CO vs. Fluorocarbons: Thermodynamic Comparison of ... · ORNL is managed by UT-Battelle, LLC for...
Transcript of CO vs. Fluorocarbons: Thermodynamic Comparison of ... · ORNL is managed by UT-Battelle, LLC for...
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ORNL is managed by UT-Battelle, LLC for the US Department of Energy
CO2 vs. Fluorocarbons: Thermodynamic Comparison of Subcritical and TranscriticalHeat Pump Water Heater (HPWH) EfficiencyKyle R. GluesenkampKashif Nawaz
ACEEE Hot Water ForumNashville, March 13, 2019Session 4A
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Acknowledgments
• Department of Energy (Contract DE-EE0006718.00)• Antonio Bouza, DOE Building Technology Office
DISCLAIMERThis material has been authored by UT-Battelle, LLC under Contract No. DE-AC05-00OR22725 with the U.S. Department of Energy. The United States Government retains and the publisher, by accepting the article for publication, acknowledges that the United States Government retains a non-exclusive, paid-up, irrevocable, world-wide license to publish or reproduce the published form of this manuscript, or allow others to do so, for United States Government purposes. The Department of Energy will provide public access to these results of federally sponsored research in accordance with the DOE Public Access Plan (http://energy.gov/downloads/doe-public-access-plan).
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Classification of HPWHs
Evaporator
HX
Wrap-around:Pumped (or external):
Evaporator
Immersed coil:
Evaporator
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Classification of Stratification Types (Stratification During Heating)
Table 1. Tank Stratification Categories
Category
Heat exchanger (HX) used to transfer
refrigerant heat to water
Locations of tank water taps, OR
coil vertical span
High pressure refrigerant
glideWater or refrigerant flow type Stratifying
potential
1 Water pumped to HX Bottom and top Any Single pass (low water flow) Very strong2 Water pumped to HX Bottom; bottom Any Multi-pass (high water flow) None3 Wrapped around tank3 Spans tank height Low-glide1 Top-down refrigerant flow Moderate4 Wrapped around tank3 Spans tank height High-glide2 Top-down refrigerant flow Strong5 Wrapped around tank3 Spans tank height Any Bottom-up refrigerant flow None 6 Immersed coil – tall3 Spans tank height Low-glide1 Top-down refrigerant flow Moderate7 Immersed coil – tall3 Spans tank height High-glide2 Top-down refrigerant flow Strong8 Immersed coil – tall3 Spans tank height Any Bottom-up refrigerant flow None9 Immersed coil – short3 Bottom region Any Any refr. flow direction None
1for example, a subcritical HFC or HFO (condensing) cycle. 2for example, a transcritical CO2 cycle. 3it is assumed a wrapped tank refrigerant coil will extend for most of the tank height, whereas an immersed coil may have a shorter vertical span.
Table from: Gluesenkamp, Kyle R., John Bush (2016). “Impact on Water Heater Performance of Heating Methods that Promote Tank Temperature Stratification”, ASHRAE Annual Meeting 2016, Conference Paper Session 19, June 29, 2016, St. Louis, MO.
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Condenser and Gas Cooler
Tem
pera
ture
[°F]
condensing
desuperheating
subcooling
refrigerant
water @ 2 GPM
Subcritical cyclecondenser
Tem
pera
ture
[°F]
refrigerant
Transcritical cycle gas cooler
heat exchange pinch point
0
58 58
0
65 65
heat exchange
pinch point
water @ 2 GPM
Cumulative heat transfer [kW, kBtu/hr]
Cumulative heat transfer [kW, kBtu/hr]
2, 6.8 2, 6.8
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Condenser and Gas Cooler
Te
mp
era
ture
[°F
]
Subcritical cycle
Te
mp
era
ture
[°F
]
Transcritical cycle
heat exchange
pinch point
0
58 58
0
wate
r @ 0
.14 G
PM
155 155
water @ 2 GPM65 65
water @ 2 GPM
wate
r @ 0
.14 G
PM
Cumulative heat
transfer [kW, kBtu/hr]
Cumulative heat
transfer [kW, kBtu/hr]
2, 6.8 2, 6.8
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Subcritical Cycle
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Transcritical Cycle
Water in counterflow external HX
Performance relies on availability of cold water: stratification
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Modeling assumptions
• Across all models:– 10 K (18°F) evaporator superheat– 3 K (5°F) closest approach at the
pinch– 0 fan and pump work– 95% motor efficiency– ηisen = 0.90 – 0.0467*PR– ηvol = 1.00 – 0.04*PR– 100 kPa condenser pressure drop– 50 kPa evaporator pressure drop
• CO2-specific:– High side pressure optimized for
COP
• HFC-specific:– 5 K condenser subcooling
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High side pressure optimization
• In transcritical cycles, the high side pressure is a free variable • Proper modeling requires optimization of this pressure
Tgcro = gas cooler refrigerant outlet temperature
Shown for Teri = 15°C
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Polynomial curve fit for optimum high side pressure
• For this work, capacity was ignored and pressure was chosen to maximize COP– In practice, this represents a small (~10%) sacrifice of capacity
• Optimum pressure as function of Teri and Tgcro:
• Poptimum [kPa] = a + bTeri + cTeri2 + dTgcro + eTgcro
2 + fTeriTgcro
– Where Ts are in °C
• Relative error <0.8% of optimum pressure
• Valid range:– 33 < Tgcro < 45°C
– -3 < Teri < 17°C
Coefficient Value
a -107.476661
