Loading the catalog…
ECL H 0752 L (Airedale)
Blurred values are subscriber-only. Sign in to start a free trial — 2 full pages a day — or subscribe for unlimited access.
| SKU | ECL H 0752 L |
|---|
| Cooler Type | chiller |
|---|---|
| Eer | |
| Product Name |
| Pc | |
|---|---|
| Pc | |
| Pc | |
| Pc | |
| Pc | |
| Pc | |
| Pc | |
| Pc |
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| Glycol |
|---|
| Glycol |
|---|
| Glycol |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| Glycol |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Pe |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| Qu |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| ΔP |
|---|
| operating_mode |
|---|
| rating_standard |
|---|
| exchanger_calc_basis |
|---|
| Glycol at TWu=25 C, TA=-15 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=25 C, TA=-5 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=25 C, TA=7 C (Suggested ethylene glycol percentage) |
|---|
| Pc |
|---|
| Pc |
|---|
| Pc |
|---|
| Glycol |
|---|
| Glycol |
|---|
| Glycol |
|---|
| Glycol |
|---|
| Glycol |
|---|
| Pc |
|---|
| 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) |
|---|
| Glycol at TWu=25 C, TA=42 * C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=35 C, TA=-15 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=35 C, TA=-5 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=35 C, TA=7 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=35 C, TA=25 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=35 C, TA=35 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=35 C, TA=42 * C (Suggested ethylene glycol percentage) |
|---|
| Ph at TWu=25 C, TA=-15 C (Heating capacity) |
|---|
| Ph at TWu=25 C, TA=-5 C (Heating capacity) |
|---|
| Ph at TWu=25 C, TA=5 C (Heating capacity) |
|---|
| Ph at TWu=25 C, TA=7 C (Heating capacity) |
|---|
| Ph at TWu=25 C, TA=15 C (Heating capacity) |
|---|
| Ph at TWu=25 C, TA=25 C (Heating capacity) |
|---|
| Ph at TWu=25 C, TA=35 C (Heating capacity) |
|---|
| Ph at TWu=25 C, TA=42 * C (Heating capacity) |
|---|
| Ph at TWu=35 C, TA=-15 C (Heating capacity) |
|---|
| Ph at TWu=35 C, TA=-5 C (Heating capacity) |
|---|
| Ph at TWu=35 C, TA=5 C (Heating capacity) |
|---|
| Ph at TWu=35 C, TA=7 C (Heating capacity) |
|---|
| Ph at TWu=35 C, TA=15 C (Heating capacity) |
|---|
| Ph at TWu=35 C, TA=25 C (Heating capacity) |
|---|
| Ph at TWu=35 C, TA=35 C (Heating capacity) |
|---|
| Ph at TWu=35 C, TA=42 * C (Heating capacity) |
|---|
| Pe at TWu=25 C, TA=-15 C (Input power) |
|---|
| Pe at TWu=25 C, TA=-5 C (Input power) |
|---|
| Pe at TWu=25 C, TA=5 C (Input power) |
|---|
| Pe at TWu=25 C, TA=7 C (Input power) |
|---|
| Pe at TWu=25 C, TA=15 C (Input power) |
|---|
| Pe at TWu=25 C, TA=25 C (Input power) |
|---|
| Pe at TWu=25 C, TA=35 C (Input power) |
|---|
| Pe at TWu=25 C, TA=42 * C (Input power) |
|---|
| Pe at TWu=35 C, TA=-15 C (Input power) |
|---|
| Pe at TWu=35 C, TA=-5 C (Input power) |
|---|
| Pe at TWu=35 C, TA=5 C (Input power) |
|---|
| Pe at TWu=35 C, TA=7 C (Input power) |
|---|
| Pe at TWu=35 C, TA=15 C (Input power) |
|---|
| Pe at TWu=35 C, TA=25 C (Input power) |
|---|
| Pe at TWu=35 C, TA=35 C (Input power) |
|---|
| Pe at TWu=35 C, TA=42 * C (Input power) |
|---|
| COP at TWu=25 C, TA=-15 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=25 C, TA=-5 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=25 C, TA=5 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=25 C, TA=7 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=25 C, TA=15 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=25 C, TA=25 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=25 C, TA=35 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=25 C, TA=42 * C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=35 C, TA=-15 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=35 C, TA=-5 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=35 C, TA=5 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=35 C, TA=7 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=35 C, TA=15 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=35 C, TA=25 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=35 C, TA=35 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=35 C, TA=42 * C (Coefficient of performance (calculated)) |
