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“ Energy Conservation by
Application of Heat Pump in
Process Line at Automobile
industry Ltd. ”
By
Mr. Shivraj N Nalawade
M . Tech- II (Energy Technology)
Under Guidance of
Prof. N. N. Shinde
Mr. S. A. Doshi
• Many industries use heating applications in their processes. These applications
could be by means of different energy inputs like electrical heating, thermal
heating, steam heating or few renewable heating. Out of these many
managements are unaware about significant energy source for their
applications. The heat energy gadgets adds heat in atmosphere
• Some organization are not much aware about energy efficient techniques
available in the market and this tends to high running and operating cost
resulting in losses.
• During the energy conservation studies at Process Industry is observed that the
highest consuming load centre is machining line. On HA crank case line
maximum energy consumption is because of electrical heaters which are used
for water heating purpose.
• The heat pumps are used now a days to recover heat and can be used as energy
gadgets as it helps maintains the cooling of working space. Comfort is very
important for increasing productivity.
• Hence the topic is selected as “Energy Conservation by Application of Heat
Pump in Crankcase Process Line at Automobile industry Ltd. ”
Relevance of the Project
Certificates
Heat pumps
 Heat pump technology
1. Air Source
2. Ground Source
3. Water Source
 Heat Pump cycle
 Components of Heat Pump
1. Compressor
2. Condenser
3. Expansion Valve
4. Evaporator
5. Refrigerant
 Heat Pump Benefits
1. Heat Pump used for Heating
2. Heat Pump used for Cooling i.e. Air Conditioning
3. Heat Pumps control the climate
4. Heat Pumps are convenient
5. Heat Pumps are safe
6. Heat Pumps are very energy efficient
• Applications of Heat Pump
i. Industrial washing machines
ii. Commercial building
iii. Restaurants
iv. Hotels
v. Health club
vi. Schools
vii. Hospitals
• IEQ (indoor environmental quality)
The quality of the air and environment inside industries that contribute to
a healthy and comfortable place to live and work. Indoor environmental
quality is affected by electrical equipment’s that release heat in to the
building. Heat pump is the major part when we consider IEQ for any
industry.
 Energy Conservation and Heat Pumps
Water Heater Type
Storage
Tank
Site-to-Source
Ratio
Energy
Factor
Source COP
Electric Resistance Tank 3.365 0.90 0.27
Heat Pump Tank 3.365 2.00 0.59
Fuel Oil Tank 1.158 0.59 0.51
Natural Gas Tank 1.092 0.59 0.54
Natural Gas Tank less 1.092 0.82 0.75
Condensing Natural Gas tank less 1.092 0.94 0.86
Propane Tank 1.151 0.59 0.51
(source: Energy Efficiency and Renewable Energy U.S. Department of Energy)
Problem Definition
 Industry case under consideration
1. In many developing countries HPWH system in widely used for water
heating application rather than that of conventional water heating
systems.
2. These applications could be by means of different energy inputs like
electrical heating, thermal heating, steam heating or few on renewable
heating.
3. In Automobile industrial sector for washing of various components
hot water is used in large amount. This requirement of hot water can
be generally fulfilled by electrical heaters. But, electrical heaters can
consumes lots of electrical energy in comparison with that of heat
pump.in developing country like India many industries are using
electrical heaters for hot water application.
4. Presently in industry, the water is heated by electrical energy
(electrical Heater). This electrical heater has consumed lot of
electrical power. Considering all condition, to study such
systems and check the feasibility for the alternate innovative
energy source for such applications.
 Overview of Existing System 1. Washing
chamber
2. Drum filter
3. Dirty tank
4. Transfer Pump
5. Compact band
filter
6. Clean tank
7. Spray pump
 Condition of Water Heating
Objectives
1. Study of final components of washing machine on crank
case machining line at automobile industry.
2. Feasibility of energy saving at component washing
machine and application of heat pump.
3. Designing of suitable heat pump considering requirement
of water heating for washing application.
4. Data collection and analysis of suitable heat pump with
respect to IEQ in the vicinity of final washing machine on
crank case line.
5. Conclusion and recommendations.
Literature Review
 This chapter covers about various literatures which contain lots of various
technologies for heat pump also it covers most important parameters like IEQ,
HPWH as well as various properties of various refrigerants.
 The various papers of national and international authors which are working
on this heat pump technology and also indoor environmental quality factor in
industry.
 While studding heat pump and refrigeration systems there are standards from
which the system is to be designed and these standards are ANSI/AHRI, some
ISO standards and also ASHRAE standards. After studying electrical hearers
and heat pump systems hardly any reference is found for study.
 Energy conservation is achieved by the heat pump. Many citation’s exists for
application of heat pump specifically in refrigeration system to recover the
waste energy in a closed loop.in this case the problem considered in chapter 2
is specifically phenomenon of replacing electrical energy by heat pump in
which the cooling load is created which can be used for cooling the air nearer
to level of the comfort which is new concept for help to maintain and IEQ in
the environment nearby. This project therefore is concentrated in designing
the heat pump for the crankcase process line at Kirloskar oil engine ltd. and to
find out energy conservation potential which will lead to reducing energy
consumption by improving system energy efficiency in general. This will
provide guidelines for the future work for maintain environment in the
industry.
Scope of the Project
1. Studied energy consumption pattern in different shops at
industry.
2. Prepare pie charts for energy balance.
3. From pie charts, machine shop is major consuming load center.
4. In depth, analyze machine shop consumption for different lines
and machine on the lines. It is observed that component washing
machine is highest energy consuming machine.
5. Studied the same for the feasibility alternative sources.
Methodology
1. Measuring energy consumption at various load centers.
2. Feasibility of energy saving at component washing machine
and application of heat pump.
3. Study of final components for wash on washing machine on
crank case machining line
4. Data Collection and analysis by Fluke analyzer (Heating
Load Measurements) on washing machine.
5. Study of vapor compression refrigerant system.
6. Designing of Suitable Heat Pump Considering Requirement
of Water Heating For Washing Application.
1. Measuring energy consumption at various load centers.
 Variable Energy Consumption at industry (In Kwh)
Centre Unit 10-11 11-12 12-13 13-14
Machine Shop Mn Units 8.01 6.76 8.49 6.51
Medium
Engine
Mn Units 2.56 2.15 2.21 2.04
GENSET Mn Units 1.15 0.99 1.50 1.00
Small Engine Mn Units 1.60 1.38 1.18 1.63
Total Mn Units 13.32 11.28 13.38 11.18
58%18%
9%
15%
Variable Energy Balance
Machine Shop
Medium Engine
GENSET
Small Engine
2. Feasibility of energy saving at component washing
machine and application of heat pump.
