Performance |
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Data — 50 HZ | Full Load |
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Table PD-15 — 40Ton — CGAF-C40
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| Entering Condenser Air Temperature (Degree F) |
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| 85.0 |
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| 95.0 |
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| 105.0 |
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| 115.0 |
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| 120.0 |
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LWT | Percent Capacity System |
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| Capacity | System |
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| Capacity | System |
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| Capacity | System |
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| Capacity | System |
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(Deg F) | Glycol |
| (Tons) | KW | EER |
| (Tons) | KW | EER | (Tons) | KW | EER |
| (Tons) | KW | EER |
| (Tons) | KW | EER |
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| 40 | 0 | 28.8 | 30.0 | 11.5 | 27.3 | 33.5 | 9.8 | 25.7 | 37.6 | 8.2 | 24.0 | 42.2 | 6.8 | 23.1 | 44.6 | 6.2 |
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42 | 0 | 29.8 | 30.2 | 11.8 | 28.3 | 33.8 | 10.0 | 26.7 | 37.9 | 8.4 | 25.0 | 42.5 | 7.0 | 24.1 | 45.0 | 6.4 |
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44 | 0 | 30.9 | 30.5 | 12.2 | 29.3 | 34.1 | 10.3 | 27.7 | 38.2 | 8.7 | 25.9 | 42.8 | 7.3 | 25.0 | 45.3 | 6.6 |
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45 | 0 | 31.5 | 30.6 | 12.3 | 29.9 | 34.3 | 10.5 | 28.2 | 38.4 | 8.8 | 26.4 | 43.0 | 7.4 | 25.4 | 45.5 | 6.7 |
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46 | 0 | 32.0 | 30.8 | 12.5 | 30.4 | 34.4 | 10.6 | 28.7 | 38.5 | 8.9 | 26.9 | 43.2 | 7.5 | 25.9 | 45.7 | 6.8 |
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48 | 0 | 33.1 | 31.1 | 12.8 | 31.5 | 34.7 | 10.9 | 29.7 | 38.9 | 9.2 | 27.8 | 43.5 | 7.7 | 26.9 | 46.1 | 7.0 |
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50 | 0 | 34.3 | 31.3 | 13.1 | 32.6 | 35.0 | 11.2 | 30.8 | 39.2 | 9.4 | 28.8 | 43.9 | 7.9 | 27.8 | 46.4 | 7.2 |
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Table PD-16 — 50Ton — CGAF-C50
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| Entering Condenser Air Temperature (Degree F) |
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| 85.0 |
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| 95.0 |
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| 105.0 |
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| 115.0 |
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| 120.0 |
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LWT | Percent CapacitySystem |
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| Capacity | System |
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| Capacity | System |
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| Capacity | System |
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| Capacity | System |
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(Deg F) Glycol | (Tons) | KW | EER |
| (Tons) | KW | EER | (Tons) | KW | EER |
| (Tons) | KW | EER |
| (Tons) | KW | EER |
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| 40 | 0 | 36.0 | 37.2 | 11.6 | 34.2 | 41.3 | 9.9 |
| 32.3 | 45.9 | 8.4 | 30.2 | 51.0 | 7.1 | 29.1 | 53.8 | 6.5 |
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42 | 0 | 37.3 | 37.5 | 11.9 | 35.5 | 41.6 | 10.2 |
| 33.5 | 46.2 | 8.7 | 31.4 | 51.4 | 7.3 | 30.2 | 54.2 | 6.7 |
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44 | 0 | 38.7 | 37.8 | 12.3 | 36.8 | 41.9 | 10.5 |
| 34.8 | 46.6 | 9.0 | 32.6 | 51.8 | 7.5 | 31.4 | 54.6 | 6.9 |
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45 | 0 | 39.4 | 38.0 | 12.4 | 37.5 | 42.1 | 10.7 |
| 35.4 | 46.8 | 9.1 | 33.2 | 52.0 | 7.7 | 32.0 | 54.8 | 7.0 |
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46 | 0 | 40.1 | 38.2 | 12.6 | 38.1 | 42.3 | 10.8 |
| 36.0 | 47.0 | 9.2 | 33.8 | 52.2 | 7.8 | 32.6 | 55.0 | 7.1 |
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48 | 0 | 41.5 | 38.5 | 12.9 | 39.5 | 42.7 | 11.1 |
| 37.3 | 47.4 | 9.5 | 35.0 | 52.6 | 8.0 | 33.8 | 55.4 | 7.3 |
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50 | 0 | 42.9 | 38.8 | 13.3 | 40.9 | 43.0 | 11.4 |
| 38.7 | 47.7 | 9.7 | 36.3 | 53.0 | 8.2 | 35.1 | 55.9 | 7.5 |
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Table PD-17— 60Ton — CGAF-C60
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| Entering Condenser Air Temperature (Degree F) |
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| 85.0 |
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| 95.0 |
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| 105.0 |
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| 115.0 |
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| 120.0 |
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LWT | Percent Capacity | System |
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| Capacity | System |
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| Capacity | System |
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| Capacity | System |
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| Capacity | System |
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(Deg F) | Glycol |
| (Tons) | KW | EER |
| (Tons) | KW | EER | (Tons) | KW | EER |
| (Tons) | KW | EER |
| (Tons) | KW | EER | ||
40 | 0 | 46.6 | 48.3 | 11.6 | 44.1 | 53.7 | 9.9 |
| 41.5 | 59.8 | 8.3 | 38.8 | 66.6 | 7.0 | 37.3 | 70.3 | 6.4 |
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42 | 0 | 48.3 | 48.7 | 11.9 | 45.8 | 54.2 | 10.1 |
| 43.1 | 60.3 | 8.6 | 40.2 | 67.2 | 7.2 | 38.7 | 70.9 | 6.6 |
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44 | 0 | 50.0 | 49.2 | 12.2 | 47.5 | 54.7 | 10.4 |
| 44.7 | 60.9 | 8.8 | 41.8 | 67.8 | 7.4 | 40.2 | 71.5 | 6.8 |
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45 | 0 | 50.9 | 49.4 | 12.4 | 48.3 | 55.0 | 10.5 |
| 45.5 | 61.2 | 8.9 | 42.5 | 68.1 | 7.5 | 41.0 | 71.8 | 6.8 |
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46 | 0 | 51.8 | 49.7 | 12.5 | 49.2 | 55.2 | 10.7 |
| 46.3 | 61.5 | 9.0 | 43.3 | 68.4 | 7.6 | 41.7 | 72.1 | 6.9 |
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48 | 0 | 53.6 | 50.2 | 12.8 | 50.9 | 55.8 | 10.9 |
| 48.0 | 62.1 | 9.3 | 44.9 | 69.0 | 7.8 | 43.2 | 72.8 | 7.1 |
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50 | 0 | 55.4 | 50.7 | 13.1 | 52.6 | 56.3 | 11.2 |
| 49.6 | 62.7 | 9.5 | 46.4 | 69.7 | 8.0 | 44.8 | 73.4 | 7.3 |
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Notes:
1.Data based on 0.0001 fouling factor at sea level.
2.Interpolation between points is permissible.
3.Extrapolation beyond points is not permissible.
4.EER - Energy Efficiency Ratio
5.Ratings based on evaporator drop of 10°F.
6.Rated in accordance with ARI Standard
7.Minimum recommended ethylene glycol percentage used for leaving water temperatures below 40°.
8.Data obtained assuming 400 Volt Supply.
9.Use the following equation to calculate COP values at other than ARI conditions, COP = EER x .2928.
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