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TEST REPORT #6 System Drop-in Tests of R-22 Alternative ... - AHRI

TEST REPORT #6 System Drop-in Tests of R-22 Alternative ... - AHRI

TEST REPORT #6 System Drop-in Tests of R-22 Alternative ... - AHRI

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List <strong>of</strong> Tested Refrigerants’ Compositions (Mass%)ARM-32a R-32/R-125//R-134a/R-1234yf (25/30/25/20)DR-7 R-32/R-1234yf (36/64)L-20 R-32/R-152a/R-1234ze(E) (45/20/35)LTR4X R-32/R-125/R-134a/R-1234ze(E) (28/25/16/31)LTR6A R-32/R-744/R-1234ze(E) (30/7/63)D52Y R-32/R-125/R-1234yf (15/25/60)


Trane Koolman <strong>Tests</strong> <strong>of</strong> "HP" Alternate RefrigerantsAppendix A: Instrumentation ListID # ** Description Units Stated Sensor Accuracy Measurement Accuracy1 BPHX Water Flow GPM SI: m³/h ± 0.5% <strong>of</strong> Rdg ± 0.5% <strong>of</strong> Rdg2 BPHX Waterside Delta P psid SI: kPa∙diff 0.2% <strong>of</strong> Span ± 0.054 PSID3 Ent BPHX Water Pressure psia SI: kPa∙abs 0.05% <strong>of</strong> FS ± 0.375 PSIA4 Lvg BPHX Water Pressure psia SI: kPa∙abs 0.05% <strong>of</strong> FS ± 0.375 PSIA5 Enter<strong>in</strong>g BPHX Water Temp °F SI: °C ± 0.1 F6 Leav<strong>in</strong>g BPHX Water Temp °F SI: °C ± 0.1 F7 Outdoor Air DB Temp °F SI: °C ± 0.1 F8 Outdoor Air WB Temp °F SI: °C ± 0.5 F9 Barometric Pressure psia SI: kPa∙abs 0.1% <strong>of</strong> FS ± 0.0157 PSIA10 Compressor Discharge Refr Pressure psia SI: kPa∙abs 0.05% <strong>of</strong> FS ± 0.375 PSIA11 RTPF Vapor Refr Pressure psia SI: kPa∙abs 0.05% <strong>of</strong> FS ± 0.375 PSIA12 RTPF Liquid Refr Pressure psia SI: kPa∙abs 0.05% <strong>of</strong> FS ± 0.375 PSIA13 Enter<strong>in</strong>g TXV Refr Pressure psia SI: kPa∙abs 0.05% <strong>of</strong> FS ± 0.375 PSIA14 BPHX Liquid Refr Pressure psia SI: kPa∙abs 0.05% <strong>of</strong> FS ± 0.375 PSIA15 BPHX Vapor Refr Pressure psia SI: kPa∙abs 0.05% <strong>of</strong> FS ± 0.375 PSIA16 Compressor Suction Pressure psia SI: kPa∙abs 0.05% <strong>of</strong> FS ± 0.375 PSIA20 Compressor Discharge Refr Temp °F SI: °C ± 1.0 F21 RTPF Vapor Refr Temp °F SI: °C ± 1.0 F<strong>22</strong> RTPF Liquid Refr Temp °F SI: °C ± 1.0 F23 Enter<strong>in</strong>g TXV Refr Temp °F SI: °C ± 1.0 F24 BPHX Liquid Refr Temp °F SI: °C ± 1.0 F25 BPHX Vapor Refr Temp °F SI: °C ± 1.0 F26 Compressor Suction Temp °F SI: °C ± 1.0 F30 Ent RTPF Circuit Temp #1 (cool<strong>in</strong>g) °F SI: °C ± 1.0 F31 Ent RTPF Circuit Temp #2 (cool<strong>in</strong>g) °F SI: °C ± 1.0 F32 Ent RTPF Circuit Temp #3 (cool<strong>in</strong>g) °F SI: °C ± 1.0 F33 Ent RTPF Circuit Temp #4 (cool<strong>in</strong>g) °F SI: °C ± 1.0 F34 Ent RTPF Circuit Temp #5 (cool<strong>in</strong>g) °F SI: °C ± 1.0 F35 Ent RTPF Circuit Temp <strong>#6</strong> (cool<strong>in</strong>g) °F SI: °C ± 1.0 F36 Ent RTPF Circuit Temp #7 (cool<strong>in</strong>g) °F SI: °C ± 1.0 F37 Ent RTPF Circuit Temp #8 (cool<strong>in</strong>g) °F SI: °C ± 1.0 F40 Lvg RTPF Circuit Temp #1 (cool<strong>in</strong>g) °F SI: °C ± 1.0 F41 Lvg RTPF Circuit Temp #2 (cool<strong>in</strong>g) °F SI: °C ± 1.0 F42 Lvg RTPF Circuit Temp #3 (cool<strong>in</strong>g) °F SI: °C ± 1.0 F43 Lvg RTPF Circuit Temp #4 (cool<strong>in</strong>g) °F SI: °C ± 1.0 F44 Lvg RTPF Circuit Temp #5 (cool<strong>in</strong>g) °F SI: °C ± 1.0 F45 Lvg RTPF Circuit Temp <strong>#6</strong> (cool<strong>in</strong>g) °F SI: °C ± 1.0 F46 Lvg RTPF Circuit Temp #7 (cool<strong>in</strong>g) °F SI: °C ± 1.0 F47 Lvg RTPF Circuit Temp #8 (cool<strong>in</strong>g) °F SI: °C ± 1.0 F50 Liquid Refrigerant Flow GPM SI: m³/h ± 0.5% <strong>of</strong> Rdg ± 0.5% <strong>of</strong> Rdg51 Compressor Liquid Injection Flow GPM SI: m³/h ± 0.5% <strong>of</strong> Rdg ± 0.5% <strong>of</strong> Rdg60 Compressor Voltage AB V SI: V 0.2% <strong>of</strong> Rdg + ± 0.1% <strong>of</strong> Range61 Compressor Voltage BC V SI: V 0.2% <strong>of</strong> Rdg + ± 0.1% <strong>of</strong> Range62 Compressor Voltage AC V SI: V 0.2% <strong>of</strong> Rdg + ± 0.1% <strong>of</strong> Range63 Compressor Current A A SI: A 0.2% <strong>of</strong> Rdg + ± 0.1% <strong>of</strong> Rang ~0.5% <strong>of</strong> Rdg w/ CTs64 Compressor Current B A SI: A 0.2% <strong>of</strong> Rdg + ± 0.1% <strong>of</strong> Rang ~0.5% <strong>of</strong> Rdg w/ CTs65 Compressor Current C A SI: A 0.2% <strong>of</strong> Rdg + ± 0.1% <strong>of</strong> Rang ~0.5% <strong>of</strong> Rdg w/ CTs66 Compressor Power W SI: W 0.2% <strong>of</strong> Rdg + ± 0.1% <strong>of</strong> Rang ~0.5% <strong>of</strong> Rdg w/ CTs70 Total Unit Voltage AN V SI: V 0.2% <strong>of</strong> Rdg + ± 0.1% <strong>of</strong> Range71 Total Unit Voltage BN V SI: V 0.2% <strong>of</strong> Rdg + ± 0.1% <strong>of</strong> Range72 Total Unit Voltage AN V SI: V 0.2% <strong>of</strong> Rdg + ± 0.1% <strong>of</strong> Range73 Total Unit Current A A SI: A 0.2% <strong>of</strong> Rdg + ± 0.1% <strong>of</strong> Rang ~0.5% <strong>of</strong> Rdg w/ CTs74 Total Unit Current B A SI: A 0.2% <strong>of</strong> Rdg + ± 0.1% <strong>of</strong> Rang ~0.5% <strong>of</strong> Rdg w/ CTs75 Total Unit Current C A SI: A 0.2% <strong>of</strong> Rdg + ± 0.1% <strong>of</strong> Rang ~0.5% <strong>of</strong> Rdg w/ CTs76 Total Unit Power W SI: W 0.2% <strong>of</strong> Rdg + ± 0.1% <strong>of</strong> Rang ~0.5% <strong>of</strong> Rdg w/ CTs90 Ent RTPF Air Temp #1 °F SI: °C ± 1.0 F91 Ent RTPF Air Temp #2 °F SI: °C ± 1.0 F92 Ent RTPF Air Temp #3 °F SI: °C ± 1.0 F93 Ent RTPF Air Temp #4 °F SI: °C ± 1.0 F94 Ent RTPF Air Temp #5 °F SI: °C ± 1.0 F95 Ent RTPF Air Temp <strong>#6</strong> °F SI: °C ± 1.0 F96 Ent RTPF Air Temp #7 °F SI: °C ± 1.0 F97 Ent RTPF Air Temp #8 °F SI: °C ± 1.0 F98 Ent RTPF Air Temp #9 °F SI: °C ± 1.0 F99 Ent RTPF Air Temp #10 °F SI: °C ± 1.0 F100 Ent RTPF Air Temp #11 °F SI: °C ± 1.0 F101 Ent RTPF Air Temp #12 °F SI: °C ± 1.0 F102 Ent RTPF Air Temp #13 °F SI: °C ± 1.0 F103 Ent RTPF Air Temp #14 °F SI: °C ± 1.0 F104 Ent RTPF Air Temp #15 °F SI: °C ± 1.0 F


