preheated water samples, the tap water showed
the maximum efficiency compared to the other samples.

2. C.N.NATARAJ AND Dr. E.S. PRAKASH dept. of studies in mechanical engineering
university BDT College of engineering Davangere.
They performed that single basin double slope solar still and a similar one coupled with flat plate
collector to study the effect of augmentation on the still performance under local condition.
The purpose of this work is to evaluate the augmentation in productivity of the still. The
productivity of the still increases nearby 40% when it is coupled to flat plate collector.
3. Robert E. Foster, New Mexico State University, MSC 3 SOLAR, P.O. Box 30001Las
Cruces, New Mexico, 88003-8001 USA
For the past decade, solar distillation has been introduced and applied as an option for
household drinking water for several colonies communities along both sides of the U.S.-Mexico
border. Purifying water through distillation is a simple yet effective means of providing drinking
water in a reliable and cost-effective manner. Solar stills effectively eliminate all water borne
pathogens, salts, and heavy metals. Solar distillation produces an ultrapure water that is superior
to most commercial bottled water sources. Three organizations have been active in promoting the
use and development of solar distillation on the Border, namely the El Paso Solar Energy
Association,
New Mexico State University and Sol Aqua. Commercial still costs were halved over the
past decade due to manufacturing improvements. Over 200 Borderland families have adopted
cost-shared solar distillers to meet their drinking water needs. In addition, Sol Aqua has worked
with Sandia National Laboratories with accelerated aging and other materials testing. This paper
discusses solar still performance and acceptance along the U.S. Mexico border.
Clean drinking water remains one of the most important international health issues of
today, and solar energy offers important and effective solutions in meeting potable water needs
worldwide. Low cost solar stills offer an immediate and effective solution in reliably providing
safe drinking water year after year. Single-basin solar stills are easy to build, inexpensive and
extremely effective in distilling water with a high total dissolved salt content and in killing
bacteria such as cholera and E. Coli. Single basic solar stills can use commonly available
equipment, based on proven solar still designs. Average water production is about 0.8 liters per
square meter per sun hour. Solar stills can bring immediate benefits to their users by alleviating
chronic problems caused by water-borne diseases.
Solar stills offer the only realistic and cost-effective means to provide safe drinking for
many Borderland colonias residents who have few other realistic and affordable options
available. Likewise, solar stills have tremendous potential worldwide in economically addressing
rural potable water needs and in saving lives. The Borderlands solar distillation water
purification projects have been an overall success. This technology calls for a different approach
to providing purified water in that it only purifies the limited amounts of water that will be
ingested by humans. Water used to flush the toilet, take a bath, wash clothes, etc. does not need
to meet the same high level of purity as water that is ingested. As Border water supplies grow
increasingly scarce and more difficult to purify (i.e. increasing salinity), solar distillation offers a
practical, effective, and relatively inexpensive means for residents to purify their drinking water.
It can be practically applied on a decentralized and immediate basis by any end-user around the
globe.

2.3 CONCLUDING REMARK
1.The tap water shows maximum efficiency at a height of 1.5cm to 2.5cm & with different
preheated water samples, the tap water showed the maximum efficiency.
2.Solar still productivity increases about 40% when coupled to flat plate collector and also
production rate decreases with increasing water depth.
3.Single basin solar stills are easy to build inexpensive with a high total dissolved salt content
and in killing bacteria. Solar stills have tremendous potential world in economically addressing
rural portable water needs & in saving lives.
CHAPTER 3: THEORITICAL ANALYSIS OF BOX TYPE SOLAR STILL (BTSS)
3.1 INTORDUCTION
Analysis of solar still is most important topic of our project. There are lots of pasteurizer are
available in market for purification of water. The cost is high and it require conventional energy.
The use of solar energy for pasteurizes water. This chapter contains theoretical analysis of BTSS.
The various components are identified and analyze theoretically with relevant references.
Components use in solar still –
Major components:
 Basin.
 Support structure.
 Double glass Transparent Top cover.
 Storage tank
Ancillary components:
 Insulation (usually under the still)
 Sealants
 Piping and valves
 Temperature Indicator

 An external cover
 Reflector
3.2 SIMPLE THERMAL ANALYSIS OF BTSS
From the First Law of Thermodynamics, you know that the amount of energy exiting a
system can never be greater than the amount of energy entering a system. The heat load can be
conservatively estimated to be equal to the amount of electricity consumed if electricity is the
only form of energy entering a system.
During pasteurization heat gain water by solar irradiation:
Q = m x Cp x ΔT ….. (3.1)
Conduction
In general, the rate of conductive heat transfer is given by:
Qcond= K(∆𝑇/∆𝑋) ….. (3.2)
Convection
Qconv = U A (T0 - Tin) ….. (3.3)
Radiation
In general, the rate of radiation heat transfer from the top surface and sky given by:
Qrad = σ .A.F1-2(Ts
4 - Tsky
4 ) ….. (3.4)
Where Tsky = Temperature of sky= 0 K, F1-2=1
3.2.1 FREE CONVECTION IN THE BTSS
Free convection can form the dominant mechanism of heat loss in a solar thermal device and
therefore it is the key item limiting the collectors efficiency.

