evaluation of r-449a as a replacement for r-22 in low and
TRANSCRIPT
July 11 -14, 2016
Evaluation of R-449A as a Replacement for R-22 in Low and Medium
Temperature Refrigeration
Andrew Pansulla, The Chemours Company
Charles Allgood, The Chemours Company
Agenda
� Regulations
� HFOs/R-449A introduction
� Thermodynamic modeling
� Calorimeter testing
� System testing in an environmental chamber
� TXV considerations
� Conclusions
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Environmental Considerations
Global Warming Potential (GWP)
The potential effect that certain substances have on climate change.
Ozone Depletion Potential (ODP)
The potential for a refrigerant to reduce the amount of ozone in the
stratosphere.
The Regulatory Challenge: R-22 is going away
The EPA has published a final rule on the amount of virgin R-22 allowed to be consumed until production ceases in 2020.
The Montreal Protocol is an
international treaty designed to protect the ozone layer by phasing
out the production of numerous substances that are responsible for
ozone depletion.
Refrigerant History : > 85 years of Enabling Technology
1930s
CFCs(R-12)
ChlorineSingle Bond
High ODPHighest GWP
1950s
HCFCs(R-22)
Less ChlorineSingle Bond
Lower ODPHigh GWP
1990s
HFCs(R-134a)
No ChlorineSingle Bond
No ODPHigh GWP
TODAY
HFOs(R-1234yf)
No ChlorineDouble Bond
No ODPVery Low
GWP
What is an HFO
HFCHydro fluorocarbon
HFCHydro fluorocarbon
HFOHydro fluoro olefin
HFOHydro fluoro olefin
1234yf – The Base HFO Molecule
R-134a HFO-1234yf
Formula CH 2FCF3 CF3CF=CH2
Molecular Weight 102 114
ODP 0 0
GWP100 (AR5) 1300 < 1
T Critical Point 102 ºC 95ºC
Boiling Point -26ºC -29ºC
� Same operating conditions as 134a (similar P/T curve)
� Thermally stable under extreme use conditions
� Capacity and efficiency similar to R-134a
� Mildly flammability (A2L)
0
0.5
1
1.5
2
2.5
3
3.5
-40 -20 0 20 40 60 80 100
134a
1234yfPre
ssur
e, M
Pa
Temperature, oC
R-449A Physical Properties
� R-449A is an HFO blend originally developed as a low GWP replacement for R-404A (and R-22)
� Composition (weight percent): R-32 (24.3%)/R-125 (24.7%)/R-1234yf (25.3%)/R-134a (25.7%)
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Thermodynamic Modeling Assumptions
� R-449A condensing and evaporating pressures calculated to have the same average condensing and evaporating temperatures as R-22
� Superheat and sub cooling calculated from average Tc and Te of R-449A to give the same return gas and liquid line temperatures for all models
� Maximum discharge temperature = 135 oC
� Isentropic efficiency = 0.70
� All models had the same theoretical compressor displacement
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R-22 and R-449A Thermodynamic Modeling
Low Temperature 1 Medium Temperature 2
ASHRAE# R-223 R-449A R-22 R-449A
Relative Capacity 1.00 1.00 1.00 1.03
Relative COP 1.00 0.96 1.00 0.94
Relative Mass Flow
1.00 1.14 1.00 1.11
Suction Pressure
(kpa [abs])
171.7 182.2 398.5 436.4
Discharge Pressure
(kpa [abs])
1554 1785 1554 1785
Discharge Temp (°C) 135 121 98.4 84.6
1LT Conditions: -30°C Evap/40°C Cond/3.89 K Sub Cool/-10°C Return Gas Temperature
2MT Conditions: -10°C Evap/40°C Cond/3.89 K Sub Cool/10 oC Return Gas Temperature
3Assumes liquid injection to maintain a maximum discharge temperature of 135 oC
R-449A Performance:
• Equivalent to 3% larger capacity
• 4-6% lower COP
• 11-14% larger mass flow
Compressor Calorimeter Testing
� Semi hermetic compressor
� Compartment temp = 35oC
� LT Evaporator condition = -31.6 oC
� MT evaporator condition = -6.7 oC
� Sub Cool Amount = 5.5 K
� Maximum discharge temp = 135 oC
� Return gas and condensing temperatures were varied
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Low Temperature Capacity and COP
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Medium Temperature Capacity and COP
System Testing in an Environmental Chamber
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Semi-Hermetic Compressor with a single condensing unit
Med/Low Temp Open Display Case
Environmental Chamber System Testing
� Experimental set up was run in accordance with ASHRAE standard 72
� All tests were run with POE lubricant
� EEV was used to regulate evaporator superheat
� Defrost every 12 hours
� Charge was optimized based on the equivalent liquid volume ratio for the recommended charge
� Performance measurements were taken every six seconds for over a 24 hour period
� “Indoor” temperature/humidity = 23.9 ± 0.27 oC dry bulb and 14.4 ± 0.27 oC wet bulb
� “Outdoor” temperature/humidity = 27.8 ± 0.27 oC dry bulb and 13.3 ±0.27 oC wet bulb
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Display Case Performance Data
Condition Refrigerant Discharge Pressure
(kpa) Discharge Temperature
(oC) Evap Superheat
(K) Evaporator Discharge Air Temp
(oC)
LT R-22 1225 96.1 5.8 -25.8
LT R-449A 1435 86.2 3.2 -26.8
MT R-22 1236 93.0 6.4 -0.2
MT R-449A 1492 76.8 3.3 -2.0
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Product temperatures
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-15.