Trane Koolman <strong>Tests</strong> <strong>of</strong> "HP" Alternate RefrigerantsAppendix B: Experimental Results at Nom<strong>in</strong>al Operat<strong>in</strong>g ConditionLow GWP AREP SYSTEM DROP‐IN <strong>TEST</strong> DATA FORM page 1Manufacturer:Basic InformationTrane12‐Oct‐2012<strong>Alternative</strong> Refrigerant DR‐7 DuPont<strong>Alternative</strong> Lubricant Type and ISO ViscosityPOE – 160SZBasel<strong>in</strong>e RefrigerantR<strong>22</strong>Basel<strong>in</strong>e Lubricant Type and ISO ViscosityPOE – 160SZMake and Model <strong>of</strong> <strong>System</strong>Koolman CGAR‐0605 – Air‐Cooled Water Chiller / Heat PumpNom<strong>in</strong>al Capacity and Type <strong>of</strong> <strong>System</strong> 15.6 kW cool<strong>in</strong>g / 17.7 kW heat<strong>in</strong>g (4.4 tons / 5.0 tons)Comparison Data Base Alt. SI Units Base Alt. IP Units RatioMode (heat<strong>in</strong>g/cool<strong>in</strong>g) cool<strong>in</strong>gCompressor Type scroll compressor (Copeland ZR81KC‐TFD – 50 Hz, 3φ, 380V)Compressor Displacement 18.7 m³/hr 662ft³/hrNom<strong>in</strong>al Motor Size not listed by Copeland kW not listed by Copeland hpMotor Speed (50 Hz)not listed by Copeland HzExpansion Device Type TXV (Danfoss, TDEX6, 068H4103)Lubricant Charge 1.8 L 1.9qtRefrigerant Charge 4.76 4.99 kg 10.5 11.0 lbm 1.048Composition (at Cmpr Suct)Chilled Leav<strong>in</strong>g Temp 7.2 °C 45°FWater Flow rate 53.0 L/m<strong>in</strong> 14.0gpmOutdoor Dry Bulb 35 °C 95°FAir Wet Bulb n/a °C n/a°FTotal Capacity 14,750 16,203 W 50,329 55,287 Btu/hr 1.099Sensible Capacity n/a n/a W n/a n/a Btu/hr n/aTotal <strong>System</strong> Power Input 5,700 6,961 W 5,700 6,961 W 1.<strong>22</strong>1Power to Compressor 5,369 6,623 W 5,369 6,623 W 1.233COP or EER (total) 2.59 2.33 [] 8.83 7.94 Btu/W∙hr 0.900COP or EER (compressor only) 2.75 2.45 [] 9.37 8.35 Btu/W∙hr 0.891Refrigerant Mass Flow Rate 345 402 kg/hr 761 887 lbm/hr 1.165Other <strong>System</strong> ChangesThe unit tested was returned to orig<strong>in</strong>al production by replac<strong>in</strong>g the compressor and TXV with orig<strong>in</strong>alequipment. The evaporator rema<strong>in</strong>s the one used dur<strong>in</strong>g R410A test<strong>in</strong>g.<strong>System</strong> Data Base Alt. RatioDegradation CoefficientSeasonal Energy Efficiency Ration – SEERHeat<strong>in</strong>g Seasonal Performance Factor – HSPFDR‐7