In case of parallel layer of stationary fluid of thickness L and having a temperature Th on one
face and Tc on the other (refer fig.3.1) Th being greater than Tc, the heat flux q (i.e. heat flow rate
per unit area) is given by eq. (3.1)
q = kf (Th– Tc) / L ….. (3.5)
Fig. 3.1: Horizontal fluid layer (θ = 0)
 Nusselt Number
To calculate the heat transfer across and inside the double glass layer by convection , a
dimensionless number called the Nusselt number(Nu.) is introduced.
qa= ha (Th – Tc)
therefore ha = qa/(Th – Tc) represent the corresponding heat transfer coefficient
then Nusselt Number is defined by following equation.
Nu = ha L / k ….. (3.6)
Nu represents the ratio of the heat across the fluid layer in the convection situation compared to
that in the purely conducting situation.
 Rayleigh Number
It is evaluated at a mean temperature, Tm, its defined as
Tm = (Th + Tc) / 2
= 1/Tm

The Rayleigh Number Ra, and the prandtl number Pr. They are defined by following equation
Ra = {g.. ( Th – Tc ) L3 }/∝.ν ….. (3.7)
 Prandalt number
Pr= Cp ./K ….. (3.8)
Where ∆T = Th – Tc. When Pr. Number it is restricted to gases, then its value varies very
less , so dependence of Nu on Pr is, very slight ,so that Prandtl number effect can be ignored for
gases. The calculation for Pr. Will be ignored for double glass cover.
 The Horizontal Layer of air between double layer glass cover
The horizontal layer as sketched in fig.3.2 is a represents the layer found in BTSS. When
it is found stationary the Nu= 1
At Rayleigh Number slightly greater than 1708, an instability in the stationary state result in the
formation of cellular motion in the fluid. The experimentally measured Nu-Ra relationship(fig.
3.2) for air .
Nu = 1 + 1.44 [1 – 1708/Ra ]* + [ ( Ra/5380) 1/3 – 1] * ….. (3.9)
where a square bracket having subscript dot indicate that if the argument inside the brackets is
negative, the total quantity is taken as zero, otherwise the brackets behave normally.
2
20
40
1
4
6
8
10
8
103 410 510 610 710 810
Nu

Fig.3.2: The experimentally measured Nu-Ra relationship for with (θ = 0)
3.2.2 COMBINED FREE CONVECTION AND RADIATION COEFFICIENTS ACROSS
AIR LAYERS
 Air Layers between two glass of cover and between water surface and bottom glass of cover
Heat transfer across parallel air layer takes place in the BTSS by two mechanisms. Namely free
convection and thermal radiation. It is described in table No.
Table No 3.1. Radiation and convection heat flow in BTSS
Particular Description
Convection 1. The convection heat transfer above the surface of top cover.
2. Convection heat transfer between the two glass cover, which is minimize by
considering Rayleigh No. upto 1708.
3.The convection heat transfer above the surface of water it is to be minimized,
but the glass cover is air tight than it is considered that air is stagnant hence
convection is negligible.
Solar Radiation 1. It is transmitted through the covers towards the absorber tray, and the
thermal radiation arising from the emission of radiation by basin.
2. Long wave radiation emits from tray surfaces at a lower temperature than
sun when no water is present. The long wave radiations do not cross the double
glass cover. This is also called green house effect.
3. When water is present in the still then the heat transfer due to radiation from
the basin is minimum can be neglected.
4. When after is present the heat transfer due to radiation from the water
surface to fluid layer-1.
5. The solar radiations incident on the Top glass cover a part of it will be

