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ECL H 0302 E (Airedale)
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| SKU | ECL H 0302 E |
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| Cooler Type | chiller |
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| Product Name |
| Glycol at TWu=25 C, TA=-15 C (Suggested ethylene glycol percentage) | |
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| Glycol at TWu=25 C, TA=-5 C (Suggested ethylene glycol percentage) | |
| Glycol at TWu=25 C, TA=7 C (Suggested ethylene glycol percentage) | |
| Glycol at TWu=25 C, TA=15 C (Suggested ethylene glycol percentage) | |
| Glycol at TWu=25 C, TA=25 C (Suggested ethylene glycol percentage) |
| Glycol at TWu=25 C, TA=35 * C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=25 C, TA=42 * C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=35 C, TA=-15 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=35 C, TA=-5 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=35 C, TA=7 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=35 C, TA=25 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=35 C, TA=35 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=35 C, TA=42 * C (Suggested ethylene glycol percentage) |
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| Ph at TWu=25 C, TA=-15 C (Heating capacity) |
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| Ph at TWu=25 C, TA=-5 C (Heating capacity) |
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| Ph at TWu=25 C, TA=5 C (Heating capacity) |
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| Ph at TWu=25 C, TA=7 C (Heating capacity) |
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| Ph at TWu=25 C, TA=15 C (Heating capacity) |
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| Ph at TWu=25 C, TA=25 C (Heating capacity) |
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| Ph at TWu=25 C, TA=35 * C (Heating capacity) |
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| Ph at TWu=25 C, TA=42 * C (Heating capacity) |
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| Ph at TWu=35 C, TA=-15 C (Heating capacity) |
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| Ph at TWu=35 C, TA=-5 C (Heating capacity) |
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| Ph at TWu=35 C, TA=5 C (Heating capacity) |
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| Ph at TWu=35 C, TA=7 C (Heating capacity) |
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| Ph at TWu=35 C, TA=15 C (Heating capacity) |
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| Ph at TWu=35 C, TA=25 C (Heating capacity) |
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| Ph at TWu=35 C, TA=35 C (Heating capacity) |
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| Ph at TWu=35 C, TA=42 * C (Heating capacity) |
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| Pe at TWu=25 C, TA=-15 C (Input power) |
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| Pe at TWu=25 C, TA=-5 C (Input power) |
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| Pe at TWu=25 C, TA=5 C (Input power) |
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| Pe at TWu=25 C, TA=7 C (Input power) |
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| Pe at TWu=25 C, TA=15 C (Input power) |
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| Pe at TWu=25 C, TA=25 C (Input power) |
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| Pe at TWu=25 C, TA=35 * C (Input power) |
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| Pe at TWu=25 C, TA=42 * C (Input power) |
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| Pe at TWu=35 C, TA=-15 C (Input power) |
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| Pe at TWu=35 C, TA=-5 C (Input power) |
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| Pe at TWu=35 C, TA=5 C (Input power) |
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| Pe at TWu=35 C, TA=7 C (Input power) |
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| Pe at TWu=35 C, TA=15 C (Input power) |
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| Pe at TWu=35 C, TA=25 C (Input power) |
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| Pe at TWu=35 C, TA=35 C (Input power) |
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| Pe at TWu=35 C, TA=42 * C (Input power) |
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| COP at TWu=25 C, TA=-15 C (Coefficient of performance (calculated)) |
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| COP at TWu=25 C, TA=-5 C (Coefficient of performance (calculated)) |
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| COP at TWu=25 C, TA=5 C (Coefficient of performance (calculated)) |
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| COP at TWu=25 C, TA=7 C (Coefficient of performance (calculated)) |
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| COP at TWu=25 C, TA=15 C (Coefficient of performance (calculated)) |
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| COP at TWu=25 C, TA=25 C (Coefficient of performance (calculated)) |
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| COP at TWu=25 C, TA=35 * C (Coefficient of performance (calculated)) |
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| COP at TWu=25 C, TA=42 * C (Coefficient of performance (calculated)) |
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| COP at TWu=35 C, TA=-15 C (Coefficient of performance (calculated)) |
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| COP at TWu=35 C, TA=-5 C (Coefficient of performance (calculated)) |
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| COP at TWu=35 C, TA=5 C (Coefficient of performance (calculated)) |
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| COP at TWu=35 C, TA=7 C (Coefficient of performance (calculated)) |
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| COP at TWu=35 C, TA=15 C (Coefficient of performance (calculated)) |
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| COP at TWu=35 C, TA=25 C (Coefficient of performance (calculated)) |
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| COP at TWu=35 C, TA=35 C (Coefficient of performance (calculated)) |
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| COP at TWu=35 C, TA=42 * C (Coefficient of performance (calculated)) |
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| Qu at TWu=25 C, TA=-15 C (System side water flow rate) |
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| Qu at TWu=25 C, TA=-5 C (System side water flow rate) |