3.74
1.76
1.64 1.62 1.57
1.45 1.4 1.31 1.27 1.19 1.19 1.15 1.15 1.14 1.1 1.07 0.99 0.98 0.92
0.91
0
20
40
60
80
100
120
0
0.5
1
1.5
2
2.5
3
3.5
4
%contribution
energyconsumption(kw)
machine name
parato chart per component energy consumption on ha crank case line
3. Study of final components for wash on washing
machine on crank case machining line.
component
Weight(
kg)
Dimension(mm)
Compone
nts Per
Shift
Temperature(0C)
Mean
Temperature
Difference
Heat loss in
component(
kWh)
Height Width
Before
washing
(t1)
After
washing
(t2)
2 Cylinder
Head
64 335.8 587 63 26.3 36.4 10.1 0.09
3 Cylinder
Head
81 335.8 457 60 26 36.1 10.1 0.12
4 Cylinder
Head
98 335.8 309 58 25.5 35.4 10 0.15
Picture before Component Washing Picture after Component Washed
 List of measuring instruments
Fluke Power Analyzer Thermal Imager Mass Flow Meter
Actual measurement on
site
 Actual pictures of machine
Washing chamber Drum filter
Electrical Heater position Crank case Component
 Data Collection and analysis by analyzer (Heating Load
Measurements) on washing machine.
Measurement – Initial stage heating (From 27°C to 55°C)
Total Energy Consumption-46 kWh
Measurement – Shift 1
Time of Shift- 8 hrs. (Initially Power analyzer is set to 0 Reading)
Total Energy Consumption for shift 1-288.6 kWh
Measurement – Shift 2
Time of Shift- 8 hrs. (Initially Power analyzer is set to 0 Reading)
Total Energy Consumption for shift 2-293 kWh
Total Energy Consumption of Heaters in 1 Day=46+288.6+293=627.6kWh
Time(Hrs.) Consumption (kWh)
1 46
Time 1 hr. 2 hr. 3 hr. 4 hr. 5 hr. 6 hr. 7 hr. 8 hr.
Consumption(kWh) 36 38 37 37.5 35.3 34.5 36.3 34
Time 1 hr. 2 hr. 3 hr. 4 hr. 5 hr. 6 hr. 7 hr. 8 hr.
Consumption(kWh) 34.9 36.8 36.3 38 35.6 38 36.4 37
0
5
10
15
20
25
30
35
40
45
50
0 2 4 6 8 10 12 14 16 18
Consumption(kWh)
Time(Hrs)
Energy Consumption of Electrical Heater
Proposed system
Block diagram of washing machine Block diagram of washing machine compatible
with heat pump
Heat capacity
Initial Condition
water flow = 1450 Litres
mh = 1450 kg
mh = 1450 kg/3600 = 0.402 kg/s
Cold fluid inlet Temperature = TCin = 270
C
Hot fluid inlet Temperature = TCot = 550
C
From steam tables,
Enthalpy of water at 270
C = hf27 = 118.8 kJ/kg
Enthalpy of water at 550
C = hf55 = 231.6 kJ/kg
∴ ∆h = hf55 −hf27
∴ ∆h = 112.8 kJ/kg
Hence, heat required to be added,
H = mh∆h
= 1450 × 112.8
= 163560 kJ
Time required to heat= 1Hr=3600 sec
Heat capacity of heater =
Heat added
time
=
90240
3600
= 45.33 kW
In Tons of refrigeration,
=
45.33
3.5167
= 12.88TR
Design of Heat Pump
Running condition
water flow = 210 Liters/min
mh = 210 kg/min
mh = 210 kg/60 = 3.5 kg/s
Inlet Temperature of water = TCin = 450
C
Outlet Temperature of water = TCot = 550C
From steam tables,
Enthalpy of water at 450C = hf27 = 217.29 kJ/kg
Enthalpy of water at 550
C = hf55 = 231.6 kJ/kg
∴ ∆h = hf55 −hf27
∴ ∆h = 12.95 kJ/kg
Hence, heat required,
H = mh∆h
= 3.5 × 12.95
= 45.33kW
In Tons of refrigeration,
=
45.33
3.5167
= 12.88TR
By considering both the above initial and running condition, capacity output of heat
pump required is about 45.33 kW or 12.88 TR. All the technical parameters are
designed on the basis of 45.33 kW output of Heat Pump.
Selection of Suitable refrigerant
Criteria Refrigerants
1= Poor 5= Excellent R-22 R-290 R-410A R-404A R-407c R-134a
Cooling capacity 3 2 5 3 2 1
Input power 3 4 1 2 3 5
Cooling COP 4 5 3 3 2 5
Refrigerant mass flow 4 1 5 5 3 2
Discharge temperature 3 5 3 5 3 5
Pressure ratio 5 5 5 5 1 2
Vol. ref. capacity. 4 3 5 4 3 1
ODP 1 5 5 5 5 5
GWP 2 5 2 1 2 3
Cost 3 5 1 2 1 2
Non-toxicity 5 5 5 5 5 5
Non-flammability 5 1 5 5 5 5
Compatibility 5 5 5 5 5 5
Total 47 51 50 50 40 46
As seen in above table the rating of R-134a having total of 46 which was middle among all
refrigerant used conventionally, selection of refrigerant as R-134a for project work.