reflected and remaining will be transmitted inside the still and absorbed by the
glass .
In actual the net long wave radiant exchange of heat across the air gap between basin and cover
hence it is to be expressed as heat is given by eq. (3.7)
qr = { σ . (Th
4
– Tc
4 )}/ (1/Є h + 1 / Є c - 1 ) ..(3.10)
The quantity 1 / (1/Є h + 1 / Є c - 1 ) termed as effective emissivity of the body.
The radiant heat transfer coefficient can be defined as work done for convective heat transfer
coefficient. Hence, h r = qr / ( Th - Tc )
h r = { σ . (Th
4
– Tc
4 )}/ {(1/Є h + 1 / Є c - 1 ) ( Th - Tc )} ….. (3.11)
Total heat flux availab le at bottom surface of bottomglass of cover
qT = qa + qr = ha ΔT + hr ΔT ….. (3.12)
 Heat Loss from the top cover
heat loss is the important and major loss in a BTSS. The variables determining the
upward heat flux are.
i. Temperature of the absorber (Basin).
ii. Temperature of the outer air and sky.
iii. Number of glass covers and spacing.
iv. Tilt of glass plates from the horizontal.
v. Wind velocity over the top cover.
The first four are important in all cases while the wind velocity assumes importance when
the solar thermal device consists of a single glass cover.
Assumptions
 The steady state unidirectional heat flow from Top cover, backs and sides of BTSS.

 Heat Flow Mechanism: The loss from basin to the first glass cover is by radiation and
convection. No radiant heat is transmitted through the glass as glass is opaque to long wave
radiation
 The Basin temperature do not exceed 150oC to 175oC. when no water is present.
 The basin temperature donot exceed 90 oC to 95 oC when water is present.
 The same quantity of heat is transferred through the upper face of the bottom cover to the
lower face of the top glass cover by radiation and convection.
 Consider thermal resistance within glass plate/cover is negligible compared with plate-to-plate
resistance.
 The mean temperature may be assigned to each glass plate.
Since the air is diathermic to radiation, the loss of heat by convection from a basin to an air space
equals the loss by convection from air space to next bottom plate of cover. The convection loss
from glass plate to next glass plate by air gap between two glasses of cover to out site air . The
schematic diagram of a BTSS is shown in fig.3.4.
Fig.3.3: Schematic diagram of box type solar still (BTSS)
The heat flux qa by convection for fluid layer-1 is given by eq. (3.13)

qa1 = hal (Thl – Tcl) ….. (3.13)
and the radiation heat flux qr for fluid layer - 1 is given by eq. (3.14)
qr1 = {σ . (Th 1
4 - Tc 1
4 ) }/ (1/Є h 1 + 1 / Є c 1 - 1 ) ….. (3.14)
Total heat loss from the fluid layer-1 is given by qTl = qal + qrl
Radiative heat transfer coefficient in fluid layer-1
hr 1 = {σ . (Th 1
2 + Tc 1
2 ) (Th 1 + Tc 1 )}/ (1/Є h 1 + 1 / Є c 1 - 1) ….. (3.15)
The same heat flux occurs from first glass cover to the second glass cover and so for
fluid layer – 2. Under steady state qT1 = qT2.
qa2 = ha2 (Th2 – Tc2) ….. (3.16)
qr2 = {σ . (Th 2
4 - Tc 2
4 )}/ (2/Є gl a s s - 1) ….. (3.17)
The total heat losses from the second fluid layer-2 is qT2 = qa2 + qr2
Heat transfer coefficient in fluid layer-2
hr2 = {σ . (Th 2
2 + Tc 2
2 ) (Th 2 + Tc 2 )} / (2/Є gl a s s - 1) ….. (3.18)
The radiant interchange between the top cover and the sky
qr3 =  . Є gl a s s (Tt
4 – Tsky
4 ) ….. (3.19)
Tsky = 0.0552 Ta
3/2 ….. (3.20)
Tt = Top cover temperature
Heat transfer coefficient between top cover and and the sky
hr3 = Є gl a s s . . (Tt
4 – Tsky
4) / ( Tt - Tsky ) ….. (3.21)
Heat carried away by the ambient air at a temperature Ta moving with a velocity Vw from the
upper surface of the top cover which is at a temperature Tt the heat transfer coefficient to the
wind speed.

hw = 5.7+3.8 Vw ….. ( 3.22)
 Rear Losses
The heat lost by conduction from back and side
q b or s = ki ( Th1 - Ta ) / δ i ….. (3.23)
h b & s= ki / δi ….. (3.24)
 Radiation heat transfer coefficient from honeycomb walls can be calculated from eq. (3.25)
hr2 = [1 / (1/Є h 2 + 1 / Є c 2 + {Є w
r (A.R) + 1}] . { (Th2
4 – Tc2
4)}/ (Th2 – Tc2) …..(3.26)
A.R.= Aspect ratio (L/w), r = Constant (equal to 1 for glass)
3.2.3 THERMAL NETWORK OF BTSS
The thermal network for a solar still with a double glass cover is shown in fig.3.4. The
tray absorbs solar Energy. This absorbed energy is distributed to losses through top, bottom and
edges and to useful energy gain. The overall heat transfer helps to convert thermal network
shown in fig.3.4(a) to the equivalent thermal network of fig.3.4 (b)

