Daikin EWLDС13I-SS [19/36] How to use the correction factors proposed in the previous tables

Daikin EWLDС13I-SS [19/36] How to use the correction factors proposed in the previous tables
19
Table 4 - Correction factors for low evaporator leaving water temperature
2 0 -2 -4 -6 -8
0.842 0.785 0.725 0.670 0.613 0.562
0.950 0.940 0.920 0.890 0.870 0.840
Note: Correction factors have to be applied at working conditions: evaporator leaving water temperature 7°C
Table 5 - Correction factors for water and glycol mixture
10% 20% 30% 40% 50%
0.991 0.982 0.972 0.961 0.946
0.996 0.992 0.986 0.976 0.966
1.013 1.04 1.074 1.121 1.178
1.070 1.129 1.181 1.263 1.308
0.985 0.964 0.932 0.889 0.846
0.993 0.983 0.969 0.948 0.929
1.017 1.032 1.056 1.092 1.139
1.120 1.272 1.496 1.792 2.128
Compressor Power Input
Flow Rate (Δ
t
)
Evaporator Pressure Drop
Ethylene Glycol
Propylene Glycol
Cooling Capacity
Compressor Power Input
Flow Rate (Δ
t
)
Evaporator Pressure Drop
Ethylene Glycol (%)
Cooling Capacity
Evaporator Leaving Water Temperature (°C)
Cooling Capacity
Compressor Power Input
How to use the Correction factors proposed in the previous tables
A) Mixture Water and Glycol --- Evaporator leaving water temperature > 4°C
- depending from the type and percentage (%) of glycol filled in the circuit (see table 3.2 and 5)
- multiply the Cooling Capacity, the Compressor Power Input by the Correction factor of Table 5
- starting from this new value of Cooling Capacity, calculate the Flow Rate (l/s) and the Evaporatore Pressure Drop (kPa)
- now multiply the new Flow Rate and the new Evaporator Pressure Drop by the Correction Factors of Table 5
Example
Unit Size: EWLD320I-SS
Mixture: Water
Working condition: ELWT 12/7°C – Saturated DischargeTemperature 45°C
- Cooling capacity: 328kW
- Power input: 83.8kW
- Flow rate (Δt 5°C): 15.67 l/s
- Evaporator pressure drop: 36kPa
Mixture: Water + Ethylene Glycol 30% (for a winter air temperature up to -15°C)
Working condition: ELWT 12/7°C – Saturated DischargeTemperature 45°C
- Cooling capacity: 328 x 0.972 = 319 kW
- Power input: 83.8 x 0.986 = 82.6 kW
- Flow rate (Δt 5°C): 15.24 (referred to 328 kW) x 1.074 = 16.36 l/s
- Evaporator pressure drop: 39 (referred to 16.36l/s) x 1.181 = 46kPa
B) Mixture Water and Glycol --- Evaporator leaving water temperature < 4°C
- depending from the type and percentage (%) of glycol filled in the circuit (see table 3.1 and 3.2 and table 4)
- depending from the evaporator leaving water temperature (see table 4)
- multiply the Cooling Capacity, the Compressor Power Input by the Correction factor of Table 4 and Table 5
- starting from this new value of Cooling Capacity, calculate the Flow Rate (l/s) and the Evaporatore Pressure Drop (kPa)
- now multiply the new Flow Rate and the new Evaporator Pressure Drop by the Correction Factors of Table 5
Example
Unit Size: EWLD320I-SS
Mixture: Water
Standard working condition ELWT 12/7°C – Saturated DischargeTemperature 40°C
- Cooling capacity: 345kW
- Power input: 75.9 kW
- Flow rate (Δt 5°C): 16.48 l/s
- Evaporator pressure drop: 39kPa
Mixture: Water + Glycol 30% (for a low evaporator leaving temperature of -1/-6°C)
Working condition: ELWT -1/-6°C – Saturated DischargeTemperature 40°C
- Cooling capacity: 345 x 0.613 x 0.972 = 206 kW
- Power input: 75.9 x 0.870 x 0.986 = 65.11 kW
- Flow rate (Δt 5°C): 9.84 l/s (referred to 206 kW) x 1.074 = 10.57 l/s
- Evaporator pressure drop: 18 kPa (referred to 10.57 l/s) x 1.181 = 21 kPa

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