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| Qu at TWu=25 C, TA=5 C (System side water flow rate) |
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| Qu at TWu=25 C, TA=7 C (System side water flow rate) |
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| Qu at TWu=25 C, TA=15 C (System side water flow rate) |
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| Qu at TWu=25 C, TA=25 C (System side water flow rate) |
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| Qu at TWu=25 C, TA=35 * C (System side water flow rate) |
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| Qu at TWu=25 C, TA=42 * C (System side water flow rate) |
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| Qu at TWu=35 C, TA=-15 C (System side water flow rate) |
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| Qu at TWu=35 C, TA=-5 C (System side water flow rate) |
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| Qu at TWu=35 C, TA=5 C (System side water flow rate) |
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| Qu at TWu=35 C, TA=7 C (System side water flow rate) |
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| Qu at TWu=35 C, TA=15 C (System side water flow rate) |
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| Qu at TWu=35 C, TA=25 C (System side water flow rate) |
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| Qu at TWu=35 C, TA=35 C (System side water flow rate) |
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| Qu at TWu=35 C, TA=42 * C (System side water flow rate) |
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| ∆P at TWu=25 C, TA=-15 C (Pressure drop to the exchanger) |
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| ∆P at TWu=25 C, TA=-5 C (Pressure drop to the exchanger) |
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| ∆P at TWu=25 C, TA=5 C (Pressure drop to the exchanger) |
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| ∆P at TWu=25 C, TA=7 C (Pressure drop to the exchanger) |
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| ∆P at TWu=25 C, TA=15 C (Pressure drop to the exchanger) |
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| ∆P at TWu=25 C, TA=25 C (Pressure drop to the exchanger) |
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| ∆P at TWu=25 C, TA=35 * C (Pressure drop to the exchanger) |
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| ∆P at TWu=25 C, TA=42 * C (Pressure drop to the exchanger) |
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| ∆P at TWu=35 C, TA=-15 C (Pressure drop to the exchanger) |
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| ∆P at TWu=35 C, TA=-5 C (Pressure drop to the exchanger) |
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| ∆P at TWu=35 C, TA=5 C (Pressure drop to the exchanger) |
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| ∆P at TWu=35 C, TA=7 C (Pressure drop to the exchanger) |
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| ∆P at TWu=35 C, TA=15 C (Pressure drop to the exchanger) |
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| ∆P at TWu=35 C, TA=25 C (Pressure drop to the exchanger) |
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| ∆P at TWu=35 C, TA=35 C (Pressure drop to the exchanger) |
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| ∆P at TWu=35 C, TA=42 * C (Pressure drop to the exchanger) |
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| Glycol at TWu=45 C, TA=-15 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=45 C, TA=-5 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=45 C, TA=7 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=45 C, TA=15 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=45 C, TA=25 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=45 C, TA=35 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=45 C, TA=42 * C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=55 C, TA=-15 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=55 C, TA=-5 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=55 C, TA=5 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=55 C, TA=7 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=55 C, TA=15 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=55 C, TA=25 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=55 C, TA=35 C (Suggested ethylene glycol percentage) |
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| Glycol at TWu=55 C, TA=42 C (Suggested ethylene glycol percentage) |
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| Ph at TWu=45 C, TA=-15 C (Heating capacity) |
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| Ph at TWu=45 C, TA=-5 C (Heating capacity) |
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| Ph at TWu=45 C, TA=5 C (Heating capacity) |
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| Ph at TWu=45 C, TA=7 C (Heating capacity) |
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| Ph at TWu=45 C, TA=15 C (Heating capacity) |
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| Ph at TWu=45 C, TA=25 C (Heating capacity) |
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| Ph at TWu=45 C, TA=35 C (Heating capacity) |
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| Ph at TWu=45 C, TA=42 * C (Heating capacity) |
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| Ph at TWu=55 C, TA=-15 C (Heating capacity) |
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| Ph at TWu=55 C, TA=-5 C (Heating capacity) |
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| Ph at TWu=55 C, TA=5 C (Heating capacity) |
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| Ph at TWu=55 C, TA=7 C (Heating capacity) |
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| Ph at TWu=55 C, TA=15 C (Heating capacity) |
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| Ph at TWu=55 C, TA=25 C (Heating capacity) |
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| Ph at TWu=55 C, TA=35 C (Heating capacity) |
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| Ph at TWu=55 C, TA=42 C (Heating capacity) |
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| Pe at TWu=45 C, TA=-15 C (Input power) |
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| Pe at TWu=45 C, TA=-5 C (Input power) |
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| Pe at TWu=45 C, TA=5 C (Input power) |
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| Pe at TWu=45 C, TA=7 C (Input power) |
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| Pe at TWu=45 C, TA=15 C (Input power) |
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| Pe at TWu=45 C, TA=25 C (Input power) |