Fig. 3.4 : Thermal network of box type solar still (BTSS).
 The breakdown of heat losses in solar still are as follows:
Table 3.2 Heat losses in box type solar still
Type of losses Percentage
Edge 1 – 3
Back 5 – 10
Radiation 5 – 7
Convection 25 – 30
 Heat losses in solar still
Heat losses in solar still based on thermal network are given in table 3.2.
Table 3.3 formulae obtained from thermal network for heat losses
Description Formula
Upward heat loss
 Basin to 1st Glazing , convection and radiation losses
through fluid layer-1
 Convection and radiation losses through fluid layer-2
 Heat loss from the top surface due to radiation and
wind velocity
R1 = 1 / (ha1 + hr1)
R2 = 1 / (ha2 + hr2)
R3=1/hw+hr3

Rear heat loss through insulation
 Back loss
 Side loss R4 = 1 = δ i
hb ki
R5 = 1 = δ i
hs ki
Heat loss coefficients
 The top loss coefficient from the cooker absorber
 The back loss coefficient
 The side loss coefficient
 The overall heat loss coefficient
Ut = 1 / ( R1+R2+ R3 )
Ub = 1/R4
Us = 1/R5
UL = Ut + Ub + Us
3.2.4 Effect of different color in solar still
We are using apoxy black coated material in solar still because of its radiation
absorption capacity is higher than all other colour so its increase efficiency of
solar still. and give better result in less time.
Table No 3.4. Description of surfaces with Absorptivity and Radiation
Sr.No Surface Solar Radiation
Absorption(α)
Low
Temperature
Radiation at
25oC
1 Polished alluminium 0.15 0.06
2 White 0.14 0.97
3 Yellow 0.30 0.95
4 Cream 0.25 0.95
5 Light gray, green blue 0.50 0.87
6 Mid. Gray, green blue 0.75 0.95
7 Dark gray, green blue 0.95 0.95

8 Black 0.97 0.96
Fig. 3.5 : Diagram of Solar Load Vs Temperature rise
3.2.6 STORAGE TANK
The design of storage tank is depend upon the capacity of BTSS. And the cooling of hot water is
through conduction and convection process.
The heat transfer is given by the basic equation,
Qtotal = mcp ΔT ….. ( 3.27)
Mass of water is depend upon by the capacity of the box type solar still. And also the decide
specific heat for water.
In storage tank the upper surface of water is cooled by the natural convection and the side and
bottom part of tank is cooled by the conduction process.
The heat transfer through conduction is given by the basic equation for conduction process.
Qcond =(K x Acond x ΔT)/L ….. ( 3.28)

The thermal conductivity (K) is depends upon which material we are selected for conduction
process.
The heat transfer through convection in storage tank is given by the basic equation for
convection process
Qconv = hw x Aconv x ΔT ….. (3.29)
Heat carried away by the ambient air at a temperature Ta moving with a velocity Vw from the
upper surface of the top cover which is at a temperature Tt, the heat transfer coefficient of
convection to the wind speed.
hw = 5.7+3.8 Vw ….. (3.30)
The wind velocity of the air (Vw) is decided by the weather analysis chart as per the location of
particular city.
The total heat transfer through the storage tank is given by
Qtotal = Qcond. + Qconv. ….. (3.31)
Using the eqn. calculate the area of the conduction by using the relation below,
Here we are considering the storage tank top surface area is vary between 17% to 40% for the
cooling through natural convection and the remaining part of the storage tank is cooling through
conduction.
Qcond. = 0.6 X Qtotal ….. (3.32)
Qconv. = 0.4 X Qtotal ….. (3.33)
Using above value of convection and conduction find the area of that particular conduction
(Acond) and convection (Aconv) process eqn. (3.28,3.29),
As=Aconv + Acond ..… (3.34)
Now, eqn. (3.39) calculate the surface area required for the cooling of hot water through
conduction and natural convection.
3.2.7 CHARACTERISTICS OF WATER
Density is a measure of how compact a substance is. It is defined as the mass of a
substance divided by its volume. Solids are almost always the most dense form of a substance,
then liquids and then gases. As temperature increases, the density generally decreases. Pure

water is an exception to this and is the only substance which has its highest density as a
liquid. Water is at its most dense at about 4 oC. This is because hydrogen bonds between water
molecules give ice a very stable open ordered structure. At low temperatures, water has a
higher density than ice and this means that ice floats.
Fig.No.3.6: Variation of water density vs Temperature.
Table No.3.5 CHARACTERISTICS OF DRINKING WATER SUPPLIED .
Parameter Average Results Drinking water
Permissible Limit
BIS:10500-1991
Colour Slightly whitish 25 Units
Odour Chlorinous Unobjectionable
Turbidity (NTU) 7 10
Total Dissolved Solids (mg/L) 385 2000
Total Hardness (mg/L) ( as CaCO3 ) 114 600
Calcium (mg/L) (as Ca) 26 200
Magnesium (mg/L) (as Mg) 12 -