PH Chart for R134a at 12.8°C Evaporating and 60°C Condensing
(source: PH chart is plotted using COOLPACK software)
2. Heat pump operating temperature and pressure
Assuming ADP (Apparatus Dew Point Temperature) of cooling coil of evaporator = 40
C
Properties of R134a at 40
C
P = 3.3755 bars
Minimum of 50C temperature difference is necessary to heat the fluid, in order to
avoid the limitation of heat transfer by finite temperature difference
∴ Condensor temperature = 55 + 5 = 600C
for R134a
@600
C , P = 16.815 bar
Point Temperature(°C) Pressure(Bar) Enthalpy(Kj/Kg)
1 23.89 4.54 415.33
2 79.06 16.81 451.10
3 79.06 16.81 451.10
4 57.23 16.81 282.88
5 N/A 4.54 282.88
6 23.9 4.54 415.33
15 N/A 16.81 282.88
3. Refrigerant mass flow rate
Now at 600
C, total heat content of refrigerant,
∆hr=enthalpy of gas @600C-enthalpy of liquid @600C
∴from properties of R134a
= 451.1 − 282.88 kJ/kg
∆hr = 165.22 kJ/kg
By 1st law of thermodynamics,
Heat added to cold water = heat rejected from condersor
∴ 45.33 = mr∆hr
∴ mr = 0.27 kg/sec
Final compressor specifications
Theoretical COP of the system 3.7
Actual COP of the system 3.6
Refrigerant mass flow rate 0.27 Kg/sec
Compressor work 9.65 kW
EPR 7.05
Isentropic efficiency of compressor 66%
4. Compressor Specifications
Condenser Design Using Trial And Error Method
Heat Flow diagram
Condenser Specifications
Condenser heat output 45.33 Kw
Tube ID 0.017 M
Tube OD 0.025 M
No. of tubes 44
No. of passes 2
No. of baffles 8
Baffle spacing 0.122 M
Tube length 1 M
Bundle diameter 0.23 M
Shell diameter 0.3 M
Tube side pressure drop 0.61 Bar
Shell side pressure drop 0.3 Bar
• Condenser Drawing
6. Expansion valve selection
The most important technical parameter for selection of thermostatic expansion valve is
MOP (Maximum Operating Pressure)
Evaporator pressures are limited to a maximum value to protect compressor from
overload conditions. MOP selection should be within maximum allowed low pressure
rating of the compressor and should be at approximately 3 K above maximum
evaporating temperature.
MOP Upper limit of evaporating temperature
Bar °C R407C R22 R 410a R134a
6.9 17 14
6.9 15 12
3.8 14 10
12.1 16 14
Note-All pressures are gauge pressure
Expansion valve specifications
Condensing Pressure 16.8 Bar
Evaporating Pressure 12.8 Bar
Total Pressure Loss 1.5 Bar
Effective pressure difference across valve 10.77 Bar
Correction factor for pressure differential 0.78
Correction factor for evaporating temperature 1.35
Evaporator specifications
Heat absorbed in evaporator 35.76 Kw
Tube diameter 0.01 M
Fin pitch 0.034 M
Fin thickness 0.048 Cm
Air mass flow rate 7.31 kg/sec
No. of tubes 28
Fine width 0.043 M
 Evaporator design
 Final Temperature and pressure on heat pump cycle
Heat Pump Compatible With Tank
Heat Pump Drawing
Proposed System Replacements
Energy, Cost saving and Environmental
Analysis
 Energy saving potential
0
5
10
15
20
25
30
35
40
45
50
0 2 4 6 8 10 12 14 16
Consumption(kWh)
Time(Hrs.)
Comparision of Electric Heater and Heat Pump Energy
Consumption in 1 day
Electric Heater
Heat Pump
• Estimated Energy and Cost saving Analysis
•Estimated Energy consumption Calculation for Electrical Heaters and
Heat Pump
Total Energy Consumption of Heaters in 1 Day =627.6 kWh (Actual
Measurements)
Total Energy consumption by heat pump=12.54kw
Therefore, total energy consumption by heat pump in 1 day= 200.64kWh (for
16hrs. of operation)
Energy Savings /Day = Consumption of Heaters in 1 Day- consumption by
heat pump in 1 day
Energy Savings /Day =627.4-200.64=426.76 kWh/day
Energy saving per year= 426.76*300=1,28,028 kWh/Year
It means that heat pump can be save up to 61,680 units of electricity per year.
•Estimated Cost saving analysis
Base rate of electricity for 1 unit= 8 Rs.
Therefore,
Cost saving per day=8*426.76=3414.08 Rs.
Cost saving per Year=3414.08*300=10,24,224 Rs.
•Payback period Calculation
Market prize of heat pump from manufacturing company is nearly= Rs. 9,
50,000/- (With installation)
Therefore, Payback period of heat pump = 1 Year
Indoor Environmental Quality (IEQ)
improvement
There are 2 main contains in IEQ as per ASHRAE 2009 handbook are
as follows:
•Thermal Comfort Indoor Environmental Health
•Air Contaminants
For consideration of IEQ the below readings are taken on site.
Limits are taken as per factory act 1948.
Sr. no Parameters Values Limit as per factory act, 1948
1. Ambient temp 0C
Dry bulb 28 290C to 340C
Wet bulb 24 220C to 260C
2. Relative humidity% 64 ---
3. Noise level in dB(a) 87.9 90
4. Suspended particular matter, mg/m3 0.09 <=10
5. Oil mist mg/m3 0.019 <=5
• Estimated room dimensions for cooling
• This chapter includes energy saving potential of electrical
heater as well as Heat Pump.
• Which clearly shows energy saving potential of
• heat pump is very high.
• This also includes cost beneficial analysis and impact of
heat pump output on IEQ at working condition.
Summary
1. On the existing system, study is done on electrical water heating system for
crankcase machine line which shows that it has an average electrical energy
consumption of 627.6 kWh,15,690 kWh and 1,88,280 kWh for daily, monthly
and yearly respectively.
2. The design data is created for the existing process layout.
3. A heat pump system has been designed and electrical consumption has been
worked out.
4. The theoretical analysis clearly indicates that the energy conservation has been
achieved 426.76 kWh, 10669kWh, 128028 kWh on daily, monthly and yearly
basis respectively.
5. This energy consumption is in accordance with the prevailing designed data
and the surrounding climatology for automobile industry.
6. The cost saving is achieved Rs 3,414.08 , Rs 85,382, Rs 10,24,224 on daily,
monthly and yearly basis respectively.
7. The actual amount of heat pump by market price is nearly Rs 9,50,000 and
savings achieved by theoretical calculations is Rs 10,24,224 yearly at base price
of electricity Rs 8 per unit. So the calculated payback period is nearly one year.
Conclusion
In view of conclusion heat pump is recommended for energy conservation for such
applications in industry. Its value addition like cooling the surrounding is also of prime
importance in the view of IEQ.
Due to limitations of cost of heat pump and time of period of completion,
prototype of heat pump development is remained
Future scope
• Development of heat pump model.
• Analysis of heat pump performance by various refrigerants.
• Testing results and analysis performance of heat pump with impact on IEQ
Recommendations
1. At the crank case line washing machine there are various
other options to replacer that electrical heaters with solar
water heater, heat pump, biogas and briquette fire
technology and also other renewable energy sources for
washing application.
2. After installing any other system for water heating do
regularly maintenance and check whether the system works
correctly and energy efficiently.
3. Use clean water for washing application and also regularly
add makeup water in tank.