|---|
| Qu at TWu=25 C, TA=-15 C (System side water flow rate) |
|---|
| Qu at TWu=25 C, TA=-5 C (System side water flow rate) |
|---|
| Qu at TWu=25 C, TA=5 C (System side water flow rate) |
|---|
| Qu at TWu=25 C, TA=7 C (System side water flow rate) |
|---|
| Qu at TWu=25 C, TA=15 C (System side water flow rate) |
|---|
| Qu at TWu=25 C, TA=25 C (System side water flow rate) |
|---|
| Qu at TWu=25 C, TA=35 C (System side water flow rate) |
|---|
| Qu at TWu=25 C, TA=42 * C (System side water flow rate) |
|---|
| Qu at TWu=35 C, TA=-15 C (System side water flow rate) |
|---|
| Qu at TWu=35 C, TA=-5 C (System side water flow rate) |
|---|
| Qu at TWu=35 C, TA=5 C (System side water flow rate) |
|---|
| Qu at TWu=35 C, TA=7 C (System side water flow rate) |
|---|
| Qu at TWu=35 C, TA=15 C (System side water flow rate) |
|---|
| Qu at TWu=35 C, TA=25 C (System side water flow rate) |
|---|
| Qu at TWu=35 C, TA=35 C (System side water flow rate) |
|---|
| Qu at TWu=35 C, TA=42 * C (System side water flow rate) |
|---|
| ∆P at TWu=25 C, TA=-15 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=25 C, TA=-5 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=25 C, TA=5 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=25 C, TA=7 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=25 C, TA=15 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=25 C, TA=25 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=25 C, TA=35 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=25 C, TA=42 * C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=35 C, TA=-15 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=35 C, TA=-5 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=35 C, TA=5 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=35 C, TA=7 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=35 C, TA=15 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=35 C, TA=25 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=35 C, TA=35 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=35 C, TA=42 * C (Pressure drop to the exchanger) |
|---|
| Glycol at TWu=45 C, TA=-15 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=45 C, TA=-5 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=45 C, TA=7 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=45 C, TA=15 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=45 C, TA=25 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=45 C, TA=35 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=45 C, TA=42 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=50 C, TA=-15 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=50 C, TA=-5 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=50 C, TA=5 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=50 C, TA=7 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=50 C, TA=15 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=50 C, TA=25 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=50 C, TA=35 C (Suggested ethylene glycol percentage) |
|---|
| Glycol at TWu=50 C, TA=42 C (Suggested ethylene glycol percentage) |
|---|
| Ph at TWu=45 C, TA=-15 C (Heating capacity) |
|---|
| Ph at TWu=45 C, TA=-5 C (Heating capacity) |
|---|
| Ph at TWu=45 C, TA=5 C (Heating capacity) |
|---|
| Ph at TWu=45 C, TA=7 C (Heating capacity) |
|---|
| Ph at TWu=45 C, TA=15 C (Heating capacity) |
|---|
| Ph at TWu=45 C, TA=25 C (Heating capacity) |
|---|
| Ph at TWu=45 C, TA=35 C (Heating capacity) |
|---|
| Ph at TWu=45 C, TA=42 C (Heating capacity) |
|---|
| Ph at TWu=50 C, TA=-15 C (Heating capacity) |
|---|
| Ph at TWu=50 C, TA=-5 C (Heating capacity) |
|---|
| Ph at TWu=50 C, TA=5 C (Heating capacity) |
|---|
| Ph at TWu=50 C, TA=7 C (Heating capacity) |
|---|
| Ph at TWu=50 C, TA=15 C (Heating capacity) |
|---|
