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Dr. N. Mukhopadhyay Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 5, Issue 4, ( Part -7) April 2015, pp.06-10
www.ijera.com 6 | P a g e
A Study on Energy Audit of a Cold Storage
1
Dr. N. Mukhopadhyay, 2
Raj Gopal Nanda
1
Assistant professor, Department of Mechanical Engineering, Jalpaiguri Govt.Engg. College,
2
M.Tech. Scholar, Department of Mechanical Engineering, Jalpaiguri Govt.Engg. College,
ABSTRACT
Energy consumption of a cold storage was measured for different storage temperatures. Suction temperature and
pressure temperature of the compressor and working time of the compressor were determined to reach
evaporator set up temperatures. An axial fan located back of the evaporator was used to distribute the cooled air
into the cold store. An electrical heater was used to defrost.
The compressor suction temperatures and discharge temperatures varied between 1.80
C - 070
C and 270
C - 350
C respectively. Condenser output temperature is varies 40
C - 100
C. Compressor suction pressure (p1) = 3.5
Kg/cm2
and discharge pressure (p2) = 10.5 Kg/cm2
.
Key words: Energy, Cold Storage, Refrigeration
I. INTRODUCTION
Energy auditing in a integral part of energy
conservation and energy management is also part and
parallel of conservation. Damage and supply gap is
large energy to lead to similar natural defects, Energy
disaster such as Tsunami and earth quake. The next
generation generating yet to come will be completely
light blind. It is because power never be available
after this disaster and not ever rehabilitate the
reconstruction of buildings. To avoid the energy
calamity proposed auditing report use the innovative
energy utilization schemes through which the
ferocious of situation might blindness can be
eradicated.
Cold Storage is a special kind of room, the
temperature of, which is kept very low with the help
of machines and precision instruments. India is
having a unique geographical position and a wide
range of soil thus producing variety of fruits and
vegetables like apples, grapes, oranges, potatoes,
chillies, ginger, etc. Marine products are also being
produced in large quantities due to large coastal
areas. The present production level of fruits and
vegetables is more than 100 million MT and keeping
in view the growth rate of population and demand,
the production of perishable commodities is
increasing every year. The cold storage facilities are
the prime infrastructural component for such
perishable commodities. Besides the role of
stabilizing market prices and evenly distributing both
on demand basis and time basis, the cold storage
industry renders other advantages and benefits to
both the farmers and the consumers. The farmers get
opportunity of producing cash crops to get
remunerative prices. The consumers get the supply of
perishable commodities with lower fluctuation of
prices. Commercially apples, potatoes, oranges are
stored on large scale in the cold storages. Other
important costly raw materials like dry fruits,
chemicals, essences and processed foods like fruit
juice/pulp, concentrate dairy products, frozen meat,
fish and eggs are being stored in cold storages to
regulate marketing channels of these products.
Energy consumption of an experimental cold
storage was measured for different storage
temperatures. Suction temperature and pressure
temperature of the compressor and working time of
the compressor were determined to reach evaporator
set up temperatures. Capacity of compressor,
condenser, and evaporator were 10460 kJ/h, 12552
kJ/h , and 10460 kJ/h, respectively. An axial fan
located back of the evaporator was used to distribute
the cooled air into the cold store. An electrical heater
was used to defrost. Refrigerant was R22.
Energy use in a cold storage facility is affected
by the amount of heat the refrigeration equipment
must remove and the efficiency of the equipment.
The main sources of heat in a facility for long-term
storage are transmission through walls, evaporator
coil fans, lights, air leakage, and respiration of the
stored commodity.
The electric energy consumption of existing cold
stores ranges between 30 and 50kWh/m3/year for
storage. It is depends on the quality of the building,
on the activities (chilled or frozen storage), room
size, stock turnover, temperature of the incoming
produce, outside temperatures, etc. The total cost of
electric energy is about 10 to 15% of the total
running costs of a store. Improving Energy
Efficiency (EE) has two goals: cost reduction and
environmental protection.