Trane Koolman <strong>Tests</strong> <strong>of</strong> "HP" Alternate RefrigerantsAppendix B: Experimental Results at Nom<strong>in</strong>al Operat<strong>in</strong>g ConditionLow GWP AREP SYSTEM DROP‐IN <strong>TEST</strong> DATA FORM page 212‐Oct‐2012Type <strong>of</strong> <strong>System</strong>: Koolman CGAR‐0605 Alternate Refrigerant: DR‐7Water/Air Side Data Base Alt. SI Units Base Alt. IP Units Ratio | DiffEvaporator (BPHE)fluidflow ratewater53.1 53.1 L/hr 14.0 14.0 gpm 0.999T enter<strong>in</strong>g 11.2 11.5 °C 52.2 52.8 °F 0.6°FT leav<strong>in</strong>g 7.2 7.2 °C 45.0 44.9 °F ‐0.1°FCondenser (f<strong>in</strong>‐&‐tube coil)fluidairflow rate not msrd L/hr not msrd gpmT enter<strong>in</strong>g °C 95.1 95.0 °F ‐0.0°FT leav<strong>in</strong>g not msrd °C not msrd °FRefrigerant SideBase Alt. Base Alt.T (°C) P (kPa) T (°C) P (kPa) T (°F) P (psia) T (°F) P (psia)Compressor (scroll)suction 6.0 492 8.5 587 42.8 71.4 47.3 85.2discharge 92.9 1982 87.4 2501 199.2 287.4 189.3 362.8suction SH 6.3 6.3 11.4 11.3Condenser (refrig‐to‐air f<strong>in</strong>‐&‐tube coil)<strong>in</strong>let 85.4 1,965 82.3 2,487 185.7 285.0 180.2 360.7outlet 43.8 1,941 42.0 2,458 110.8 281.5 107.6 356.5outlet subcool<strong>in</strong>g 6.2 8.0 11.1 14.4Expansion Device (TXV)<strong>in</strong>let 43.2 1,924 41.7 2,439 109.7 279.1 107.1 353.7<strong>in</strong>let subcool<strong>in</strong>g 6.4 7.9 11.6 14.3Evaporator (water‐to‐refrig BPHE)<strong>in</strong>let 7.4 607 6.2 747 45.4 88.0 43.2 108.3outlet 4.7 505 6.9 604 40.4 73.3 44.4 87.6outlet superheat 4.2 3.8 7.6 6.9Refrigerant Revers<strong>in</strong>g ValveLP <strong>in</strong>let 4.7 505 6.9 604 40.4 73.3 44.4 87.6LP outlet 6.0 492 8.5 587 42.8 71.4 47.3 85.2HP <strong>in</strong>let 92.9 1,982 87.4 2,501 199.2 287.4 189.3 362.8HP outlet 85.4 1,965 82.3 2,487 185.7 285.0 180.2 360.7DR‐7


Trane Koolman <strong>Tests</strong> <strong>of</strong> "HP" Alternate RefrigerantsAppendix B: Experimental Results at Nom<strong>in</strong>al Operat<strong>in</strong>g ConditionLow GWP AREP SYSTEM DROP‐IN <strong>TEST</strong> DATA FORM page 1Manufacturer:Basic InformationTrane12‐Oct‐2012<strong>Alternative</strong> Refrigerant ARM‐32a Arkema<strong>Alternative</strong> Lubricant Type and ISO ViscosityPOE – 160SZBasel<strong>in</strong>e RefrigerantR<strong>22</strong>Basel<strong>in</strong>e Lubricant Type and ISO ViscosityPOE – 160SZMake and Model <strong>of</strong> <strong>System</strong>Koolman CGAR‐0605 – Air‐Cooled Water Chiller / Heat PumpNom<strong>in</strong>al Capacity and Type <strong>of</strong> <strong>System</strong> 15.6 kW cool<strong>in</strong>g / 17.7 kW heat<strong>in</strong>g (4.4 tons / 5.0 tons)Comparison Data Base Alt. SI Units Base Alt. IP Units RatioMode (heat<strong>in</strong>g/cool<strong>in</strong>g) cool<strong>in</strong>gCompressor Type scroll compressor (Copeland ZR81KC‐TFD – 50 Hz, 3φ, 380V)Compressor Displacement 18.7 m³/hr 662ft³/hrNom<strong>in</strong>al Motor Size not listed by Copeland kW not listed by Copeland hpMotor Speed (50 Hz)not listed by Copeland HzExpansion Device Type TXV (Danfoss, TDEX6, 068H4103)Lubricant Charge 1.8 L 1.9qtRefrigerant Charge 4.76 4.99 kg 10.5 11.0 lbm 1.048Composition (at Cmpr Suct)Chilled Leav<strong>in</strong>g Temp 7.2 °C 45°FWater Flow rate 53.0 L/m<strong>in</strong> 14.0gpmOutdoor Dry Bulb 35 °C 95°FAir Wet Bulb n/a °C n/a°FTotal Capacity 14,750 15,612 W 50,329 53,269 Btu/hr 1.058Sensible Capacity n/a n/a W n/a n/a Btu/hr n/aTotal <strong>System</strong> Power Input 5,700 6,775 W 5,700 6,775 W 1.189Power to Compressor 5,369 6,431 W 5,369 6,431 W 1.198COP or EER (total) 2.59 2.30 [] 8.83 7.86 Btu/W∙hr 0.891COP or EER (compressor only) 2.75 2.43 [] 9.37 8.28 Btu/W∙hr 0.884Refrigerant Mass Flow Rate 345 405 kg/hr 761 894 lbm/hr 1.174Other <strong>System</strong> ChangesThe unit tested was returned to orig<strong>in</strong>al production by replac<strong>in</strong>g the compressor and TXV with orig<strong>in</strong>alequipment. The evaporator rema<strong>in</strong>s the one used dur<strong>in</strong>g R410A test<strong>in</strong>g.<strong>System</strong> Data Base Alt. RatioDegradation CoefficientSeasonal Energy Efficiency Ration – SEERHeat<strong>in</strong>g Seasonal Performance Factor – HSPFARM‐32a