References
1. Xing Xu, Yunho Hwang*, Reinhard Radermacher,” Refrigerant injection for heat
pumping/air conditioning systems: Literature review and challenges discussions” Center
for Environmental Energy Engineering, University of Maryland College Park, 3163
Glenn Martin Hall Bldg., MD 20742, USA.
2. MG Apte1*, D Dibartolomeo1, T Hotchi1, AT Hodgson1, SM Lee1; SM Liff2, LI
Rainer3, DG Shendell1, DP Sullivan1, and WJ Fisk1, “ Simultaneous Energy Savings
and IEQ Improvements in Relocatable Classrooms” Indoor Environment Dept.,
Lawrence Berkeley National Laboratory, Berkeley, CA, USA Massachusetts Institute of
Technology, Boston, MA Davis Energy Group, Davis, CA.
3. Mauro A. S. S. Ravagnani1, Aline P. Silva1 and Jose A. Caballero2,” Optimal Shell and
Tube Heat Exchangers Design”, 1State University of Maringá2University of Alicante
1Brazil 2Spain. Guoping Liu*,1, Genfu Xiao1,2, Junting Wang1, Wei Luo1 and Honggun
Song1”The Optimal Design of the Scroll Profiles Based on Chaos PSO”, the Open
Mechanical Engineering Journal, 2011, 5, 194-198
4. Paul BYRNE*, Redouane GHOUBALI, Jacques MIRIEL,” Scroll compressor modeling
for heat pumps using hydrocarbons as refrigerants”" international Journal of
Refrigeration 41 (2013) 1-13.
5. Winandy, Eric and Hundy, Guy, "Refrigerant and Scroll Compressor Options for Best
Performance of Various European Heat Pump Configurations" (2008). International
Refrigeration and Air Conditioning Conference. paper 895
6. Zogg M. 2008. “History of Heat Pumps - Swiss Contributions and International
Milestones”, final report, Swiss Federal Office of Energy, Berne; with 285 references,
downloadable from www.zogg-engineering.ch/publi/HistoryHP.pdf
7. Tina Fawcett,” The future role of heat pumps in the domestic sector”, Environmental
Change Institute University of Oxford South Parks Road Oxford OX1 3QY UK.
8. Tina Fawcett,” The future role of heat pumps in the domestic sector”, Environmental
Change Institute University of Oxford South Parks Road Oxford OX1 3QY UK.
9. John Dieckmann, P.E., Member ASHRAE; Bob Zogg, P.E., Member ASHRAE;
DetlefWestphalen, Ph.D., Member ASHRAE; Kurt Roth, Ph.D., Associate Member
ASHRAE; and James Brodrick, Ph.D., Member,” Heat-Only, Heat-Activated Heat
Pumps” ASHRAE Journal, January 2005. © Copyright 2005 American Society of
Heating, Refrigerating andAir-Conditioning Engineers, Inc.
10. Bernardi WP, Blevins RP, Sloane BD. Examination and life assessment of fieldtested
heat pump water heaters. Prepared by Energy Utilization Systems, Incorporated for Oak
Ridge National Laboratory operated by Union Carbide Corporation for the U.S.
Department of Energy, December 1982.
11. Sauer HJ, Howell RH. Heat pump systems. USA: John Wiley & Sons, Inc.; 1983
12. Kokkinides L, Sachs HM. Toward market transformation: commercial heat pump water
heaters for the „„New York energy $marts Region‟‟. Final Report. Prepared for The New
York State energy research and development authority and prepared by American council
for an energy efficient economy, NYSERDA, October 2002.
13. ArifHepbasli a, YildizKalinci b,”A review of heat pump water heating systems”,a
Department of Mechanical Engineering, Faculty of Engineering, Ege University, 35100
Izmir, Turkey .b Plumbing Technology, Department of Technical Programs, Izmir
Vocational School, DokuzEylul University, Education Campus Buca, Izmir, Turkey.
14. Tomasz Sobota (2011). Experimental Prediction of Heat Transfer Correlations in Heat
Exchangers, Developments in Heat Transfer, Dr. Marco Aurelio Dos Santos Bernardes
(Ed.), ISBN: 978-953-307-569-3,InTech, Available from:
http://www.intechopen.com/books/developments-in-heat-transfer/experimentalprediction-
of-heat-transfer-correlations-in-heat-exchangers.
15. Kumar, Ph.D., Member ASHRAE, and William J. Fisk, P.E., Member ASHRAE,” IEQ and
the Impact On Building Occupants”ASHRAE Journal, April, 2002.
16. Ban-Huat Ng1, ZainalAbidin Akasah2,” Energy-Efficient Buildings: An In-Depth
Look into Definitions, and Design Problems”Int. J. Emerg. Sci., 3(4), 345-358,
December 2013 ISSN: 2222-4254.
17. Nalawade Shivraj N,”Training report on energy assessment and conservation in
Kirloskar oil engine .ltd. Kagal” (2014). Energy Technology, Department of
Technology, Shivaji University, Kolhapur.
18. Handbook on “Heat Exchangers selection, Rating and Thermal Design (Second
Edition),”by Sadik Kakac1, Hongtan liu2.
19. Handbook on ”Process Heat Transfer”, by Donald Q. Kern.
20. Handbook on” Compact Heat exchangers.” By Kays W. M. and London, A.L.[1984].
21. Handbook on “ASHRAE standard for IEQ and Energy Standard for Buildings except
Low-Rise Residential Buildings”.
