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RHA - Ferroli

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Correction factor for the use of glycol<br />

Correction factor for the use of glycol IN HEATING MODE<br />

ethylene glycol with water produced between 30÷55ºC.<br />

Percentage Of glycol in mass / volume 0 / 0 10 / 8,9 20 / 18,1 30 / 27,7 40 / 37,5<br />

Freezing point [°C] 0 -3.2 -8 -14 -22<br />

Heating capacity CCPF Power input CCPA 1.000 0.995 0.985 0.975 0.970<br />

Compressor power input CCPA 1.000 1.010 1.015 1.020 1.030<br />

Water flow rate CCQA 1.000 1.038 1.062 1.091 1.127<br />

Water pressure drop CCDP 1.000 1.026 1.051 1.077 1.103<br />

Propylene Glycol with water produced between 30÷55ºC.<br />

Percentage Of glycol in mass / volume 0 / 0 10 / 9,6 20 / 19,4 30 / 29,4 40 / 39,6<br />

Freezing point [°C] 0 -3.3 -7 -13 -21<br />

Heating capacity CCPF Power input CCPA 1.000 0.990 0.975 0.965 0.955<br />

Compressor power input CCPA 1.000 1.010 1.020 1.030 1.040<br />

Water flow rate CCQA 1.000 1.018 1.032 1.053 1.082<br />

Water pressure drop CCDP 1.000 1.026 1.051 1.077 1.103<br />

Correction factor for the use of glycol IN COOLING MODE<br />

ethylene glycol with water produced between 5÷20ºC.<br />

Percentage Of glycol in mass / volume 0 / 0 10 / 8,9 20 / 18,1 30 / 27,7 40 / 37,5<br />

Freezing point [°C] 0 -3.2 -8 -14 -22<br />

Cooling capacity CCPF Power input CCPA 1.00 0.99 0.98 0.97 0.95<br />

Compressor power input CCPA 1.00 1.00 0.99 0.99 0.98<br />

Water flow rate CCQA 1.00 1.04 1.08 1.12 1.16<br />

Water pressure drop CCDP 1.00 1.08 1.16 1.25 1.35<br />

Propylene Glycol with water produced between 5÷20ºC.<br />

Percentage Of glycol in mass / volume 0 / 0 10 / 9,6 20 / 19,4 30 / 29,4 40 / 39,6<br />

Freezing point [°C] 0 -3.3 -7 -13 -21<br />

Cooling capacity CCPF Power input CCPA 1.00 0.98 0.96 0.94 0.92<br />

Compressor power input CCPA 1.00 0.99 0.98 0.95 0.93<br />

Water flow rate CCQA 1.00 1.01 1.03 1.06 1.09<br />

Water pressure drop CCDP 1.00 1.05 1.11 1.22 1,38<br />

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