Trane Koolman <strong>Tests</strong> <strong>of</strong> "HP" Alternate RefrigerantsAppendix B: Experimental Results at Nom<strong>in</strong>al Operat<strong>in</strong>g ConditionLow GWP AREP SYSTEM DROP‐IN <strong>TEST</strong> DATA FORM page 212‐Oct‐2012Type <strong>of</strong> <strong>System</strong>: Koolman CGAR‐0605 Alternate Refrigerant: ARM‐32aWater/Air Side Data Base Alt. SI Units Base Alt. IP Units Ratio | DiffEvaporator (BPHE)fluidflow ratewater53.1 52.9 L/hr 14.0 14.0 gpm 0.996T enter<strong>in</strong>g 11.2 11.4 °C 52.2 52.5 °F 0.4°FT leav<strong>in</strong>g 7.2 7.2 °C 45.0 45.0 °F ‐0.1°FCondenser (f<strong>in</strong>‐&‐tube coil)fluidairflow rate not msrd L/hr not msrd gpmT enter<strong>in</strong>g °C 95.1 95.0 °F ‐0.1°FT leav<strong>in</strong>g not msrd °C not msrd °FRefrigerant SideBase Alt. Base Alt.T (°C) P (kPa) T (°C) P (kPa) T (°F) P (psia) T (°F) P (psia)Compressor (scroll)suction 6.0 492 7.9 565 42.8 71.4 46.2 81.9discharge 92.9 1982 85.1 2430 199.2 287.4 185.1 352.5suction SH 6.3 5.8 11.4 10.5Condenser (refrig‐to‐air f<strong>in</strong>‐&‐tube coil)<strong>in</strong>let 85.4 1,965 80.0 2,415 185.7 285.0 176.0 350.2outlet 43.8 1,941 43.2 2,386 110.8 281.5 109.7 346.0outlet subcool<strong>in</strong>g 6.2 6.6 11.1 11.8Expansion Device (TXV)<strong>in</strong>let 43.2 1,924 42.8 2,366 109.7 279.1 109.0 343.2<strong>in</strong>let subcool<strong>in</strong>g 6.4 6.6 11.6 11.8Evaporator (water‐to‐refrig BPHE)<strong>in</strong>let 7.4 607 7.3 740 45.4 88.0 45.1 107.3outlet 4.7 505 6.1 583 40.4 73.3 43.0 84.5outlet superheat 4.2 3.1 7.6 5.7Refrigerant Revers<strong>in</strong>g ValveLP <strong>in</strong>let 4.7 505 6.1 583 40.4 73.3 43.0 84.5LP outlet 6.0 492 7.9 565 42.8 71.4 46.2 81.9HP <strong>in</strong>let 92.9 1,982 85.1 2,430 199.2 287.4 185.1 352.5HP outlet 85.4 1,965 80.0 2,415 185.7 285.0 176.0 350.2ARM‐32a