Objective of this research is to determine energy
consumption of a cold storage for different storage
temperatures. Energy consumption of the system
elements such as compressor, condenser and fan of
the evaporator were measured and evaluated. In
RESEARCH ARTICLE OPEN ACCESS
Dr. N. Mukhopadhyay Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 5, Issue 4, ( Part -7) April 2015, pp.06-10
www.ijera.com 7 | P a g e
addition, suction and pressure temperatures of the
compressor, condenser output temperature and
required time to reach to the each set up temperature
were determined and evaluated.
Energy auditing is one tool through which
balancing of demand and supply is determined and
the positive mismatch cannot be compensated either
by organic way or it might be difficult task.
This paper deals with different aspects of design
of cold storage and includes all standard refrigeration
principles and heat load factors which are normally
considered in a cold storage design and various
energy audits.
II. MODEL ANALYSIS
(a) Technical analysis –
I visit a cold storage at West Bengal , INDIA and collect the data which is given below :-
T1 = 2.5 0
C , T2 = 30 0
C
T3 = 4.5 0
C , T4 = 1 0
C
P1 = 3.5 kg/cm 2
, P2 = 10.5 kg/cm 2
Calculation for Actual energy : -
At first I take the data of actual energy by a compressor (KC 2) for one chamber from reading, this is equal
to = 55 KW per hour.
Now also I got this actual energy by the electricity bill for that cold storage --
Month Electricity bill
July , 2014 73,890 KWH
August , 2014 86,135 KWH
September , 2014 60,295 KWH
So, the average of this three months electricity bill is
=
73890 + 86135 + 60295
3
=
220320
3
= 𝟕𝟑𝟒𝟒𝟎 KWH
This unit is for one month and for 2 chambers only.
The running time for a month is 540 Hours.
Now, Total unit consumption for one hour and for one chamber
=
73440
540 × 2
= 𝟔𝟖 𝑲𝑾 𝒑𝒆𝒓 𝒉𝒐𝒖𝒓
[ One compressor is running for one chamber ]
Now , there is also a pump, 336 pieces of fan & 800 lights are running .
Dr. N. Mukhopadhyay Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 5, Issue 4, ( Part -7) April 2015, pp.06-10
www.ijera.com 8 | P a g e
Unit consumed by the pump = 11.19 KW
Unit consumed by the fan = 0.06 KW
Unit consumed by the light = 0.018 KW
So, the total unit consumed by this three
= [ 11.19 + 0.06 + 0.018 ] KW
= 11.27 KW
So, unit consumed by a compressor is = [ 68 - 11.27 ] KW
= 56.73 KW
This value is approximately similar to the actual energy by a compressor from reading. So, I take 55 KW/h
So,
Calculation for Theoretical energy : -
I have done this theoretical energy calculation with
three process :-
(i) The power of compressor = V . I . CosØ
Here , V = 415 volt
I = 125 Amp.
