Refrigerants from a Danfoss Perspective · COP=’1.90 ’ COP=’2.31 ’ COP=’2.28 ’ 75 80 85...
Transcript of Refrigerants from a Danfoss Perspective · COP=’1.90 ’ COP=’2.31 ’ COP=’2.28 ’ 75 80 85...
Refrigeration & A/C Controls | 1 | 1
CO2 for Supermarkets
Torben Funder-Kristensen Danfoss Refrigeration and Air Conditioning Controls [email protected]
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Agenda The history of CO2 Notes on CO2 Basic application of CO2
Subcritical application Transcritical application
Top applications for CO2 in the Cold Chain
Industrial Refrigeration Food Retail Refrigeration (incl. case study)
Trends for CO2 in the Chinese market CO2 Outlook for the future
Conclusion
HFC (CFC) HCFC
NH3
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1850 1993 1960 1920 -1930
The peak of utilizing CO2 as refrigerant
Reinvention of CO2-refrigeration technology (G. Lorentzen)
Proposal to use CO2 as a refrigerant (A. Twining, British patent)
One of the first refrigerants at all Deemed out for decades Finally returned to play a major role within refrigeration applications
The history of CO2
2012
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Notes on CO2
Non-toxic and Low GWP
Energy efficient but observe the limitations for outdoor temperature and design the system accordingly
Systems and components have been under development during the last decade
The state of art performance increases and maturity have not been reached yet
Subcritical CO2
Transcritical & Subcritical CO2
Transcritical & Subcritical CO2
Subcritical CO2
Efficiency Limits of Transcritical CO2
Subcritical CO2
Transcritical & Subcritical CO2
Transcritical & Subcritical CO2
Subcritical CO2Subcritical CO2
Transcritical & Subcritical CO2
Transcritical & Subcritical CO2
Subcritical CO2
Efficiency Limits of Transcritical CO2
75 80 85 90 95 100 105 110 115 120Gas cooler pressure [bar]
0.00
0.25
0.50
0.75
1.00
1.25
1.50
Ref
riger
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g ca
paci
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W] a
nd C
OP
[-] COP
QE
tE = -10 °C, tSH = 10 KtGC,OUT = 35 °C
OPERATING CONDITION
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CO2
NH3 R2XX R4XX R1XX
Subcritical Applications
First applications used in IR and CR
CO2 used up to approx. 50 pressure
CO2 used in cascade with another refrigerant
CO2 used with direct expansion and / or as brine
Many systems installed in especially EU
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CO2
Only used in northern climates
Max pressure up to approx. 120 bar
Two stage compression
CO2 used with direct expansion and / or as brine
Now 1000+ systems installed in especially EU.
Transcritical Applications
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Top Applications for CO2 in Refrigeration Cold Chain
Industrial Refrigeration Safe fluid, running cost savings, first cost savings, and space savings
Food Retail Cheap and safe refrigerant, long term solution, lower running costs,
- and space-heating,
Transport Refrigeration Safe fluid, long term solution, cheap and safe refrigerant, potential future carbon quota offsetting
Bottle Coolers
alternative to R290.
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CO2 in Food Retail Future environmental secured no new phase down State of the art technology Component and system knowhow available CO2 in cascade with HFC/HC/NH3 CO2 in booster systems Globally applicable Higher efficiencies CO2 systems show outstanding performance using heat reclaim
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Food Retail System and Components
New developed technology applicable up to 140 bar pressure Full program of Controls available including supermarket supervision Established and well proven technology Education and training available at Danfoss
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The Fakta Case Study
2nd generation CO2 system
3 system types compared R404a conventional latest technology CO2/CO2 - 1st generation system CO2/CO2 - 2nd generation system
10 stores comparable in each category All stores located within distance of 150 Kilometers Running time is 12 months Data acquisition on remote basis
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CO2 - outlook for the future
Due to the advantages of CO2 seen from an energy, total cost and environmental point of view Danfoss foresees that CO2 will become a major global refrigerant
The technical advantages using CO2 is not yet fully exploited which means a considerable amount of development will still happen
Especially in the field of combining refrigeration and heating purposes a high development potential is foreseen
Relative sizing of pipes to give the same capacity: R134a R22 CO2 Dry suction line Liquid Line
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Conclusion
CO2 has shown to be a competitive refrigerant and environmentally benign in all senses within IR and FR
CO2 applications within IR and FR are showing high growth rates
During the last 10 years a lot of development has taken place and systems are running very reliable.
CO2 systems needs special attention because they are different to HFC and alike systems.
CO2 refrigeration systems in combination with heat recovery is expected grow considerably.
Opportunities with CO2 are far from being exploited. Here is still a lot of room for innovation
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ODP = 0 (Ozone depletion potential) GWP = 1 (Global warming potential) Not flammable Not toxic (EN 378) Low viscosity High volumetric cooling capacity Small compressors Small suction lines
High pressures Low critical temperature High tripple point
co2phasechanges128Kbit.wmv
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0,3
0,4
0,5
0,6
0,7
0,8
0,9
-5 5 15 25 35 45 55tc [°C]
Car
not e
ffici
ency
[-]
R717R22R134aR600aR290R410AR507R404AR407CR744
Poor thermodynamic efficiency of a refrigerant can be compensated for by increased efficiency of components or by changes to the configuration of
the system.
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High Volumetric Cooling Capacity A small volume of refrigerant has a high capacity 5 7 times higher than R22 Smaller line sizes are needed Smaller compressor is needed
High Pressure Refrigerant
1 Kelvin = 1 Bar Effect of line losses is very low
High Density Gas
Heat exchangers become very efficient Low temperature difference between CO2 and air
Relative sizing of pipes to give the same capacity: R134a R22 CO2 Dry suction line Liquid Line
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SUB-CRITICAL
TRANS-CRITICAL
TWO-STAGE COMBINED
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hEVAP hCOMP
COP = 1.90
COP = 2.31
COP = 2.28
75 80 85 90 95 100 105 110 115 120Gas cooler pressure [bar]
0.00
0.25
0.50
0.75
1.00
1.25
1.50
Ref
riger
atin
g ca
paci
ty [k
W] a
nd C
OP
[-] COP
QE
tE = -10 °C, tSH = 10 KtGC,OUT = 35 °C
OPERATING CONDITION