Trane Koolman <strong>Tests</strong> <strong>of</strong> "HP" Alternate RefrigerantsAppendix B: Experimental Results at Nom<strong>in</strong>al Operat<strong>in</strong>g ConditionLow GWP AREP SYSTEM DROP‐IN <strong>TEST</strong> DATA FORM page 1Manufacturer:Basic InformationTrane12‐Oct‐2012<strong>Alternative</strong> Refrigerant L‐20 Honeywell<strong>Alternative</strong> Lubricant Type and ISO ViscosityPOE – 160SZBasel<strong>in</strong>e RefrigerantR<strong>22</strong>Basel<strong>in</strong>e Lubricant Type and ISO ViscosityPOE – 160SZMake and Model <strong>of</strong> <strong>System</strong>Koolman CGAR‐0605 – Air‐Cooled Water Chiller / Heat PumpNom<strong>in</strong>al Capacity and Type <strong>of</strong> <strong>System</strong> 15.6 kW cool<strong>in</strong>g / 17.7 kW heat<strong>in</strong>g (4.4 tons / 5.0 tons)Comparison Data Base Alt. SI Units Base Alt. IP Units RatioMode (heat<strong>in</strong>g/cool<strong>in</strong>g) cool<strong>in</strong>gCompressor Type scroll compressor (Copeland ZR81KC‐TFD – 50 Hz, 3φ, 380V)Compressor Displacement 18.7 m³/hr 662ft³/hrNom<strong>in</strong>al Motor Size not listed by Copeland kW not listed by Copeland hpMotor Speed (50 Hz)not listed by Copeland HzExpansion Device Type TXV (Danfoss, TDEX6, 068H4103)Lubricant Charge 1.8 L 1.9qtRefrigerant Charge 4.76 4.31 kg 10.5 9.5 lbm 0.905Composition (at Cmpr Suct)Chilled Leav<strong>in</strong>g Temp 7.2 °C 45°FWater Flow rate 53.0 L/m<strong>in</strong> 14.0gpmOutdoor Dry Bulb 35 °C 95°FAir Wet Bulb n/a °C n/a°FTotal Capacity 14,750 14,857 W 50,329 50,695 Btu/hr 1.007Sensible Capacity n/a n/a W n/a n/a Btu/hr n/aTotal <strong>System</strong> Power Input 5,700 6,052 W 5,700 6,052 W 1.062Power to Compressor 5,369 5,718 W 5,369 5,718 W 1.065COP or EER (total) 2.59 2.46 [] 8.83 8.38 Btu/W∙hr 0.949COP or EER (compressor only) 2.75 2.60 [] 9.37 8.87 Btu/W∙hr 0.946Refrigerant Mass Flow Rate 345 268 kg/hr 761 591 lbm/hr 0.777Other <strong>System</strong> ChangesThe unit tested was returned to orig<strong>in</strong>al production by replac<strong>in</strong>g the compressor and TXV with orig<strong>in</strong>alequipment. The evaporator rema<strong>in</strong>s the one used dur<strong>in</strong>g R410A test<strong>in</strong>g.<strong>System</strong> Data Base Alt. RatioDegradation CoefficientSeasonal Energy Efficiency Ration – SEERHeat<strong>in</strong>g Seasonal Performance Factor – HSPFL‐20


Trane Koolman <strong>Tests</strong> <strong>of</strong> "HP" Alternate RefrigerantsAppendix B: Experimental Results at Nom<strong>in</strong>al Operat<strong>in</strong>g ConditionLow GWP AREP SYSTEM DROP‐IN <strong>TEST</strong> DATA FORM page 212‐Oct‐2012Type <strong>of</strong> <strong>System</strong>: Koolman CGAR‐0605 Alternate Refrigerant: L‐20Water/Air Side Data Base Alt. SI Units Base Alt. IP Units Ratio | DiffEvaporator (BPHE)fluidflow ratewater53.1 52.7 L/hr 14.0 13.9 gpm 0.992T enter<strong>in</strong>g 11.2 11.2 °C 52.2 52.2 °F ‐0.0°FT leav<strong>in</strong>g 7.2 7.2 °C 45.0 44.9 °F ‐0.1°FCondenser (f<strong>in</strong>‐&‐tube coil)fluidairflow rate not msrd L/hr not msrd gpmT enter<strong>in</strong>g °C 95.1 95.0 °F ‐0.1°FT leav<strong>in</strong>g not msrd °C not msrd °FRefrigerant SideBase Alt. Base Alt.T (°C) P (kPa) T (°C) P (kPa) T (°F) P (psia) T (°F) P (psia)Compressor (scroll)suction 6.0 492 9.8 490 42.8 71.4 49.6 71.0discharge 92.9 1982 98.0 2142 199.2 287.4 208.4 310.7suction SH 6.3 6.5 11.4 11.8Condenser (refrig‐to‐air f<strong>in</strong>‐&‐tube coil)<strong>in</strong>let 85.4 1,965 90.6 2,133 185.7 285.0 195.1 309.4outlet 43.8 1,941 42.5 2,114 110.8 281.5 108.5 306.7outlet subcool<strong>in</strong>g 6.2 5.3 11.1 9.5Expansion Device (TXV)<strong>in</strong>let 43.2 1,924 42.0 2,104 109.7 279.1 107.5 305.2<strong>in</strong>let subcool<strong>in</strong>g 6.4 5.6 11.6 10.2Evaporator (water‐to‐refrig BPHE)<strong>in</strong>let 7.4 607 2.8 581 45.4 88.0 37.0 84.3outlet 4.7 505 7.5 500 40.4 73.3 45.6 72.5outlet superheat 4.2 3.7 7.6 6.6Refrigerant Revers<strong>in</strong>g ValveLP <strong>in</strong>let 4.7 505 7.5 500 40.4 73.3 45.6 72.5LP outlet 6.0 492 9.8 490 42.8 71.4 49.6 71.0HP <strong>in</strong>let 92.9 1,982 98.0 2,142 199.2 287.4 208.4 310.7HP outlet 85.4 1,965 90.6 2,133 185.7 285.0 195.1 309.4L‐20