CosØ = 0.8
So, Etheoritical = V . I . CosØ
= 415 X 125 X 0.85
= 44093.75 Watt
Etheoritical = 44.09 KW per hour
(ii) Also we know,
Etheoritical = work done by a compressor
Etheoritical =
𝒏
𝒏−𝟏
𝐩 𝟏 𝐯 𝟏 {
𝒑 𝟐
𝒑 𝟏
𝒏−𝟏
𝒏
− 𝟏}
Where,
n = 1.4
p 1 = 3.5 kg/cm2
= 35000 kg/m2
= 35000/101. 972 KPa
= 343.23 KPa
v 1 =
𝜋
4
𝐷2
𝐿 where D = Bore = 160 mm
L = Stroke = 110 mm
=
𝜋
4
0.16 2
× 0.11
= 0.00221 m3
p 2 = 10.5 kg/cm2
= 105000 kg/m2
= 105000/101.972 KPa = 1029.69 KPa
Etheoritical =
1.4
1.4−1
343.23 x 0.00221 x
{
10.5
3.5
1.4−1
1.4
− 1}
= 2.665 x [ 1.375 - 1]
Etheoritical = 0.996 Joule
Here the speed of motor for compressor is = 1440
rpm and number of cylinder is = 2, then
Etheoritical =
0.996 × 2 ×1440
60
Etheoritical = 47.8 KW per hour
(iii) Now,
Heat grade energy output ( KWH)
Co-efficient of performance (COP) = -------------------
-----------------------------------
Electrical/Mechanical energy input (KWH)
COP =
𝑸
𝑾
Also, COP =
𝒅𝒕 𝟏
𝒅𝒕 𝟏−𝒅𝒕 𝟐
Where, dt1 = Condensing temperature difference
dt2 = Evaporating temperature difference
So,
𝑸
𝑾
=
𝒅𝒕 𝟏
𝒅𝒕 𝟏−𝒅𝒕 𝟐
𝑾 =
𝑸(𝒅𝒕 𝟏 − 𝒅𝒕 𝟐)
𝒅𝒕 𝟏
Dr. N. Mukhopadhyay Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 5, Issue 4, ( Part -7) April 2015, pp.06-10
www.ijera.com 9 | P a g e
Here Q = 55 KW per hour. [ It is calculated from a
journal paper]
Then, 𝑾 =
𝟓𝟓 𝑻 𝟐−𝑻 𝟑 − 𝑻 𝟏−𝑻 𝟒
𝑻 𝟐−𝑻 𝟑
𝑾 =
𝟓𝟓 𝟑𝟎𝟑 − 𝟐𝟕𝟕. 𝟓 – 𝟐𝟕𝟓. 𝟓 − 𝟐𝟕𝟒
𝟑𝟎𝟑 − 𝟐𝟕𝟕. 𝟓
𝑾 =
𝟓𝟓 𝟐𝟓. 𝟓 − 𝟏. 𝟓
𝟐𝟓. 𝟓
𝑾 = 𝟓𝟏. 𝟕𝟔 𝑲𝑾 𝒑𝒆𝒓 𝒉𝒐𝒖𝒓
Etheoritical = 51.76 KW per hour
Now , the average of this three
Etheoritical =
44.09 + 47.8 + 51.76
3
= 47.88 KW per hour
So, when I take mechanical/electrical energy loss of
the compressor then this energy is equal to
(b) Energy Gap Analysis –
There is a huge gap when I calculating the
energy difference.
Gap energy = Eactual - Etheoritical
= 55 − 50 KW per hour = 5 KW per
hour
If I take per month then it becomes :-
Gap energy = 5 × 540 KW per hour
= 2700 KW per hour
If I take per year it becomes :-
Gap energy = 2700 × 12 KW per hour
= 32400 KW per hour
(c) Cost Analysis –
This data is collected from total electricity bill of that
cold storage –
Month Unit Cost
July 2014 73890 KWH Rs. 5,38,972 /-
August 2014 86135 KWH Rs. 5,42,071 /-
September
2014
60295 KWH Rs. 4,66,395 /-
So, the average cost of one month =
538972 + 542071 +466395
3
= Rs. 5,15,813 /-
Now the excess energy for a month is equal to 2700
KWH and for a year is equal to 32400 KWH.
So the saving money is = 2700 x 7.5 = Rs. 20,250 /-
in a month.
= 32400 x 7.5 = Rs. 2,43,000 /- in a year.
III. RESULT & DISCUSSION
At first I make a programming for the equation
Etheoritical =
𝒏
𝒏−𝟏
× 𝟐 × 𝟐𝟒 × 𝐩 𝟏 𝐯 𝟏 {
𝒑 𝟐
𝒑 𝟏
𝒏−𝟏
𝒏
− 𝟏}
in KW
Where n = 1.4
The program is -
#include<iostream.h>
#include<conio.h>
#include<math.h>
int main( ) {
double p1 , p2 , v1 = 0.00221, e , x ;
cout<< “give the value of p1 , p2 / n”;
cin>> p1 >> p2
x = pow (p2 / p1 , 0.29);
e = 3.5 * 2 * 24 *(p1 * v1 * x – p1 * v1);
cout << e ;
return 0 ;
}
This programming is done for the twenty values of p1
, p2 and E which is used for making the graph plotting
–
(i) p1 vs E and (ii) p2 vs E (iii) T1 vs E
Where p1 = suction pressure, p2 = discharge pressure,
E = energy and T1 = suction tempera ture.