22. Data sheet of “Thermo-expansion valve” by Emerson Climate Technologies.
23. http://www.ahrinet.org/site/686/Standards/HVACR-Industry-Standards/Search-
Standards
24. http://www.nrcan.gc.ca/energy/publications/efficiency/eeproducts/roomaircond/6667
Paper Publications
 “ENERGY CONSERVATION ANALYSIS BY APPLICATION OF HEAT PUMP SYSTEM-
A CASE STUDY” paper is published in “INTERNATIONAL JOURNAL OF
ENGINEERING SCIENCES & RESEARCH TECHNOLOGY.(IJESRT)”
Shivraj Nalawade Thesis123_ENERGY CONSERVATION ANALYSIS BY
APPLICATION OF HEAT PUMP SYSTEM- A CASE STUDY.pdf
 “PERFORMANCE EVALUATION OF HEAT PUMP USING SIMULATION
TECHNIQUES FOR REPLACING ELECTRIC WATER HEATING SYSTEM TO
ACHIEVE ENERGY CONSERVATION AND IMPROVE IEQ IN AN PROCESS
INDUSTRY” paper is published in “INTERNATIONAL JOURNALOF CURRENT
RESEARCH”
Shivraj Nalawade ThesisPERFORMANCE EVALUATION OF HEAT PUMP USING
SIMULATION TECHNIQUES FOR.pdf
Thank You

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Energy Conservation in Automobile Industry Using Heat Pumps

  • 1. “ Energy Conservation by Application of Heat Pump in Process Line at Automobile industry Ltd. ” By Mr. Shivraj N Nalawade M . Tech- II (Energy Technology) Under Guidance of Prof. N. N. Shinde Mr. S. A. Doshi
  • 2. • Many industries use heating applications in their processes. These applications could be by means of different energy inputs like electrical heating, thermal heating, steam heating or few renewable heating. Out of these many managements are unaware about significant energy source for their applications. The heat energy gadgets adds heat in atmosphere • Some organization are not much aware about energy efficient techniques available in the market and this tends to high running and operating cost resulting in losses. • During the energy conservation studies at Process Industry is observed that the highest consuming load centre is machining line. On HA crank case line maximum energy consumption is because of electrical heaters which are used for water heating purpose. • The heat pumps are used now a days to recover heat and can be used as energy gadgets as it helps maintains the cooling of working space. Comfort is very important for increasing productivity. • Hence the topic is selected as “Energy Conservation by Application of Heat Pump in Crankcase Process Line at Automobile industry Ltd. ” Relevance of the Project
  • 4. Heat pumps  Heat pump technology 1. Air Source 2. Ground Source 3. Water Source  Heat Pump cycle
  • 5.  Components of Heat Pump 1. Compressor 2. Condenser 3. Expansion Valve 4. Evaporator 5. Refrigerant  Heat Pump Benefits 1. Heat Pump used for Heating 2. Heat Pump used for Cooling i.e. Air Conditioning 3. Heat Pumps control the climate 4. Heat Pumps are convenient 5. Heat Pumps are safe 6. Heat Pumps are very energy efficient
  • 6. • Applications of Heat Pump i. Industrial washing machines ii. Commercial building iii. Restaurants iv. Hotels v. Health club vi. Schools vii. Hospitals • IEQ (indoor environmental quality) The quality of the air and environment inside industries that contribute to a healthy and comfortable place to live and work. Indoor environmental quality is affected by electrical equipment’s that release heat in to the building. Heat pump is the major part when we consider IEQ for any industry.
  • 7.  Energy Conservation and Heat Pumps Water Heater Type Storage Tank Site-to-Source Ratio Energy Factor Source COP Electric Resistance Tank 3.365 0.90 0.27 Heat Pump Tank 3.365 2.00 0.59 Fuel Oil Tank 1.158 0.59 0.51 Natural Gas Tank 1.092 0.59 0.54 Natural Gas Tank less 1.092 0.82 0.75 Condensing Natural Gas tank less 1.092 0.94 0.86 Propane Tank 1.151 0.59 0.51 (source: Energy Efficiency and Renewable Energy U.S. Department of Energy)
  • 8. Problem Definition  Industry case under consideration 1. In many developing countries HPWH system in widely used for water heating application rather than that of conventional water heating systems. 2. These applications could be by means of different energy inputs like electrical heating, thermal heating, steam heating or few on renewable heating. 3. In Automobile industrial sector for washing of various components hot water is used in large amount. This requirement of hot water can be generally fulfilled by electrical heaters. But, electrical heaters can consumes lots of electrical energy in comparison with that of heat pump.in developing country like India many industries are using electrical heaters for hot water application. 4. Presently in industry, the water is heated by electrical energy (electrical Heater). This electrical heater has consumed lot of electrical power. Considering all condition, to study such systems and check the feasibility for the alternate innovative energy source for such applications.
  • 9.  Overview of Existing System 1. Washing chamber 2. Drum filter 3. Dirty tank 4. Transfer Pump 5. Compact band filter 6. Clean tank 7. Spray pump
  • 10.  Condition of Water Heating
  • 11. Objectives 1. Study of final components of washing machine on crank case machining line at automobile industry. 2. Feasibility of energy saving at component washing machine and application of heat pump. 3. Designing of suitable heat pump considering requirement of water heating for washing application. 4. Data collection and analysis of suitable heat pump with respect to IEQ in the vicinity of final washing machine on crank case line. 5. Conclusion and recommendations.
  • 12. Literature Review  This chapter covers about various literatures which contain lots of various technologies for heat pump also it covers most important parameters like IEQ, HPWH as well as various properties of various refrigerants.  The various papers of national and international authors which are working on this heat pump technology and also indoor environmental quality factor in industry.  While studding heat pump and refrigeration systems there are standards from which the system is to be designed and these standards are ANSI/AHRI, some ISO standards and also ASHRAE standards. After studying electrical hearers and heat pump systems hardly any reference is found for study.  Energy conservation is achieved by the heat pump. Many citation’s exists for application of heat pump specifically in refrigeration system to recover the waste energy in a closed loop.in this case the problem considered in chapter 2 is specifically phenomenon of replacing electrical energy by heat pump in which the cooling load is created which can be used for cooling the air nearer to level of the comfort which is new concept for help to maintain and IEQ in the environment nearby. This project therefore is concentrated in designing the heat pump for the crankcase process line at Kirloskar oil engine ltd. and to find out energy conservation potential which will lead to reducing energy consumption by improving system energy efficiency in general. This will provide guidelines for the future work for maintain environment in the industry.
  • 13. Scope of the Project 1. Studied energy consumption pattern in different shops at industry. 2. Prepare pie charts for energy balance. 3. From pie charts, machine shop is major consuming load center. 4. In depth, analyze machine shop consumption for different lines and machine on the lines. It is observed that component washing machine is highest energy consuming machine. 5. Studied the same for the feasibility alternative sources.
  • 14. Methodology 1. Measuring energy consumption at various load centers. 2. Feasibility of energy saving at component washing machine and application of heat pump. 3. Study of final components for wash on washing machine on crank case machining line 4. Data Collection and analysis by Fluke analyzer (Heating Load Measurements) on washing machine. 5. Study of vapor compression refrigerant system. 6. Designing of Suitable Heat Pump Considering Requirement of Water Heating For Washing Application.