Chloride (mg/L) (as Cl ) 109 1000
Sulphate (mg/L) (as SO4 ) 54 400
Ammoniacal Nitrogen (mg/L) (as N ) 0.07 -
Albuminoid Nitrogen (mg/L) (as N ) 0.30 -
Nitrite (mg/L) (as N ) Nil -
Nitrate (mg/L) (as NO3 ) Nil 100
Phenolphthalein Alkalinity (mg/L) ( as CaCO3 ) Nil -
Total Alkalinity (mg/L) ( as CaCO3 ) 62 600
Phosphates (mg/L) (as PO4 ) 0.015 -
Iron (mg/L) (as Fe ) 0.10 1.0
PH 7.1 6.5 - 8.5
Silicates (mg/L) (as SiO2 ) 10 -
Fluoride (mg/L) (as F ) 0.10 1.5
Specific conductance (micro mhos/cm) 595 -
3.3 CONCLUSION
The present chapter has outlined the development of the model used to simulate the box
type solar still operation. Here we calculate the thermal effect which is occurs during
process. By thermal analysis we conclude that water can be pasturised at minimum cost and
minimum time.

CHAPTER 4 : EXPERIMENTAL SETUP AND PLANNING OF EXPERIMENT
4.1 INTRODUCTION
In this chapter, we have arranged the full experiment set-up, which is appropriate to the
solar still system work easily. Also the work to be carried out by the experimental set-up is
properly or not. Here the decide the full experiment procedure and process planning for our
project. And through full arrangement of the experimental set-up to full-fill the result which is to
be achieved. So this chapter is also useful for our project work.
4.2 EXPERIMENTAL SET-UP

Fig. 4.1: Experimental Set-up of BTSS
Experimental work to be carried out
A standard commercial Box Type Solar Still with the following specification was used:
Capacity: 20 litres
Effectiveness factor: 80 %
Power consumption: Through Solar Energy
Dimensions: (400mm x 436mm x 125mm)
Experiment procedures
The procedures will be as follows:

a) Water inlet in box type solar still’s basin, thermometer is placed in for temperature
measurement.
b) Water will be heated at 80 0C to 90 0C by solar energy.
c) Then this water will be drawn to the storage tank through pipe, in the storage tank water will
be cooled by natural convection.
d) Here in storage tank the water will be cooled and temperature will be reached at 35 0C
e) The filter is provided at the outlet of storage tank which removes dust particals from water.
f) Then filtered water is brought to earthen pot through pipe for further normal cooling of water.
g) Here in earthen pot water temperature reach at 27 0C to 30 0C.
Results to be achieved
The pasteurised drinkable water will be obtained at effectiveness of greater than 80% of solar
still.
4.3 MATERIAL SELECTION
Sr. No. Name of the parts Material Quantity
1. Solar Cooker Alluminium 1
2. Steel Tank Steel 1
3. Flexible Pipe PVC 2mtr
4. ½”Elbow PVC 2
5. ½”Tee PVC 2
6. ½”Washer PVC 2
7. ½”Valve PVC 1

8. Bush PVC 2
9. ¾”Angle Mild Steel 14 Kg.
10. N.C.Paint - 500ml
11. Thinner - 500ml
4.4 REQUIREMENT OF M/C TOOLS AND MEASURING EQUIPMENTS
 Requirment of Machine Tools
 Hacksaw Machine
 Welding Machine
 Soldering Machine
 Drilling Machine
 Requirment of Different Equipments
 Hacksaw Blede
 Cutting Tools
 Welding Rod
 Hammer
 Sizzer
 File
 Measuring Instruments
 Thermometer
 Measuring Tap
 Shrinkage Rule

CHAPTER 5 : COSTING
5.1 INTORDUCTON
It is the determination of actual cost of article after adding different expensive incurring
in various departments. It may also be definite as a system which systematically. Record and the
expenditure included in the various departments.
To determine any the cost of manufacture product.
5.2 AIM OF COSTING