(i) Graph of compressor suction pressure vs compressor energy :-
The graph indicates that energy increases with increase in suction pressure
(ii) Graph of compressor discharge pressure vs compressor energy :-
Etheoritical = 50 KW per hour.
Dr. N. Mukhopadhyay Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 5, Issue 4, ( Part -7) April 2015, pp.06-10
www.ijera.com 10 | P a g e
The graph indicates that energy increases with increase in discharge pressure
(iii) Graph of compressor suction temperature vs compressor energy :-
The graph indicates that energy increases with increase in discharge pressure
IV. CONCLUSION
It has been observed that the actual energy
consumption of a cold storage by a compressor for
one chamber is 55 KW per hour and theoretical
energy consumption is 50 KW per hour. So, a gap of
5 KW per hour is found between the theoretical and
actual energy consumption by a compressor. If this
gap is fulfilled then a savings of Rs 20,250 /- per
month will be obtained which will amount to Rs
2,43,000 /- per year.
To save energy the following practices must be
implemented:-
1. Reducing Heat Loads
2. Uses of latest energy saving equipments
3. Proper Insulation
4. Efficient maintenance practices
5. Automation & Integration
There are other factor which contributes to the
total energy consumption, which are (i) lights (total
800 pcs) , (ii) fans (total 336 pcs). To increase the
efficiency, conventional lights will replaced by
energy efficient devices that is LED, CFL etc.
If we replace three compressors for three
chambers with a single equivalent compressor which
will deliver the same amount of load, then maximum
energy will be saved.
REFERANCES
[1] www.google.com
[2] http://en.wikipedia.org
[3] Engineering Thermodynamics, P. K. Nag
(Book)
[4] Willis croft PMP, NZ Rural Press Limited,
Auckland, 2007
[5] ISHRAE Publications, Air conditioning and
Refrigeration

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A Study on Energy Audit of a Cold Storage

  • 1. Dr. N. Mukhopadhyay Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 4, ( Part -7) April 2015, pp.06-10 www.ijera.com 6 | P a g e A Study on Energy Audit of a Cold Storage 1 Dr. N. Mukhopadhyay, 2 Raj Gopal Nanda 1 Assistant professor, Department of Mechanical Engineering, Jalpaiguri Govt.Engg. College, 2 M.Tech. Scholar, Department of Mechanical Engineering, Jalpaiguri Govt.Engg. College, ABSTRACT Energy consumption of a cold storage was measured for different storage temperatures. Suction temperature and pressure temperature of the compressor and working time of the compressor were determined to reach evaporator set up temperatures. An axial fan located back of the evaporator was used to distribute the cooled air into the cold store. An electrical heater was used to defrost. The compressor suction temperatures and discharge temperatures varied between 1.80 C - 070 C and 270 C - 350 C respectively. Condenser output temperature is varies 40 C - 100 C. Compressor suction pressure (p1) = 3.5 Kg/cm2 and discharge pressure (p2) = 10.5 Kg/cm2 . Key words: Energy, Cold Storage, Refrigeration I. INTRODUCTION Energy auditing in a integral part of energy conservation and energy management is also part and parallel of conservation. Damage and supply gap is large energy to lead to similar natural defects, Energy disaster such as Tsunami and earth quake. The next generation generating yet to come will be completely light blind. It is because power never be available after this disaster and not ever rehabilitate the reconstruction of buildings. To avoid the energy calamity proposed auditing report use the innovative energy utilization schemes through which the ferocious of situation might blindness can be eradicated. Cold Storage is a special kind of room, the temperature of, which is kept very low with the help of machines and precision instruments. India is having a unique geographical position and a wide range of soil thus producing variety of fruits and vegetables like apples, grapes, oranges, potatoes, chillies, ginger, etc. Marine products are also being produced in large quantities due to large coastal areas. The present production level of fruits and vegetables is more than 100 million MT and keeping in view the