Trane CG-PRC007-EN 20-25Ton, Performance, Data - 60 HZ, Full Load, Table PD-3- 20Ton - CGAF-C20

Performance	(20–25Ton)
Data — 60 HZ	Full Load

Table PD-3 — 20Ton — CGAF-C20

								Entering Condenser Air Temperature (Degree F)
				75.0		85.0				95.0			105.0				115.0
	LWT	Percent	Capacity	System			Capacity	System		Capacity	System			Capacity	System			Capacity	System
(Deg F)		Glycol	(Tons)	KW	EER		(Tons)	KW	EER	(Tons)	KW	EER		(Tons)	KW	EER		(Tons)	KW	EER
	20	28	12.0	15.6	9.2	11.4		17.3	8.0	10.8	19.2	6.8	10.1		21.3	5.7	9.4		23.8	4.8
25		24	13.4	16.0	10.0	12.7		17.7	8.6	12.1	19.6	7.4	11.3		21.8	6.2	10.6		24.3	5.2
30		19	14.8	16.4	10.8	14.1		18.1	9.4	13.4	20.1	8.0	12.6		22.3	6.8	11.8		24.9	5.7
35		14	16.4	16.9	11.6	15.6		18.6	10.1	14.8	20.6	8.6	14.0		22.9	7.3	13.1		25.4	6.2
40		0	18.1	17.4	12.5	17.3		19.2	10.9	16.4	21.2	9.3	15.5		23.5	7.9	14.5		26.1	6.7
42		0	18.8	17.6	12.8	18.0		19.4	11.1	17.0	21.4	9.6	16.1		23.7	8.1	15.1		26.3	6.9
44		0	19.5	17.8	13.2	18.6		19.6	11.4	17.7	21.6	9.8	16.7		24.0	8.3	15.6		26.5	7.1
45		0	19.8	17.9	13.3	18.9		19.7	11.5	18.0	21.7	9.9	17.0		24.1	8.5	15.9		26.7	7.1
46		0	20.1	18.0	13.5	19.2		19.8	11.7	18.3	21.8	10.0	17.3		24.2	8.6	16.2		26.8	7.2
48		0	20.8	18.2	13.8	19.9		20.0	11.9	18.9	22.1	10.3	17.9		24.4	8.8	16.7		27.0	7.4
50		0	21.5	18.4	14.1	20.6		20.2	12.2	19.5	22.3	10.5	18.5		24.7	9.0	17.3		27.3	7.6
55		0	23.3	18.9	14.8	22.3		20.8	12.9	21.2	22.9	11.1	20.0		25.3	9.5	18.8		27.9	8.1
60		0	25.2	19.4	15.5	24.0		21.4	13.5	22.9	23.5	11.7	21.6		26.0	10.0	20.3		28.6	8.5

Table PD-4 — 25Ton — CGAF-C25

									Entering Condenser Air Temperature (Degree F)
					75.0		85.0				95.0				105.0				115.0
		LWT	Percent	Capacity	System			Capacity	System			Capacity	System			Capacity	System			Capacity	System
(Deg F)			Glycol	(Tons)	KW	EER		(Tons)	KW	EER		(Tons)	KW	EER		(Tons)	KW	EER		(Tons)	KW	EER
		20	28	15.6	20.9	8.9	14.8		22.9	7.8	14.0		25.2	6.7	13.2		27.8	5.7	12.3		30.7	4.8
25			24	17.4	21.4	9.7	16.5		23.4	8.5	15.7		25.8	7.3	14.7		28.4	6.2	13.8		31.4	5.3
30			19	19.3	21.9	10.6	18.4		24.0	9.2	17.4		26.4	7.9	16.4		29.1	6.8	15.4		32.1	5.8
35			14	21.3	22.5	11.4	20.4		24.6	9.9	19.3		27.0	8.6	18.2		29.8	7.4	17.1		32.8	6.3
40			0	23.7	23.1	12.3	22.6		25.3	10.7	21.5		27.8	9.3	20.3		30.6	8.0	19.1		33.7	6.8
42			0	24.6	23.3	12.6	23.5		25.5	11.0	22.3		28.0	9.5	21.1		30.8	8.2	19.8		34.0	7.0
44			0	25.4	23.6	13.0	24.3		25.8	11.3	23.1		28.3	9.8	21.9		31.1	8.4	20.6		34.3	7.2
45			0	25.9	23.7	13.1	24.7		25.9	11.5	23.5		28.4	9.9	22.3		31.3	8.5	21.0		34.4	7.3
46			0	26.3	23.8	13.3	25.2		26.0	11.6	23.9		28.6	10.0	22.7		31.4	8.7	21.3		34.6	7.4
48			0	27.3	24.1	13.6	26.0		26.3	11.9	24.8		28.9	10.3	23.5		31.7	8.9	22.1		34.9	7.6
50			0	28.2	24.3	13.9	26.9		26.6	12.2	25.6		29.2	10.6	24.3		32.0	9.1	22.9		35.2	7.8
55			0	30.6	25.0	14.7	29.2		27.3	12.9	27.8		29.9	11.2	26.4		32.8	9.6	24.9		36.1	8.3
	60		0	33.0	25.6	15.5	31.6		28.0	13.5	30.1		30.7	11.8	28.6		33.7	10.2	27.0		36.9	8.8

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 (Btu/watt-hour). Power inputs include compressors, condenser fans and control power.

5.Ratings based on evaporator drop of 10°F.

6.Rated in accordance with ARI Standard 550/590-98.

7.Minimum recommended ethylene glycol percentage used for leaving water temperatures below 40°F.

8.Use the following equation to calculate COP values at other than ARI conditions, COP = EER x .2928.

22 CG-PRC007-EN