The important aim and object of costing are as follows:
1. To determine the cost of each article.
2. To determine the cost of each article operation to keep central over head expenses’.
3. To supply information for costing of wastage.
4. It helps in reducing the total cost of manufacture.
5.3 PURCHASE MATERIAL AND LABOUR COST
Sr.
No.
Name of Parts and Materials Rate Quantity Total Rupees
1. Solar Cooker 3500/piece 1 3500
2. Glass 140/piece 2 280
3. Wooden Frame 180/piece 1 180
4. Stainless Steel Sheet 300/kg 2kg 600
5. NC Black Coating 225/Lt 400ml 90
6. Brush 12/piece 1 12
7. Thinner 70/Lt 500ml 35
8. Galvanised Sheet 45/kg 3.5kg 158
9. Earthen Pot 65/piece 1 65
10. M.S.Angle 40/kg 13.5kg 540
11. All PVC Fittings - - 275
TOTAL 5735
5.3 FINAL COST OF BTSS
PRIME COST
= Total cost of purchase material and part + Labor cost
= 5735 + 755
=6490 Rs.
SALES AND DISTRIBUTION OVERHEAD COST

= 10% of Prime Cost
= 649 Rs.
TOTAL COST OF BTSS
= Prime cost + Sales and Distribution Overhead Cost
= 7139 Rs.
PROFIT
= 10% of Total Cost
= 714 Rs.
SALING PRICE
= Total Cost + Profit
= 7850 Rs.
CHAPTER 6 : RESULTS AND DISCUSSION
2.1 INTRODUCTION
2.2 RESULTS AND DISCUSSION

CHAPTER 7: CONCLUSION
7.1 FUTURE SCOPE OF WORK
The solar energy is non convectional energy which easily available everywhere.
So its an environmental friendly product. In this chapter we are also analyze or evaluated its
design by using the commercial solar cooker convert in to the solar still.
The solar still is using water to in drinkable form and also pasteurized water. In
future we have using these solar still to get the distilled water. Also its make water to in
drinkable form.

In future the solar still is give a different impression in big industries and special
occasions.
7.2 CONCLUSION
We have given detail explation of our project. We finally conclude that our project is
completed in a given time limit with satisfaction. While doing this project we learn about various
engineering fields helps each other to make different kind of work easily. We visited various
industries, work shop and engineering shop. We also know about cost of various materials,
which we required. We learn the group works from this project, which is important for our future
industrial life and how to manage with different skill persons and how to work different
condition without loosing more time, how we can give our best work to our project/industrial
life.
Finally we are very thankful all group members and our all the mechanical department
professors and H.O.D. and also our class collogues, which directly of indirectly help us to
complete this project on time.
APPENDIX- I
Sample Calculations:
Performance evaluation of Box Type Solar Still
Table 1. Radiation properties of some surface coatings and materials used in solar still.
Sl.
No.
Description
Solar Energy
Absorptance α
Long waves Radiation
admittance Є

1. Black Enamel Paint 0.83 0.83
2. Lamp Black 0.95 0.95
3. Sol chrome (Black chrome on nickel
plated copper Substrate)
0.965 0.15
4. Lamp Black in Epoxy 0.96 0.89
5. Selective Paint 0.94-0.96 0.35-0.45
6. Aluminium 0.09-0.1 0.102-0.113
7. Parsons Black Point 0.98 0.981
Table 2. Physical and optical properties of some glazing materials available in India
Sl. No. Description
Thermal Conductivity (K)
W /m K
Transmittance
1. Glass 0.640 - 0.7443 ---
2. Safex (4mm) 0.84-0.88
3. Atul (5mm) 0.80-0.84
4. Vallabh Glass 0.80-0.85
Fig .1

Fig2
Below Table shows break down of Heat losses in solar cookers
Type of losses Percentage
Edge 1 – 3
Back 5 – 10
Radiation 5 – 7
Convection 25 - 30
THERMAL NETWORK OF BOX TYPE SOLAR STILL
The thermal network for a Box type solar still with a double glass cover is shown in fig.
The tray absorbs solar Energy. This absorbed energy is distributed to losses through top, bottom

and edges and to useful energy gain. The overall heat transfer helps to convert thermal network
shown in fig.(1) to the equivalent thermal network of fig.(2)
Heat Transfer Calculations For Fluid Layer-1
Data used for calculation as given below:
Th1 = 75oC and Tc1 = 65oC
Tm = ( Th1 + Tc1 ) = {(75 + 273 )+ (65 + 273 ) }/ 2 = 343 K or 70oC
Properties of air at a mean temperature of 70oC
Kinematic Viscosity, ν = 20.21 x 10-6 m2/sec.
Thermal diffusivity, = 2.891 x 10-5 m2/sec
Coefficient of Volumetric expansion, β = 2.91 x 10-3 / K