growth rate of population and demand, the production of perishable commodities is increasing every year. The cold storage facilities are the prime infrastructural component for such perishable commodities. Besides the role of stabilizing market prices and evenly distributing both on demand basis and time basis, the cold storage industry renders other advantages and benefits to both the farmers and the consumers. The farmers get opportunity of producing cash crops to get remunerative prices. The consumers get the supply of perishable commodities with lower fluctuation of prices. Commercially apples, potatoes, oranges are stored on large scale in the cold storages. Other important costly raw materials like dry fruits, chemicals, essences and processed foods like fruit juice/pulp, concentrate dairy products, frozen meat, fish and eggs are being stored in cold storages to regulate marketing channels of these products. Energy consumption of an experimental cold storage was measured for different storage temperatures. Suction temperature and pressure temperature of the compressor and working time of the compressor were determined to reach evaporator set up temperatures. Capacity of compressor, condenser, and evaporator were 10460 kJ/h, 12552 kJ/h , and 10460 kJ/h, respectively. An axial fan located back of the evaporator was used to distribute the cooled air into the cold store. An electrical heater was used to defrost. Refrigerant was R22. Energy use in a cold storage facility is affected by the amount of heat the refrigeration equipment must remove and the efficiency of the equipment. The main sources of heat in a facility for long-term storage are transmission through walls, evaporator coil fans, lights, air leakage, and respiration of the stored commodity. The electric energy consumption of existing cold stores ranges between 30 and 50kWh/m3/year for storage. It is depends on the quality of the building, on the activities (chilled or frozen storage), room size, stock turnover, temperature of the incoming produce, outside temperatures, etc. The total cost of electric energy is about 10 to 15% of the total running costs of a store. Improving Energy Efficiency (EE) has two goals: cost reduction and environmental protection. Objective of this research is to determine energy consumption of a cold storage for different storage temperatures. Energy consumption of the system elements such as compressor, condenser and fan of the evaporator were measured and evaluated. In RESEARCH ARTICLE OPEN ACCESS
  • 2. Dr. N. Mukhopadhyay Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 4, ( Part -7) April 2015, pp.06-10 www.ijera.com 7 | P a g e addition, suction and pressure temperatures of the compressor, condenser output temperature and required time to reach to the each set up temperature were determined and evaluated. Energy auditing is one tool through which balancing of demand and supply is determined and the positive mismatch cannot be compensated either by organic way or it might be difficult task. This paper deals with different aspects of design of cold storage and includes all standard refrigeration principles and heat load factors which are normally considered in a cold storage design and various energy audits. II. MODEL ANALYSIS (a) Technical analysis – I visit a cold storage at West Bengal , INDIA and collect the data which is given below :- T1 = 2.5 0 C , T2 = 30 0 C T3 = 4.5 0 C , T4 = 1 0 C P1 = 3.5 kg/cm 2 , P2 = 10.5 kg/cm 2 Calculation for Actual energy : - At first I take the data of actual energy by a compressor (KC 2) for one chamber from reading, this is equal to = 55 KW per hour. Now also I got this actual energy by the electricity bill for that cold storage -- Month Electricity bill July , 2014 73,890 KWH August , 2014 86,135 KWH September , 2014 60,295 KWH So, the average of this three months electricity bill is = 73890 + 86135 + 60295 3 = 220320 3 = 𝟕𝟑𝟒𝟒𝟎 KWH This unit is for one month and for 2 chambers only. The running time for a month is 540 Hours. Now, Total unit consumption for one hour and for one chamber = 73440 540 × 2 = 𝟔𝟖 𝑲𝑾 𝒑𝒆𝒓 𝒉𝒐𝒖𝒓 [ One compressor is running for one chamber ] Now , there is also a pump, 336 pieces of fan & 800 lights are running .