  • 15. 1. Measuring energy consumption at various load centers.  Variable Energy Consumption at industry (In Kwh) Centre Unit 10-11 11-12 12-13 13-14 Machine Shop Mn Units 8.01 6.76 8.49 6.51 Medium Engine Mn Units 2.56 2.15 2.21 2.04 GENSET Mn Units 1.15 0.99 1.50 1.00 Small Engine Mn Units 1.60 1.38 1.18 1.63 Total Mn Units 13.32 11.28 13.38 11.18
  • 16. 58%18% 9% 15% Variable Energy Balance Machine Shop Medium Engine GENSET Small Engine
  • 17. 2. Feasibility of energy saving at component washing machine and application of heat pump. 3.74 1.76 1.64 1.62 1.57 1.45 1.4 1.31 1.27 1.19 1.19 1.15 1.15 1.14 1.1 1.07 0.99 0.98 0.92 0.91 0 20 40 60 80 100 120 0 0.5 1 1.5 2 2.5 3 3.5 4 %contribution energyconsumption(kw) machine name parato chart per component energy consumption on ha crank case line
  • 18. 3. Study of final components for wash on washing machine on crank case machining line. component Weight( kg) Dimension(mm) Compone nts Per Shift Temperature(0C) Mean Temperature Difference Heat loss in component( kWh) Height Width Before washing (t1) After washing (t2) 2 Cylinder Head 64 335.8 587 63 26.3 36.4 10.1 0.09 3 Cylinder Head 81 335.8 457 60 26 36.1 10.1 0.12 4 Cylinder Head 98 335.8 309 58 25.5 35.4 10 0.15 Picture before Component Washing Picture after Component Washed
  • 19.  List of measuring instruments Fluke Power Analyzer Thermal Imager Mass Flow Meter Actual measurement on site
  • 20.  Actual pictures of machine Washing chamber Drum filter Electrical Heater position Crank case Component
  • 21.  Data Collection and analysis by analyzer (Heating Load Measurements) on washing machine. Measurement – Initial stage heating (From 27°C to 55°C) Total Energy Consumption-46 kWh Measurement – Shift 1 Time of Shift- 8 hrs. (Initially Power analyzer is set to 0 Reading) Total Energy Consumption for shift 1-288.6 kWh Measurement – Shift 2 Time of Shift- 8 hrs. (Initially Power analyzer is set to 0 Reading) Total Energy Consumption for shift 2-293 kWh Total Energy Consumption of Heaters in 1 Day=46+288.6+293=627.6kWh Time(Hrs.) Consumption (kWh) 1 46 Time 1 hr. 2 hr. 3 hr. 4 hr. 5 hr. 6 hr. 7 hr. 8 hr. Consumption(kWh) 36 38 37 37.5 35.3 34.5 36.3 34 Time 1 hr. 2 hr. 3 hr. 4 hr. 5 hr. 6 hr. 7 hr. 8 hr. Consumption(kWh) 34.9 36.8 36.3 38 35.6 38 36.4 37
  • 22. 0 5 10 15 20 25 30 35 40 45 50 0 2 4 6 8 10 12 14 16 18 Consumption(kWh) Time(Hrs) Energy Consumption of Electrical Heater
  • 23. Proposed system Block diagram of washing machine Block diagram of washing machine compatible with heat pump
  • 24. Heat capacity Initial Condition water flow = 1450 Litres mh = 1450 kg mh = 1450 kg/3600 = 0.402 kg/s Cold fluid inlet Temperature = TCin = 270 C Hot fluid inlet Temperature = TCot = 550 C From steam tables, Enthalpy of water at 270 C = hf27 = 118.8 kJ/kg Enthalpy of water at 550 C = hf55 = 231.6 kJ/kg ∴ ∆h = hf55 −hf27 ∴ ∆h = 112.8 kJ/kg Hence, heat required to be added, H = mh∆h = 1450 × 112.8 = 163560 kJ Time required to heat= 1Hr=3600 sec Heat capacity of heater = Heat added time = 90240 3600 = 45.33 kW In Tons of refrigeration, = 45.33 3.5167 = 12.88TR Design of Heat Pump
  • 25. Running condition water flow = 210 Liters/min mh = 210 kg/min mh = 210 kg/60 = 3.5 kg/s Inlet Temperature of water = TCin = 450 C Outlet Temperature of water = TCot = 550C From steam tables, Enthalpy of water at 450C = hf27 = 217.29 kJ/kg Enthalpy of water at 550 C = hf55 = 231.6 kJ/kg ∴ ∆h = hf55 −hf27 ∴ ∆h = 12.95 kJ/kg Hence, heat required, H = mh∆h = 3.5 × 12.95 = 45.33kW In Tons of refrigeration, = 45.33 3.5167 = 12.88TR By considering both the above initial and running condition, capacity output of heat pump required is about 45.33 kW or 12.88 TR. All the technical parameters are designed on the basis of 45.33 kW output of Heat Pump.
  • 26. Selection of Suitable refrigerant Criteria Refrigerants 1= Poor 5= Excellent R-22 R-290 R-410A R-404A R-407c R-134a Cooling capacity 3 2 5 3 2 1 Input power 3 4 1 2 3 5 Cooling COP 4 5 3 3 2 5 Refrigerant mass flow 4 1 5 5 3 2 Discharge temperature 3 5 3 5 3 5 Pressure ratio 5 5 5 5 1 2 Vol. ref. capacity. 4 3 5 4 3 1 ODP 1 5 5 5 5 5 GWP 2 5 2 1 2 3 Cost 3 5 1 2 1 2 Non-toxicity 5 5 5 5 5 5 Non-flammability 5 1 5 5 5 5 Compatibility 5 5 5 5 5 5 Total 47 51 50 50 40 46 As seen in above table the rating of R-134a having total of 46 which was middle among all refrigerant used conventionally, selection of refrigerant as R-134a for project work.