Trane Koolman <strong>Tests</strong> <strong>of</strong> "HP" Alternate RefrigerantsAppendix B: Experimental Results at Nom<strong>in</strong>al Operat<strong>in</strong>g ConditionLow GWP AREP SYSTEM DROP‐IN <strong>TEST</strong> DATA FORM page 1Manufacturer:Basic InformationTrane12‐Oct‐2012<strong>Alternative</strong> Refrigerant LTR4X Mexichem<strong>Alternative</strong> Lubricant Type and ISO ViscosityPOE – 160SZBasel<strong>in</strong>e RefrigerantR<strong>22</strong>Basel<strong>in</strong>e Lubricant Type and ISO ViscosityPOE – 160SZMake and Model <strong>of</strong> <strong>System</strong>Koolman CGAR‐0605 – Air‐Cooled Water Chiller / Heat PumpNom<strong>in</strong>al Capacity and Type <strong>of</strong> <strong>System</strong> 15.6 kW cool<strong>in</strong>g / 17.7 kW heat<strong>in</strong>g (4.4 tons / 5.0 tons)Comparison Data Base Alt. SI Units Base Alt. IP Units RatioMode (heat<strong>in</strong>g/cool<strong>in</strong>g) cool<strong>in</strong>gCompressor Type scroll compressor (Copeland ZR81KC‐TFD – 50 Hz, 3φ, 380V)Compressor Displacement 18.7 m³/hr 662ft³/hrNom<strong>in</strong>al Motor Size not listed by Copeland kW not listed by Copeland hpMotor Speed (50 Hz)not listed by Copeland HzExpansion Device Type TXV (Danfoss, TDEX6, 068H4103)Lubricant Charge 1.8 L 1.9qtRefrigerant Charge 4.76 4.76 kg 10.5 10.5 lbm 1.000Composition (at Cmpr Suct)Chilled Leav<strong>in</strong>g Temp 7.2 °C 45°FWater Flow rate 53.0 L/m<strong>in</strong> 14.0gpmOutdoor Dry Bulb 35 °C 95°FAir Wet Bulb n/a °C n/a°FTotal Capacity 14,750 14,790 W 50,329 50,464 Btu/hr 1.003Sensible Capacity n/a n/a W n/a n/a Btu/hr n/aTotal <strong>System</strong> Power Input 5,700 6,297 W 5,700 6,297 W 1.105Power to Compressor 5,369 5,955 W 5,369 5,955 W 1.109COP or EER (total) 2.59 2.35 [] 8.83 8.01 Btu/W∙hr 0.908COP or EER (compressor only) 2.75 2.48 [] 9.37 8.47 Btu/W∙hr 0.904Refrigerant Mass Flow Rate 345 349 kg/hr 761 769 lbm/hr 1.011Other <strong>System</strong> ChangesThe unit tested was returned to orig<strong>in</strong>al production by replac<strong>in</strong>g the compressor and TXV with orig<strong>in</strong>alequipment. The evaporator rema<strong>in</strong>s the one used dur<strong>in</strong>g R410A test<strong>in</strong>g.<strong>System</strong> Data Base Alt. RatioDegradation CoefficientSeasonal Energy Efficiency Ration – SEERHeat<strong>in</strong>g Seasonal Performance Factor – HSPFLTR4X


Trane Koolman <strong>Tests</strong> <strong>of</strong> "HP" Alternate RefrigerantsAppendix B: Experimental Results at Nom<strong>in</strong>al Operat<strong>in</strong>g ConditionLow GWP AREP SYSTEM DROP‐IN <strong>TEST</strong> DATA FORM page 212‐Oct‐2012Type <strong>of</strong> <strong>System</strong>: Koolman CGAR‐0605 Alternate Refrigerant: LTR4XWater/Air Side Data Base Alt. SI Units Base Alt. IP Units Ratio | DiffEvaporator (BPHE)fluidflow ratewater53.1 53.4 L/hr 14.0 14.1 gpm 1.004T enter<strong>in</strong>g 11.2 11.2 °C 52.2 52.1 °F ‐0.0°FT leav<strong>in</strong>g 7.2 7.2 °C 45.0 45.0 °F ‐0.0°FCondenser (f<strong>in</strong>‐&‐tube coil)fluidairflow rate not msrd L/hr not msrd gpmT enter<strong>in</strong>g °C 95.1 95.0 °F ‐0.1°FT leav<strong>in</strong>g not msrd °C not msrd °FRefrigerant SideBase Alt. Base Alt.T (°C) P (kPa) T (°C) P (kPa) T (°F) P (psia) T (°F) P (psia)Compressor (scroll)suction 6.0 492 10.8 500 42.8 71.4 51.5 72.6discharge 92.9 1982 90.4 <strong>22</strong>45 199.2 287.4 194.7 325.7suction SH 6.3 8.6 11.4 15.4Condenser (refrig‐to‐air f<strong>in</strong>‐&‐tube coil)<strong>in</strong>let 85.4 1,965 84.4 2,237 185.7 285.0 184.0 324.4outlet 43.8 1,941 41.2 2,212 110.8 281.5 106.2 320.9outlet subcool<strong>in</strong>g 6.2 6.7 11.1 12.1Expansion Device (TXV)<strong>in</strong>let 43.2 1,924 40.8 2,197 109.7 279.1 105.5 318.7<strong>in</strong>let subcool<strong>in</strong>g 6.4 6.8 11.6 12.3Evaporator (water‐to‐refrig BPHE)<strong>in</strong>let 7.4 607 4.5 635 45.4 88.0 40.1 92.1outlet 4.7 505 7.3 514 40.4 73.3 45.1 74.6outlet superheat 4.2 4.2 7.6 7.6Refrigerant Revers<strong>in</strong>g ValveLP <strong>in</strong>let 4.7 505 7.3 514 40.4 73.3 45.1 74.6LP outlet 6.0 492 10.8 500 42.8 71.4 51.5 72.6HP <strong>in</strong>let 92.9 1,982 90.4 2,245 199.2 287.4 194.7 325.7HP outlet 85.4 1,965 84.4 2,237 185.7 285.0 184.0 324.4LTR4X