  • 3. Dr. N. Mukhopadhyay Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 4, ( Part -7) April 2015, pp.06-10 www.ijera.com 8 | P a g e Unit consumed by the pump = 11.19 KW Unit consumed by the fan = 0.06 KW Unit consumed by the light = 0.018 KW So, the total unit consumed by this three = [ 11.19 + 0.06 + 0.018 ] KW = 11.27 KW So, unit consumed by a compressor is = [ 68 - 11.27 ] KW = 56.73 KW This value is approximately similar to the actual energy by a compressor from reading. So, I take 55 KW/h So, Calculation for Theoretical energy : - I have done this theoretical energy calculation with three process :- (i) The power of compressor = V . I . CosØ Here , V = 415 volt I = 125 Amp. CosØ = 0.8 So, Etheoritical = V . I . CosØ = 415 X 125 X 0.85 = 44093.75 Watt Etheoritical = 44.09 KW per hour (ii) Also we know, Etheoritical = work done by a compressor Etheoritical = 𝒏 𝒏−𝟏 𝐩 𝟏 𝐯 𝟏 { 𝒑 𝟐 𝒑 𝟏 𝒏−𝟏 𝒏 − 𝟏} Where, n = 1.4 p 1 = 3.5 kg/cm2 = 35000 kg/m2 = 35000/101. 972 KPa = 343.23 KPa v 1 = 𝜋 4 𝐷2 𝐿 where D = Bore = 160 mm L = Stroke = 110 mm = 𝜋 4 0.16 2 × 0.11 = 0.00221 m3 p 2 = 10.5 kg/cm2 = 105000 kg/m2 = 105000/101.972 KPa = 1029.69 KPa Etheoritical = 1.4 1.4−1 343.23 x 0.00221 x { 10.5 3.5 1.4−1 1.4 − 1} = 2.665 x [ 1.375 - 1] Etheoritical = 0.996 Joule Here the speed of motor for compressor is = 1440 rpm and number of cylinder is = 2, then Etheoritical = 0.996 × 2 ×1440 60 Etheoritical = 47.8 KW per hour (iii) Now, Heat grade energy output ( KWH) Co-efficient of performance (COP) = ------------------- ----------------------------------- Electrical/Mechanical energy input (KWH) COP = 𝑸 𝑾 Also, COP = 𝒅𝒕 𝟏 𝒅𝒕 𝟏−𝒅𝒕 𝟐 Where, dt1 = Condensing temperature difference dt2 = Evaporating temperature difference So, 𝑸 𝑾 = 𝒅𝒕 𝟏 𝒅𝒕 𝟏−𝒅𝒕 𝟐 𝑾 = 𝑸(𝒅𝒕 𝟏 − 𝒅𝒕 𝟐) 𝒅𝒕 𝟏
  • 4. Dr. N. Mukhopadhyay Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 4, ( Part -7) April 2015, pp.06-10 www.ijera.com 9 | P a g e Here Q = 55 KW per hour. [ It is calculated from a journal paper] Then, 𝑾 = 𝟓𝟓 𝑻 𝟐−𝑻 𝟑 − 𝑻 𝟏−𝑻 𝟒 𝑻 𝟐−𝑻 𝟑 𝑾 = 𝟓𝟓 𝟑𝟎𝟑 − 𝟐𝟕𝟕. 𝟓 – 𝟐𝟕𝟓. 𝟓 − 𝟐𝟕𝟒 𝟑𝟎𝟑 − 𝟐𝟕𝟕. 𝟓 𝑾 = 𝟓𝟓 𝟐𝟓. 𝟓 − 𝟏. 𝟓 𝟐𝟓. 𝟓 𝑾 = 𝟓𝟏. 𝟕𝟔 𝑲𝑾 𝒑𝒆𝒓 𝒉𝒐𝒖𝒓 Etheoritical = 51.76 KW per hour Now , the average of this three Etheoritical = 44.09 + 47.8 + 51.76 3 = 47.88 KW per hour So, when I take mechanical/electrical energy loss of the compressor then this energy is equal to (b) Energy Gap Analysis – There is a huge gap when I calculating the energy difference. Gap energy = Eactual - Etheoritical = 55 − 50 KW per hour = 5 KW per hour If I take per month then it becomes :- Gap energy = 5 × 540 KW per hour = 2700 KW per hour If I take per year it becomes :- Gap energy = 2700 × 12 KW per hour = 32400 KW per hour (c) Cost Analysis – This data is collected from total electricity bill of that cold storage – Month Unit Cost July 2014 73890 KWH Rs. 5,38,972 /- August 2014 86135 KWH Rs. 5,42,071 /- September 