  • 27. PH Chart for R134a at 12.8°C Evaporating and 60°C Condensing (source: PH chart is plotted using COOLPACK software)
  • 28. 2. Heat pump operating temperature and pressure Assuming ADP (Apparatus Dew Point Temperature) of cooling coil of evaporator = 40 C Properties of R134a at 40 C P = 3.3755 bars Minimum of 50C temperature difference is necessary to heat the fluid, in order to avoid the limitation of heat transfer by finite temperature difference ∴ Condensor temperature = 55 + 5 = 600C for R134a @600 C , P = 16.815 bar Point Temperature(°C) Pressure(Bar) Enthalpy(Kj/Kg) 1 23.89 4.54 415.33 2 79.06 16.81 451.10 3 79.06 16.81 451.10 4 57.23 16.81 282.88 5 N/A 4.54 282.88 6 23.9 4.54 415.33 15 N/A 16.81 282.88
  • 29. 3. Refrigerant mass flow rate Now at 600 C, total heat content of refrigerant, ∆hr=enthalpy of gas @600C-enthalpy of liquid @600C ∴from properties of R134a = 451.1 − 282.88 kJ/kg ∆hr = 165.22 kJ/kg By 1st law of thermodynamics, Heat added to cold water = heat rejected from condersor ∴ 45.33 = mr∆hr ∴ mr = 0.27 kg/sec Final compressor specifications Theoretical COP of the system 3.7 Actual COP of the system 3.6 Refrigerant mass flow rate 0.27 Kg/sec Compressor work 9.65 kW EPR 7.05 Isentropic efficiency of compressor 66% 4. Compressor Specifications
  • 30. Condenser Design Using Trial And Error Method Heat Flow diagram
  • 31. Condenser Specifications Condenser heat output 45.33 Kw Tube ID 0.017 M Tube OD 0.025 M No. of tubes 44 No. of passes 2 No. of baffles 8 Baffle spacing 0.122 M Tube length 1 M Bundle diameter 0.23 M Shell diameter 0.3 M Tube side pressure drop 0.61 Bar Shell side pressure drop 0.3 Bar
  • 33. 6. Expansion valve selection The most important technical parameter for selection of thermostatic expansion valve is MOP (Maximum Operating Pressure) Evaporator pressures are limited to a maximum value to protect compressor from overload conditions. MOP selection should be within maximum allowed low pressure rating of the compressor and should be at approximately 3 K above maximum evaporating temperature. MOP Upper limit of evaporating temperature Bar °C R407C R22 R 410a R134a 6.9 17 14 6.9 15 12 3.8 14 10 12.1 16 14 Note-All pressures are gauge pressure
  • 34. Expansion valve specifications Condensing Pressure 16.8 Bar Evaporating Pressure 12.8 Bar Total Pressure Loss 1.5 Bar Effective pressure difference across valve 10.77 Bar Correction factor for pressure differential 0.78 Correction factor for evaporating temperature 1.35 Evaporator specifications Heat absorbed in evaporator 35.76 Kw Tube diameter 0.01 M Fin pitch 0.034 M Fin thickness 0.048 Cm Air mass flow rate 7.31 kg/sec No. of tubes 28 Fine width 0.043 M  Evaporator design
  • 35.  Final Temperature and pressure on heat pump cycle
  • 36. Heat Pump Compatible With Tank
  • 39. Energy, Cost saving and Environmental Analysis  Energy saving potential 0 5 10 15 20 25 30 35 40 45 50 0 2 4 6 8 10 12 14 16 Consumption(kWh) Time(Hrs.) Comparision of Electric Heater and Heat Pump Energy Consumption in 1 day Electric Heater Heat Pump
  • 40. • Estimated Energy and Cost saving Analysis •Estimated Energy consumption Calculation for Electrical Heaters and Heat Pump Total Energy Consumption of Heaters in 1 Day =627.6 kWh (Actual Measurements) Total Energy consumption by heat pump=12.54kw Therefore, total energy consumption by heat pump in 1 day= 200.64kWh (for 16hrs. of operation) Energy Savings /Day = Consumption of Heaters in 1 Day- consumption by heat pump in 1 day Energy Savings /Day =627.4-200.64=426.76 kWh/day Energy saving per year= 426.76*300=1,28,028 kWh/Year
  • 41. It means that heat pump can be save up to 61,680 units of electricity per year. •Estimated Cost saving analysis Base rate of electricity for 1 unit= 8 Rs. Therefore, Cost saving per day=8*426.76=3414.08 Rs. Cost saving per Year=3414.08*300=10,24,224 Rs. •Payback period Calculation Market prize of heat pump from manufacturing company is nearly= Rs. 9, 50,000/- (With installation) Therefore, Payback period of heat pump = 1 Year
  • 42. Indoor Environmental Quality (IEQ) improvement There are 2 main contains in IEQ as per ASHRAE 2009 handbook are as follows: •Thermal Comfort Indoor Environmental Health •Air Contaminants For consideration of IEQ the below readings are taken on site. Limits are taken as per factory act 1948. Sr. no Parameters Values Limit as per factory act, 1948 1. Ambient temp 0C Dry bulb 28 290C to 340C Wet bulb 24 220C to 260C 2. Relative humidity% 64 --- 3. Noise level in dB(a) 87.9 90 4. Suspended particular matter, mg/m3 0.09 <=10 5. Oil mist mg/m3 0.019 <=5
  • 43. • Estimated room dimensions for cooling
  • 44. • This chapter includes energy saving potential of electrical heater as well as Heat Pump. • Which clearly shows energy saving potential of • heat pump is very high. • This also includes cost beneficial analysis and impact of heat pump output on IEQ at working condition. Summary
  • 45. 1. On the existing system, study is done on electrical water heating system for crankcase machine line which shows that it has an average electrical energy consumption of 627.6 kWh,15,690 kWh and 1,88,280 kWh for daily, monthly and yearly respectively. 2. The design data is created for the existing process layout. 3. A heat pump system has been designed and electrical consumption has been worked out. 4. The theoretical analysis clearly indicates that the energy conservation has been achieved 426.76 kWh, 10669kWh, 128028 kWh on daily, monthly and yearly basis respectively. 5. This energy consumption is in accordance with the prevailing designed data and the surrounding climatology for automobile industry. 6. The cost saving is achieved Rs 3,414.08 , Rs 85,382, Rs 10,24,224 on daily, monthly and yearly basis respectively. 7. The actual amount of heat pump by market price is nearly Rs 9,50,000 and savings achieved by theoretical calculations is Rs 10,24,224 yearly at base price of electricity Rs 8 per unit. So the calculated payback period is nearly one year. Conclusion
  • 46. In view of conclusion heat pump is recommended for energy conservation for such applications in industry. Its value addition like cooling the surrounding is also of prime importance in the view of IEQ. Due to limitations of cost of heat pump and time of period of completion, prototype of heat pump development is remained Future scope • Development of heat pump model. • Analysis of heat pump performance by various refrigerants. • Testing results and analysis performance of heat pump with impact on IEQ
  • 47. Recommendations 1. At the crank case line washing machine there are various other options to replacer that electrical heaters with solar water heater, heat pump, biogas and briquette fire technology and also other renewable energy sources for washing application. 2. After installing any other system for water heating do regularly maintenance and check whether the system works correctly and energy efficiently. 3. Use clean water for washing application and also regularly add makeup water in tank.