Trane Koolman <strong>Tests</strong> <strong>of</strong> "HP" Alternate RefrigerantsAppendix B: Experimental Results at Nom<strong>in</strong>al Operat<strong>in</strong>g ConditionLow GWP AREP SYSTEM DROP‐IN <strong>TEST</strong> DATA FORM page 1Manufacturer:Basic InformationTrane12‐Oct‐2012<strong>Alternative</strong> Refrigerant LTR6A Mexichem<strong>Alternative</strong> Lubricant Type and ISO ViscosityPOE – 160SZBasel<strong>in</strong>e RefrigerantR<strong>22</strong>Basel<strong>in</strong>e Lubricant Type and ISO ViscosityPOE – 160SZMake and Model <strong>of</strong> <strong>System</strong>Koolman CGAR‐0605 – Air‐Cooled Water Chiller / Heat PumpNom<strong>in</strong>al Capacity and Type <strong>of</strong> <strong>System</strong> 15.6 kW cool<strong>in</strong>g / 17.7 kW heat<strong>in</strong>g (4.4 tons / 5.0 tons)Comparison Data Base Alt. SI Units Base Alt. IP Units RatioMode (heat<strong>in</strong>g/cool<strong>in</strong>g) cool<strong>in</strong>gCompressor Type scroll compressor (Copeland ZR81KC‐TFD – 50 Hz, 3φ, 380V)Compressor Displacement 18.7 m³/hr 662ft³/hrNom<strong>in</strong>al Motor Size not listed by Copeland kW not listed by Copeland hpMotor Speed (50 Hz)not listed by Copeland HzExpansion Device Type TXV (Danfoss, TDEX6, 068H4103)Lubricant Charge 1.8 L 1.9qtRefrigerant Charge 4.76 5.44 kg 10.5 12.0 lbm 1.143Composition (at Cmpr Suct)Chilled Leav<strong>in</strong>g Temp 7.2 °C 45°FWater Flow rate 53.0 L/m<strong>in</strong> 14.0gpmOutdoor Dry Bulb 35 °C 95°FAir Wet Bulb n/a °C n/a°FTotal Capacity 14,750 14,971 W 50,329 51,082 Btu/hr 1.015Sensible Capacity n/a n/a W n/a n/a Btu/hr n/aTotal <strong>System</strong> Power Input 5,700 7,112 W 5,700 7,112 W 1.248Power to Compressor 5,369 6,765 W 5,369 6,765 W 1.260COP or EER (total) 2.59 2.11 [] 8.83 7.18 Btu/W∙hr 0.813COP or EER (compressor only) 2.75 2.21 [] 9.37 7.55 Btu/W∙hr 0.806Refrigerant Mass Flow Rate 345 317 kg/hr 761 698 lbm/hr 0.917Other <strong>System</strong> ChangesThe unit tested was returned to orig<strong>in</strong>al production by replac<strong>in</strong>g the compressor and TXV with orig<strong>in</strong>alequipment. The evaporator rema<strong>in</strong>s the one used dur<strong>in</strong>g R410A test<strong>in</strong>g.<strong>System</strong> Data Base Alt. RatioDegradation CoefficientSeasonal Energy Efficiency Ration – SEERHeat<strong>in</strong>g Seasonal Performance Factor – HSPFLTR6A


Trane Koolman <strong>Tests</strong> <strong>of</strong> "HP" Alternate RefrigerantsAppendix B: Experimental Results at Nom<strong>in</strong>al Operat<strong>in</strong>g ConditionLow GWP AREP SYSTEM DROP‐IN <strong>TEST</strong> DATA FORM page 212‐Oct‐2012Type <strong>of</strong> <strong>System</strong>: Koolman CGAR‐0605 Alternate Refrigerant: LTR6AWater/Air Side Data Base Alt. SI Units Base Alt. IP Units Ratio | DiffEvaporator (BPHE)fluidflow ratewater53.1 53.3 L/hr 14.0 14.1 gpm 1.003T enter<strong>in</strong>g 11.2 11.2 °C 52.2 52.2 °F 0.0°FT leav<strong>in</strong>g 7.2 7.2 °C 45.0 45.0 °F ‐0.0°FCondenser (f<strong>in</strong>‐&‐tube coil)fluidairflow rate not msrd L/hr not msrd gpmT enter<strong>in</strong>g °C 95.1 95.0 °F ‐0.0°FT leav<strong>in</strong>g not msrd °C not msrd °FRefrigerant SideBase Alt. Base Alt.T (°C) P (kPa) T (°C) P (kPa) T (°F) P (psia) T (°F) P (psia)Compressor (scroll)suction 6.0 492 10.1 519 42.8 71.4 50.2 75.3discharge 92.9 1982 102.5 2561 199.2 287.4 216.5 371.4suction SH 6.3 4.1 11.4 7.4Condenser (refrig‐to‐air f<strong>in</strong>‐&‐tube coil)<strong>in</strong>let 85.4 1,965 95.0 2,549 185.7 285.0 203.0 369.6outlet 43.8 1,941 40.7 2,531 110.8 281.5 105.2 367.1outlet subcool<strong>in</strong>g 6.2 5.1 11.1 9.2Expansion Device (TXV)<strong>in</strong>let 43.2 1,924 40.3 2,518 109.7 279.1 104.6 365.3<strong>in</strong>let subcool<strong>in</strong>g 6.4 5.3 11.6 9.5Evaporator (water‐to‐refrig BPHE)<strong>in</strong>let 7.4 607 0.2 644 45.4 88.0 32.3 93.3outlet 4.7 505 9.5 532 40.4 73.3 49.1 77.1outlet superheat 4.2 2.8 7.6 5.1Refrigerant Revers<strong>in</strong>g ValveLP <strong>in</strong>let 4.7 505 9.5 532 40.4 73.3 49.1 77.1LP outlet 6.0 492 10.1 519 42.8 71.4 50.2 75.3HP <strong>in</strong>let 92.9 1,982 102.5 2,561 199.2 287.4 216.5 371.4HP outlet 85.4 1,965 95.0 2,549 185.7 285.0 203.0 369.6LTR6A