2014 60295 KWH Rs. 4,66,395 /- So, the average cost of one month = 538972 + 542071 +466395 3 = Rs. 5,15,813 /- Now the excess energy for a month is equal to 2700 KWH and for a year is equal to 32400 KWH. So the saving money is = 2700 x 7.5 = Rs. 20,250 /- in a month. = 32400 x 7.5 = Rs. 2,43,000 /- in a year. III. RESULT & DISCUSSION At first I make a programming for the equation Etheoritical = 𝒏 𝒏−𝟏 × 𝟐 × 𝟐𝟒 × 𝐩 𝟏 𝐯 𝟏 { 𝒑 𝟐 𝒑 𝟏 𝒏−𝟏 𝒏 − 𝟏} in KW Where n = 1.4 The program is - #include<iostream.h> #include<conio.h> #include<math.h> int main( ) { double p1 , p2 , v1 = 0.00221, e , x ; cout<< “give the value of p1 , p2 / n”; cin>> p1 >> p2 x = pow (p2 / p1 , 0.29); e = 3.5 * 2 * 24 *(p1 * v1 * x – p1 * v1); cout << e ; return 0 ; } This programming is done for the twenty values of p1 , p2 and E which is used for making the graph plotting – (i) p1 vs E and (ii) p2 vs E (iii) T1 vs E Where p1 = suction pressure, p2 = discharge pressure, E = energy and T1 = suction tempera ture. (i) Graph of compressor suction pressure vs compressor energy :- The graph indicates that energy increases with increase in suction pressure (ii) Graph of compressor discharge pressure vs compressor energy :- Etheoritical = 50 KW per hour.
  • 5. Dr. N. Mukhopadhyay Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 4, ( Part -7) April 2015, pp.06-10 www.ijera.com 10 | P a g e The graph indicates that energy increases with increase in discharge pressure (iii) Graph of compressor suction temperature vs compressor energy :- The graph indicates that energy increases with increase in discharge pressure IV. CONCLUSION It has been observed that the actual energy consumption of a cold storage by a compressor for one chamber is 55 KW per hour and theoretical energy consumption is 50 KW per hour. So, a gap of 5 KW per hour is found between the theoretical and actual energy consumption by a compressor. If this gap is fulfilled then a savings of Rs 20,250 /- per month will be obtained which will amount to Rs 2,43,000 /- per year. To save energy the following practices must be implemented:- 1. Reducing Heat Loads 2. Uses of latest energy saving equipments 3. Proper Insulation 4. Efficient maintenance practices 5. Automation & Integration There are other factor which contributes to the total energy consumption, which are (i) lights (total 800 pcs) , (ii) fans (total 336 pcs). To increase the efficiency, conventional lights will replaced by energy efficient devices that is LED, CFL etc. If we replace three compressors for three chambers with a single equivalent compressor which will deliver the same amount of load, then maximum energy will be saved. REFERANCES [1] www.google.com [2] http://en.wikipedia.org [3] Engineering Thermodynamics, P. K. Nag (Book) [4] Willis croft PMP, NZ Rural Press Limited, Auckland, 2007 [5] ISHRAE Publications, Air conditioning and Refrigeration