  • 48. References 1. Xing Xu, Yunho Hwang*, Reinhard Radermacher,” Refrigerant injection for heat pumping/air conditioning systems: Literature review and challenges discussions” Center for Environmental Energy Engineering, University of Maryland College Park, 3163 Glenn Martin Hall Bldg., MD 20742, USA. 2. MG Apte1*, D Dibartolomeo1, T Hotchi1, AT Hodgson1, SM Lee1; SM Liff2, LI Rainer3, DG Shendell1, DP Sullivan1, and WJ Fisk1, “ Simultaneous Energy Savings and IEQ Improvements in Relocatable Classrooms” Indoor Environment Dept., Lawrence Berkeley National Laboratory, Berkeley, CA, USA Massachusetts Institute of Technology, Boston, MA Davis Energy Group, Davis, CA. 3. Mauro A. S. S. Ravagnani1, Aline P. Silva1 and Jose A. Caballero2,” Optimal Shell and Tube Heat Exchangers Design”, 1State University of Maringá2University of Alicante 1Brazil 2Spain. Guoping Liu*,1, Genfu Xiao1,2, Junting Wang1, Wei Luo1 and Honggun Song1”The Optimal Design of the Scroll Profiles Based on Chaos PSO”, the Open Mechanical Engineering Journal, 2011, 5, 194-198
  • 49. 4. Paul BYRNE*, Redouane GHOUBALI, Jacques MIRIEL,” Scroll compressor modeling for heat pumps using hydrocarbons as refrigerants”" international Journal of Refrigeration 41 (2013) 1-13. 5. Winandy, Eric and Hundy, Guy, "Refrigerant and Scroll Compressor Options for Best Performance of Various European Heat Pump Configurations" (2008). International Refrigeration and Air Conditioning Conference. paper 895 6. Zogg M. 2008. “History of Heat Pumps - Swiss Contributions and International Milestones”, final report, Swiss Federal Office of Energy, Berne; with 285 references, downloadable from www.zogg-engineering.ch/publi/HistoryHP.pdf 7. Tina Fawcett,” The future role of heat pumps in the domestic sector”, Environmental Change Institute University of Oxford South Parks Road Oxford OX1 3QY UK.
  • 50. 8. Tina Fawcett,” The future role of heat pumps in the domestic sector”, Environmental Change Institute University of Oxford South Parks Road Oxford OX1 3QY UK. 9. John Dieckmann, P.E., Member ASHRAE; Bob Zogg, P.E., Member ASHRAE; DetlefWestphalen, Ph.D., Member ASHRAE; Kurt Roth, Ph.D., Associate Member ASHRAE; and James Brodrick, Ph.D., Member,” Heat-Only, Heat-Activated Heat Pumps” ASHRAE Journal, January 2005. © Copyright 2005 American Society of Heating, Refrigerating andAir-Conditioning Engineers, Inc. 10. Bernardi WP, Blevins RP, Sloane BD. Examination and life assessment of fieldtested heat pump water heaters. Prepared by Energy Utilization Systems, Incorporated for Oak Ridge National Laboratory operated by Union Carbide Corporation for the U.S. Department of Energy, December 1982. 11. Sauer HJ, Howell RH. Heat pump systems. USA: John Wiley & Sons, Inc.; 1983
  • 51. 12. Kokkinides L, Sachs HM. Toward market transformation: commercial heat pump water heaters for the „„New York energy $marts Region‟‟. Final Report. Prepared for The New York State energy research and development authority and prepared by American council for an energy efficient economy, NYSERDA, October 2002. 13. ArifHepbasli a, YildizKalinci b,”A review of heat pump water heating systems”,a Department of Mechanical Engineering, Faculty of Engineering, Ege University, 35100 Izmir, Turkey .b Plumbing Technology, Department of Technical Programs, Izmir Vocational School, DokuzEylul University, Education Campus Buca, Izmir, Turkey. 14. Tomasz Sobota (2011). Experimental Prediction of Heat Transfer Correlations in Heat Exchangers, Developments in Heat Transfer, Dr. Marco Aurelio Dos Santos Bernardes (Ed.), ISBN: 978-953-307-569-3,InTech, Available from: http://www.intechopen.com/books/developments-in-heat-transfer/experimentalprediction- of-heat-transfer-correlations-in-heat-exchangers. 15. Kumar, Ph.D., Member ASHRAE, and William J. Fisk, P.E., Member ASHRAE,” IEQ and the Impact On Building Occupants”ASHRAE Journal, April, 2002.
  • 52. 16. Ban-Huat Ng1, ZainalAbidin Akasah2,” Energy-Efficient Buildings: An In-Depth Look into Definitions, and Design Problems”Int. J. Emerg. Sci., 3(4), 345-358, December 2013 ISSN: 2222-4254. 17. Nalawade Shivraj N,”Training report on energy assessment and conservation in Kirloskar oil engine .ltd. Kagal” (2014). Energy Technology, Department of Technology, Shivaji University, Kolhapur. 18. Handbook on “Heat Exchangers selection, Rating and Thermal Design (Second Edition),”by Sadik Kakac1, Hongtan liu2. 19. Handbook on ”Process Heat Transfer”, by Donald Q. Kern. 20. Handbook on” Compact Heat exchangers.” By Kays W. M. and London, A.L.[1984]. 21. Handbook on “ASHRAE standard for IEQ and Energy Standard for Buildings except Low-Rise Residential Buildings”. 22. Data sheet of “Thermo-expansion valve” by Emerson Climate Technologies. 23. http://www.ahrinet.org/site/686/Standards/HVACR-Industry-Standards/Search- Standards 24. http://www.nrcan.gc.ca/energy/publications/efficiency/eeproducts/roomaircond/6667
  • 53. Paper Publications  “ENERGY CONSERVATION ANALYSIS BY APPLICATION OF HEAT PUMP SYSTEM- A CASE STUDY” paper is published in “INTERNATIONAL JOURNAL OF ENGINEERING SCIENCES & RESEARCH TECHNOLOGY.(IJESRT)” Shivraj Nalawade Thesis123_ENERGY CONSERVATION ANALYSIS BY APPLICATION OF HEAT PUMP SYSTEM- A CASE STUDY.pdf  “PERFORMANCE EVALUATION OF HEAT PUMP USING SIMULATION TECHNIQUES FOR REPLACING ELECTRIC WATER HEATING SYSTEM TO ACHIEVE ENERGY CONSERVATION AND IMPROVE IEQ IN AN PROCESS INDUSTRY” paper is published in “INTERNATIONAL JOURNALOF CURRENT RESEARCH” Shivraj Nalawade ThesisPERFORMANCE EVALUATION OF HEAT PUMP USING SIMULATION TECHNIQUES FOR.pdf