56
-19.
41
-11.
84
-21.
61
-7.4
5
4.19
2.13
6.17
1.83
6.48
-15.
82
-19.
84
-11.
22
-21.
41
-7.2
3
3.11
1.06
5.39
0.89
5.61
-25.00
-20.00
-15.00
-10.00
-5.00
0.00
5.00
10.00
15.00AT CTSA WTSA CTS WTS AT CTSA WTSA CTS WTS
Low Temp Medium Temp
Tem
pera
ture
[°C
]
R-22 R-449AAT = Average temperature of all test simulators
CTSA = Coldest test simulator average temperature
WTSA = Warmest test simulator average temperature
CTS = Minimum temperature recorded of the coldest simulator
Energy comparison
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30.4
88
26.4
06
30.3
29
25.5
80
0.000
5.000
10.000
15.000
20.000
25.000
30.000
35.000
Low Temp Medium Temp
Ene
rgy
Con
sum
ptio
n [k
Wh/
24h]
Energy Consumption
R-22
R-449A
Med/Low TempOpen Display Case with EEV inEnvironmental Chamber
Background on adjustments
� During refrigeration operation, a TXV balances three pressure forces
� P1 – Opening force of the powerhead
� P2 – Closing force of the suction pressure
� P3 – Closing force of the spring pressure
Adjustable R-22 TXVs
� Suction pressure differences for the same average evaporator temp
» LT: 13.8 kpa higher
» MT: 34.5 kpa higher
� TXVs may need to be opened to reach target superheats
� Mass flow of R-449A is roughly 14% higher than R-22
» No changes to properly sized valves/powerhead are necessary
0.0
100.0
200.0
300.0
400.0
500.0
600.0
-40.0 -30.0 -20.0 -10.0 0.0 10.0
Pre
ssur
e (k
pa)
Temperature (oC)
Set point pressure to reach the same average evaporator temperature for
R-22 and R-449A
R-22
R-449A
Field Data
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0.00
10.00
20.00
30.00
40.00
50.00
60.00
0.00 5.00 10.00 15.00 20.00 25.00
Ene
rgy
(Kw
h)
Hourly Temperature ( oC)
MT R-22 retrofit to R-449A Rack Energy vs Ambient Temperature
R-22
R-449A
Conclusions
� R-22 is being phased out
� HFOs were developed as low GWP and zero ODP alternatives to current HFCs
� R-449A is a HFO containing blend that has exhibited similar or better performance relative to R-22 in:
- Cycle Modeling
- Calorimeter Testing
- System Testing
� During retrofits, minor adjustments to valves might be needed to reach target superheats
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References
� AHRI, Standard 210/240-2008, Unitary A/C and Air Source Heat Pump Standard, Arlington, VA, 2008.
� ASHRAE, Standard 23.1 Methods of Testing for Performance Rating Positive Displacement Refrigerant Compressors and Condensing Units That Operate at Subcritical Temperatures of the Refrigerant, American Society of Heating, Refrigerating and Air-Conditioning Engineers, 2010.
� ASHRAE, Standard 72 Method of Testing Open and Closed Commercial Refrigerators and Freezers, American Society of Heating, Refrigerating and Air-Conditioning Engineers, 2014.
� IPCC. 2013. Climate Change 2013: The physical Science Basis. Contribution of Working Group I to the Fifth Assessment Report of the Intergovernmental Panel on Climate Change. Cambridge University Press, Cambridge, United Kingdom and New York, NY, USA.
� J. Steven Brown, Piotr A. Domanski, Eric W. Lemmon. (2015). Cycle D Version 5.0. National Institute of Standards and Technology.
� Powell, P. (2014). EPA Finalizes R-22 Phaseout Plan. ACHR News. http://www.achrnews.com/articles/127966-epa-finalizes-r-22-phaseout-plan
� UNEP. 2000. The Montreal Protocol on Substances that Deplete the Ozone Layer. The Vienna Convention for the Protection of the Ozone Layer & The Montreal Protocol on Substances that Deplete the Ozone Layer. UNON, Nariobi, Kenya.
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QUESTIONS
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