| Ph at TWu=50 C, TA=25 C (Heating capacity) |
|---|
| Ph at TWu=50 C, TA=35 C (Heating capacity) |
|---|
| Ph at TWu=50 C, TA=42 C (Heating capacity) |
|---|
| Pe at TWu=45 C, TA=-15 C (Input power) |
|---|
| Pe at TWu=45 C, TA=-5 C (Input power) |
|---|
| Pe at TWu=45 C, TA=5 C (Input power) |
|---|
| Pe at TWu=45 C, TA=7 C (Input power) |
|---|
| Pe at TWu=45 C, TA=15 C (Input power) |
|---|
| Pe at TWu=45 C, TA=25 C (Input power) |
|---|
| Pe at TWu=45 C, TA=35 C (Input power) |
|---|
| Pe at TWu=45 C, TA=42 C (Input power) |
|---|
| Pe at TWu=50 C, TA=-15 C (Input power) |
|---|
| Pe at TWu=50 C, TA=-5 C (Input power) |
|---|
| Pe at TWu=50 C, TA=5 C (Input power) |
|---|
| Pe at TWu=50 C, TA=7 C (Input power) |
|---|
| Pe at TWu=50 C, TA=15 C (Input power) |
|---|
| Pe at TWu=50 C, TA=25 C (Input power) |
|---|
| Pe at TWu=50 C, TA=35 C (Input power) |
|---|
| Pe at TWu=50 C, TA=42 C (Input power) |
|---|
| COP at TWu=45 C, TA=-15 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=45 C, TA=-5 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=45 C, TA=5 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=45 C, TA=7 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=45 C, TA=15 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=45 C, TA=25 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=45 C, TA=35 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=45 C, TA=42 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=50 C, TA=-15 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=50 C, TA=-5 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=50 C, TA=5 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=50 C, TA=7 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=50 C, TA=15 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=50 C, TA=25 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=50 C, TA=35 C (Coefficient of performance (calculated)) |
|---|
| COP at TWu=50 C, TA=42 C (Coefficient of performance (calculated)) |
|---|
| Qu at TWu=45 C, TA=-15 C (System side water flow rate) |
|---|
| Qu at TWu=45 C, TA=-5 C (System side water flow rate) |
|---|
| Qu at TWu=45 C, TA=5 C (System side water flow rate) |
|---|
| Qu at TWu=45 C, TA=7 C (System side water flow rate) |
|---|
| Qu at TWu=45 C, TA=15 C (System side water flow rate) |
|---|
| Qu at TWu=45 C, TA=25 C (System side water flow rate) |
|---|
| Qu at TWu=45 C, TA=35 C (System side water flow rate) |
|---|
| Qu at TWu=45 C, TA=42 C (System side water flow rate) |
|---|
| Qu at TWu=50 C, TA=-15 C (System side water flow rate) |
|---|
| Qu at TWu=50 C, TA=-5 C (System side water flow rate) |
|---|
| Qu at TWu=50 C, TA=5 C (System side water flow rate) |
|---|
| Qu at TWu=50 C, TA=7 C (System side water flow rate) |
|---|
| Qu at TWu=50 C, TA=15 C (System side water flow rate) |
|---|
| Qu at TWu=50 C, TA=25 C (System side water flow rate) |
|---|
| Qu at TWu=50 C, TA=35 C (System side water flow rate) |
|---|
| Qu at TWu=50 C, TA=42 C (System side water flow rate) |
|---|
| ∆P at TWu=45 C, TA=-15 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=45 C, TA=-5 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=45 C, TA=5 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=45 C, TA=7 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=45 C, TA=15 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=45 C, TA=25 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=45 C, TA=35 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=45 C, TA=42 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=50 C, TA=-15 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=50 C, TA=-5 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=50 C, TA=5 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=50 C, TA=7 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=50 C, TA=15 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=50 C, TA=25 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=50 C, TA=35 C (Pressure drop to the exchanger) |
|---|
| ∆P at TWu=50 C, TA=42 C (Pressure drop to the exchanger) |
|---|