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| Pe at TWu=45 C, TA=35 C (Input power) |
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| Pe at TWu=45 C, TA=42 * C (Input power) |
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| Pe at TWu=55 C, TA=-15 C (Input power) |
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| Pe at TWu=55 C, TA=-5 C (Input power) |
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| Pe at TWu=55 C, TA=5 C (Input power) |
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| Pe at TWu=55 C, TA=7 C (Input power) |
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| Pe at TWu=55 C, TA=15 C (Input power) |
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| Pe at TWu=55 C, TA=25 C (Input power) |
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| Pe at TWu=55 C, TA=35 C (Input power) |
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| Pe at TWu=55 C, TA=42 C (Input power) |
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| COP at TWu=45 C, TA=-15 C (Coefficient of performance (calculated)) |
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| COP at TWu=45 C, TA=-5 C (Coefficient of performance (calculated)) |
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| COP at TWu=45 C, TA=5 C (Coefficient of performance (calculated)) |
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| COP at TWu=45 C, TA=7 C (Coefficient of performance (calculated)) |
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| COP at TWu=45 C, TA=15 C (Coefficient of performance (calculated)) |
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| COP at TWu=45 C, TA=25 C (Coefficient of performance (calculated)) |
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| COP at TWu=45 C, TA=35 C (Coefficient of performance (calculated)) |
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| COP at TWu=45 C, TA=42 * C (Coefficient of performance (calculated)) |
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| COP at TWu=55 C, TA=-15 C (Coefficient of performance (calculated)) |
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| COP at TWu=55 C, TA=-5 C (Coefficient of performance (calculated)) |
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| COP at TWu=55 C, TA=5 C (Coefficient of performance (calculated)) |
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| COP at TWu=55 C, TA=7 C (Coefficient of performance (calculated)) |
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| COP at TWu=55 C, TA=15 C (Coefficient of performance (calculated)) |
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| COP at TWu=55 C, TA=25 C (Coefficient of performance (calculated)) |
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| COP at TWu=55 C, TA=35 C (Coefficient of performance (calculated)) |
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| COP at TWu=55 C, TA=42 C (Coefficient of performance (calculated)) |
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| Qu at TWu=45 C, TA=-15 C (System side water flow rate) |
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| Qu at TWu=45 C, TA=-5 C (System side water flow rate) |
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| Qu at TWu=45 C, TA=5 C (System side water flow rate) |
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| Qu at TWu=45 C, TA=7 C (System side water flow rate) |
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| Qu at TWu=45 C, TA=15 C (System side water flow rate) |
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| Qu at TWu=45 C, TA=25 C (System side water flow rate) |
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| Qu at TWu=45 C, TA=35 C (System side water flow rate) |
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| Qu at TWu=45 C, TA=42 * C (System side water flow rate) |
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| Qu at TWu=55 C, TA=-15 C (System side water flow rate) |
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| Qu at TWu=55 C, TA=-5 C (System side water flow rate) |
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| Qu at TWu=55 C, TA=5 C (System side water flow rate) |
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| Qu at TWu=55 C, TA=7 C (System side water flow rate) |
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| Qu at TWu=55 C, TA=15 C (System side water flow rate) |
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| Qu at TWu=55 C, TA=25 C (System side water flow rate) |
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| Qu at TWu=55 C, TA=35 C (System side water flow rate) |
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| Qu at TWu=55 C, TA=42 C (System side water flow rate) |
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| ∆P at TWu=45 C, TA=-15 C (Pressure drop to the exchanger) |
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| ∆P at TWu=45 C, TA=-5 C (Pressure drop to the exchanger) |
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| ∆P at TWu=45 C, TA=5 C (Pressure drop to the exchanger) |
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| ∆P at TWu=45 C, TA=7 C (Pressure drop to the exchanger) |
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| ∆P at TWu=45 C, TA=15 C (Pressure drop to the exchanger) |
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| ∆P at TWu=45 C, TA=25 C (Pressure drop to the exchanger) |
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| ∆P at TWu=45 C, TA=35 C (Pressure drop to the exchanger) |
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| ∆P at TWu=45 C, TA=42 * C (Pressure drop to the exchanger) |
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| ∆P at TWu=55 C, TA=-15 C (Pressure drop to the exchanger) |
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| ∆P at TWu=55 C, TA=-5 C (Pressure drop to the exchanger) |
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| ∆P at TWu=55 C, TA=5 C (Pressure drop to the exchanger) |
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| ∆P at TWu=55 C, TA=7 C (Pressure drop to the exchanger) |
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| ∆P at TWu=55 C, TA=15 C (Pressure drop to the exchanger) |
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| ∆P at TWu=55 C, TA=25 C (Pressure drop to the exchanger) |
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| ∆P at TWu=55 C, TA=35 C (Pressure drop to the exchanger) |
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| ∆P at TWu=55 C, TA=42 C (Pressure drop to the exchanger) |
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