g = 9.81 m/sec2 , characteristic depth L 1 =0.80 m,
Thermal conductivity of air, kf = 29.48 x 10-3 W/m K
The aperture area of glass cover, A = .436 x .436 = 0.190096m2
Є h 1 = 0.89 (refer table for Lamp Black in Epoxy)
Є c 1 =0.85 (refer table for Vallabh glass)
Ra = {g ( Th1 – Tc1 ) L3 }/ .ν
Ra = 2.5 x 108
Nu = 1 + 1.44 [1 – 1708/Ra ]* + [ ( Ra/5380) 1/3 – 1] *
Nu = 37.39
Nu = ha1 L1 / kf
ha1 = 1.38W/m2 K
qa1 = ha1 (( Th1 - Tc1 ) = 1.38. ( 75 + 273) - (65 + 273) =13.8 W/m2
Qa1 = qa1 x At = 13.8 x 0.190096m2 = 2.62 W
qr1 = σ . (Th 1
4 - Tc 1
4 ) / ( 1 / Є h 1 + 1 / Є c 1 - 1 )
qr1 = 70.41 W/m2
Qrl = q r 1 x Area = 70.41 x 0.190096 m2 = 13.38 W
Radiation heat transfer coefficient hrl

hr 1 = {σ . (Th 1
2 + Tc 1
2 ) (Th 1 + Tc 1 )} / (1/Є h 1 + 1 / Є c 1 - 1)
h r 1 = 7.04 W/m2K
Total heat Supplied to Cooker Cover through fluid layer -1
Q1 = Qal + Qrl = 2.62 W + 13.38 W = 16 W
Heat Transfer Calculations for Fluid Layer – 2
Q1 = 16 W
Thermal conductivity of glass k = 0.7443 W/m K (refer table )
Thickness of cover glass t = .003 m, L2 = 0.0125 m.
The aperture area of glass cover A = .436 x .436 = 0.190096m2
Є gl a s s = 0.85 (refer table for Vallabh glass)
The heat transferred due to conduction
Qc = {k.A (Tcl – Th2)} / L = Q1 =16 W
(Tcl – Th2) = Qc .L / k.A = ( 16x 0.003 ) / ( 0.7443 x .0190096) = 33 oC (take 1 oC)
Tcl = 338K. Th2 = 338 – 1 = 337 K
Similarly Tt - Tc2 = 1oC or K. Taking the maximum value of Tt observed
Tt = 40 oC = 313 K,
Tc2 = Tt – 1 k = 313 – 1 = 312K
The mean temperature therefore for fluid layer-2 is equal to

Tm = (337 + 312) / 2 = 324.5K or 51.5 oC (take 54oC)
The air properties at a mean temperature of 54oC as follows
Kinematic viscosity, ν = 18.61 x 10-6 m2/sec.
Thermal diffusivity,  = 2.65 x 10-5 m2/sec.
Coefficient of volumetric expansion, β = 3.06 x 10-3/K.
Taking the thermal conductivity of air, K=28.3 x 10-3 W/m K
g = 9.81 m/sec2 , characteristic depth L 2 =0.0125 m .
(Th2 – Tc2 ) = (337– 312) = 25 K
Ra = {g (Th2 – Tc2 ) L3 }/ .ν
Ra = 2973
Nu = 1 + 1.44 [1 – 1708/Ra]* + [ ( Ra/5380) 1/3 – 1] *
Nu = 1.43
Nu = ha2.L2 / kf
ha2 = 3.23 W/m2 K
qa2 = ha2 x ( Th2 – Tc2 ) = 80.75 W/m2
Qa2 = qa2 x A = 15.35 W
qr2 = {σ . (Th 2
4 - Tc 2
4 )}/ (2/Є gl a s s - 1)
qr2 = 143.41 W/m2
hr2 = {σ . (Th 2
2 + Tc 2
2 ) (Th 2 + Tc 2 )} / (2/Є gl a s s - 1)
hr2 = 5.74 W/m2 K
Qr2 = qr2 x A2 where A2 = 0.190096 m2