b 30.9365
c -0.410714286
d 246.74575
e 0.165625
f -1.0285
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Computing closest approach at the pinchCounterflow heat exchanger
Approach temperature: leaving hot vs. entering cold
Approach temperature:
leaving cold vs. entering hot fluid
Closest approach at
the pinch
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Computing closest approach at the pinch
Closest approach at
the pinch
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Results: transcritical cycle performance
(animations – see slides 23-47)
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Results: subcritical cycle performance (R134a)Ambient air temperature = 15°C
Water entering heat pump = 18 °C
COP = 2.8059% of Carnot
COP = 6.4767% of Carnot
Tsupply = 48°C Tsupply = 96°C
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Results: subcritical cycle performance (R1234yf)Ambient air temperature = 15°C
Water entering heat pump = 18 °C
COP = 2.5358% of Carnot
COP = 6.2767% of Carnot
Tsupply = 48°C Tsupply = 96°C
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Results
Ambient air temperature = 15°C
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Results
Ambient air temperature = –5°C
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Results: crossover temperature
CO2 COP advantage over R134a
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Conclusions
• At 15°C Ambient, CO2 has higher COP:– Above 42°C for 18°C return– Above 56°C for 28°C return– Above 67°C for 38°C return
• At -5°C Ambient, CO2 has higher COP:– Above 47°C for 18°C return– Above 54°C for 28°C return– Above 62°C for 38°C return
The “crossover temperature”
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References
• Gluesenkamp, K., Abdelaziz, O., Patel, V., Mandel, B., deAlmeida, V. (May 2017). “High Efficiency Water Heating Technology Development – Final Report, Part II: CO2 and Absorption-Based Residential Heat Pump Water Heater Development” ORNL publication TM-2016/291. Available at http://info.ornl.gov/sites/publications/Files/Pub68329.pdf
• Kashif Nawaz, Bo Shen, Ahmed Elatar, Van Baxter. “Hydroflouroolefins (HFOs) as Low GWP Refrigerants for Residential Heat Pump Water Heaters”, ACEEE HWF 2017.
• Gluesenkamp, K., Bush, J. (2016). “Impact on Water Heater Performance of Heating Methods that Promote Tank Temperature Stratification”, ASHRAE Annual Meeting 2016, Conference Paper Session 19, June 29, 2016, St. Louis, MO.
• B. Shen, K. Nawaz, A. Elatar, V. Baxter, “Development and Validation of Quasi-Steady-State Heat Pump Water Heater Model Having Stratified Water Tank and Wrapped-Tank Condenser” International Journal of Refrigeration, 2018, 87,78-90.
• K. Nawaz, B. Shen, A. Elatar, V. Baxter, O. Abdelaziz, “Performance Optimization of CO2 HPWH System”, International Journal of Refrigeration, 2017, 85, 213-218.
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Thank You
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AnimationAmbient air temperature = 15°C
Supply water temperature = 46°C
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AnimationAmbient air temperature = 15°C
Supply water temperature = 50°C
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AnimationAmbient air temperature = 15°C
Supply water temperature = 54°C
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AnimationAmbient air temperature = 15°C
Supply water temperature = 58°C
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AnimationAmbient air temperature = 15°C
Supply water temperature = 64°C
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AnimationAmbient air temperature = 15°C
Supply water temperature = 68°C
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AnimationAmbient air temperature = 15°C
Supply water temperature = 72°C
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AnimationAmbient air temperature = 15°C
Supply water temperature = 76°C
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AnimationAmbient air temperature = 15°C
Supply water temperature = 80°C
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AnimationAmbient air temperature = 15°C
Supply water temperature = 84°C
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AnimationAmbient air temperature = 15°C
Supply water temperature = 88°C
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AnimationAmbient air temperature = 15°C
Supply water temperature = 92°C
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AnimationAmbient air temperature = 15°C
Supply water temperature = 96°C
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AnimationEvaporation temperature = 15°C
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AnimationEvaporation temperature = 15°C
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AnimationEvaporation temperature = 15°C
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AnimationEvaporation temperature = 15°C
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AnimationEvaporation temperature = 15°C
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AnimationEvaporation temperature = 15°C
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AnimationEvaporation temperature = 15°C
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AnimationEvaporation temperature = 15°C
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AnimationEvaporation temperature = 15°C