Trane Koolman <strong>Tests</strong> <strong>of</strong> "HP" Alternate RefrigerantsAppendix B: Experimental Results at Nom<strong>in</strong>al Operat<strong>in</strong>g ConditionLow GWP AREP SYSTEM DROP‐IN <strong>TEST</strong> DATA FORM page 1Manufacturer:Basic InformationTrane15‐Oct‐2012<strong>Alternative</strong> Refrigerant D52Y Daik<strong>in</strong><strong>Alternative</strong> Lubricant Type and ISO ViscosityPOE – 160SZBasel<strong>in</strong>e RefrigerantR<strong>22</strong>Basel<strong>in</strong>e Lubricant Type and ISO ViscosityPOE – 160SZMake and Model <strong>of</strong> <strong>System</strong>Koolman CGAR‐0605 – Air‐Cooled Water Chiller / Heat PumpNom<strong>in</strong>al Capacity and Type <strong>of</strong> <strong>System</strong> 15.6 kW cool<strong>in</strong>g / 17.7 kW heat<strong>in</strong>g (4.4 tons / 5.0 tons)Comparison Data Base Alt. SI Units Base Alt. IP Units RatioMode (heat<strong>in</strong>g/cool<strong>in</strong>g) cool<strong>in</strong>gCompressor Type scroll compressor (Copeland ZR81KC‐TFD – 50 Hz, 3φ, 380V)Compressor Displacement 18.7 m³/hr 662ft³/hrNom<strong>in</strong>al Motor Size not listed by Copeland kW not listed by Copeland hpMotor Speed (50 Hz)not listed by Copeland HzExpansion Device Type TXV (Danfoss, TDEX6, 068H4103)Lubricant Charge 1.8 L 1.9qtRefrigerant Charge 4.76 4.99 kg 10.5 11.0 lbm 1.048Composition (at Cmpr Suct)Chilled Leav<strong>in</strong>g Temp 7.2 °C 45°FWater Flow rate 53.0 L/m<strong>in</strong> 14.0gpmOutdoor Dry Bulb 35 °C 95°FAir Wet Bulb n/a °C n/a°FTotal Capacity 14,750 13,954 W 50,329 47,612 Btu/hr 0.946Sensible Capacity n/a n/a W n/a n/a Btu/hr n/aTotal <strong>System</strong> Power Input 5,700 5,926 W 5,700 5,926 W 1.040Power to Compressor 5,369 5,597 W 5,369 5,597 W 1.042COP or EER (total) 2.59 2.35 [] 8.83 8.03 Btu/W∙hr 0.910COP or EER (compressor only) 2.75 2.49 [] 9.37 8.51 Btu/W∙hr 0.908Refrigerant Mass Flow Rate 345 423 kg/hr 761 933 lbm/hr 1.<strong>22</strong>5Other <strong>System</strong> ChangesThe unit tested was returned to orig<strong>in</strong>al production by replac<strong>in</strong>g the compressor and TXV with orig<strong>in</strong>alequipment. The evaporator rema<strong>in</strong>s the one used dur<strong>in</strong>g R410A test<strong>in</strong>g.<strong>System</strong> Data Base Alt. RatioDegradation CoefficientSeasonal Energy Efficiency Ration – SEERHeat<strong>in</strong>g Seasonal Performance Factor – HSPFD52Y


Trane Koolman <strong>Tests</strong> <strong>of</strong> "HP" Alternate RefrigerantsAppendix B: Experimental Results at Nom<strong>in</strong>al Operat<strong>in</strong>g ConditionLow GWP AREP SYSTEM DROP‐IN <strong>TEST</strong> DATA FORM page 215‐Oct‐2012Type <strong>of</strong> <strong>System</strong>: Koolman CGAR‐0605 Alternate Refrigerant: D52YWater/Air Side Data Base Alt. SI Units Base Alt. IP Units Ratio | DiffEvaporator (BPHE)fluidflow ratewater53.1 53.1 L/hr 14.0 14.0 gpm 0.999T enter<strong>in</strong>g 11.2 11.0 °C 52.2 51.7 °F ‐0.4°FT leav<strong>in</strong>g 7.2 7.2 °C 45.0 45.0 °F ‐0.1°FCondenser (f<strong>in</strong>‐&‐tube coil)fluidairflow rate not msrd L/hr not msrd gpmT enter<strong>in</strong>g °C 95.1 95.0 °F ‐0.1°FT leav<strong>in</strong>g not msrd °C not msrd °FRefrigerant SideBase Alt. Base Alt.T (°C) P (kPa) T (°C) P (kPa) T (°F) P (psia) T (°F) P (psia)Compressor (scroll)suction 6.0 492 8.3 514 42.8 71.4 46.9 74.5discharge 92.9 1982 74.7 2113 199.2 287.4 166.4 306.5suction SH 6.3 5.4 11.4 9.8Condenser (refrig‐to‐air f<strong>in</strong>‐&‐tube coil)<strong>in</strong>let 85.4 1,965 70.2 2,095 185.7 285.0 158.3 303.9outlet 43.8 1,941 42.4 2,065 110.8 281.5 108.4 299.4outlet subcool<strong>in</strong>g 6.2 5.2 11.1 9.4Expansion Device (TXV)<strong>in</strong>let 43.2 1,924 42.1 2,042 109.7 279.1 107.8 296.2<strong>in</strong>let subcool<strong>in</strong>g 6.4 5.2 11.6 9.4Evaporator (water‐to‐refrig BPHE)<strong>in</strong>let 7.4 607 8.9 706 45.4 88.0 48.1 102.4outlet 4.7 505 7.4 533 40.4 73.3 45.4 77.3outlet superheat 4.2 3.5 7.6 6.3Refrigerant Revers<strong>in</strong>g ValveLP <strong>in</strong>let 4.7 505 7.4 533 40.4 73.3 45.4 77.3LP outlet 6.0 492 8.3 514 42.8 71.4 46.9 74.5HP <strong>in</strong>let 92.9 1,982 74.7 2,113 199.2 287.4 166.4 306.5HP outlet 85.4 1,965 70.2 2,095 185.7 285.0 158.3 303.9D52Y

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