Qr2 = 27.26 W
Total Heat transfer from fluid layer-2
Q2 = Qa2 + Qr2 = 15.35 + 27.26 = 42.62 W
Heat transfer between top cover and sky
The aperture area of glass cover A = .436 x .436 = 0.190096m2
Average wind velocity Vw =8 kmph as per the weather analysis chart
Є gl a s s = 0.85 (refer table for Vallabh glass)
Tt = 313K
Ta = 303 K
Tsky = 0.0552 Ta
3/2 = 291.14 K
hr3 = Є gl a s s . (Tt
4 – Tsky
4) / ( Tt - Tsky )
hr3 = 0.85 x 5.67 x 10-8 x {(313) 4 – (291.14) 4}/ (313 – 291.14) = 5.26 W/m2 K.
hw = 5.7+3.8 Vw W/m2K = 14.14 W/m2 K.
Back and side losses from tray
Thermal conductivity of insulation (glass wool), k = 0.0372 W/m K
Thickness of back δi b = 52 mm

Thickness of side δi s = 74 mm
Area of the back, A b = 400mm x 400mm = 0.16 m2
Area of each side, A s = 0.08 x (0.436 + 0.400) /2 = 0.03344 m2
Th1 = 348 K and Tcasing = Ta = 303K
h b (back) = ki / δi b = 0.0372 / .052 = 0.715 W/m2 K
q b (back) = h b x ( Th1- Ta ) =32.18 W/m2
Q b (back) = q b x A b = 5.15 W
h s (side) = ki / δi s = 0.0372 / 0.074 = 0.503 W/m2K
q s (side)= h s x ( Th1- Ta ) = 0.503 ( 348 – 303) = 22.64 W/m2
Q s (side) = qs x A s x 4 = 3.03 W (four sides)
Total heat loss from the back and sides
QL(back and side) = Q b (back) + Q s (sides) = 5.15 + 3.03 = 8.18 W
Overall heat loss coefficient of solar still
Thermal Resistances
R1 = 1 / (ha1 + hr1) = 0.1188 m2 K/W

R2 = 1 / (ha2 + hr2) = 0.1115 m2 K/W
R3=1/ (hw+hr3) = 0.0515 m2K/W
R4 = 1 / hb = δ i b / ki = 1.4 m2K/W
R5 = 1 / hs = δ i s / ki = 2 m2 K/W
Overall Heat Loss Coefficient
Ut = 1 / (R1+R2+ R3) = 3.5 W/m2 K.
Ub = 1/R4 = 0.71 W/m2 K.
Us = 1/R5 = 0.50 W/m2 K
UL = Ut + Ub + Us
UL = 4.71 W/m2 K.
QL = Q2 + QL(back and side) = 50.8 W
REFERENCES
1. ↑ Heat transfer. (2010, April 15). In Wikipedia, the Free Encyclopedia. Retrieved 15:56,
April 22, 2010, from
http://en.wikipedia.org/w/index.php?title=Heat_transfer&oldid=356169993

2. ↑ Convection. (2010, April 22). In Wikipedia, the Free Encyclopedia. Retrieved 16:31,
April 22, 2010, from
http://en.wikipedia.org/w/index.php?title=Convection&oldid=357620678
3. ↑ Conduction (heat). (2010, April 21). In Wikipedia, the Free Encyclopedia. Retrieved
16:14, April 22, 2010, from
http://en.wikipedia.org/w/index.php?title=Conduction_(heat)&oldid=357403462
4. ↑ Thermal radiation. (2010, April 12). In Wikipedia, the Free Encyclopedia. Retrieved
16:18, April 22, 2010, from
http://en.wikipedia.org/w/index.php?title=Thermal_radiation&oldid=355601161
5. Pr. Kaabi Abdenacer, Smakdji Nafila, 2007, Impact of temperature difference (water-
solar collector) on solar-still global efficiency, Desalination, Volume 209, Pages 298-305.
6. K. Kalidasa Murugavel, Kn.K.S.K. Chockalingam, K. Srithar, 2008, An experimental
study on single basin double slope simulation solar still with thin layer of water in the
basin, Desalination, Volume 220, Pages 687-693.
7. Bilal A. Akash, Mousa S. Mohsen, Omar Osta and Yaser Elayan, 1998, Experimental
evaluation of a single-basin solar still using different absorbing materials, Renewable
Energy, Volume 14, Issues 1-4,
8. Robert E. Foster New Mexico state university, Ten Years of Solar Distillation
Application Along The u.s-mexico.
9. A.Mahesh, C.E. Sooriamoorthi, A.K.Kumaraguru,Department of Solar Energy,School of
Energy, Environment and Natural Resources,Madurai Kamaraj University,Design
construction and performance evaluation of low cost basin type solar still.
10. C.N.NATARAJ AND Dr. E.S. PRAKASH dept. of studies in mechanical engineering
university BDT College of engineering Davangere., Experimental Study of Single basin
solar still coupled with flat plate collector.
11. Engineering heat and mass transfer by M.M.Rathore ch-2,7,12

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