
42
UH-SVX01A-EN
Steam Performance Data
Performance based on 2# steam pressure (13.8 kpa) at heater with air entering @ 60°F (16°C).
For Sound Ratings See Pages 28 and 29.
Use conversion table for all metric conversions.
* For the lower output, an optional Speed Controller must be ordered.
†Stated AMP is full load for the standard motors. AMP draw varies by motor manufacturer ± 0.2 AMPS. Please see your unit's motor data plate for exact (FLA) Full Load Amp
rating.
280
280,000
(82.0)
280.0
(126.8)
1100
(102.2)
121
(49)
1/2
(.373)
1100
4200
(1.982)
980
(4.978)
5.4
20
(508.0)
300
300,000
(87.9)
310.0
(140.4)
1250
(116.1)
117
(47)
1/2
(.373)
1100
5000
(2.360)
700
(3.556)
5.4
24
(609.6)
360
360,000
(105.5)
366.0
(165.8)
1500
(139.4)
120
(49)
1/2
(.373)
1100
5500
(2.596)
1000
(5.080)
5.4
24
(609.6)
Table 21. Steam Calculations and Correction Factors
EXAMPLE:
Unit Size: ___________ 24
Steam Pressure____ 10 PSI
Entering Air Temp. ___ 40°F
I. CAPACITY
A. For 2 lbs. steam, 60° entering air
Read output directly from
, 24,000 BTU/
HR. (Ref., Std. 24).
B. For higher steam pressures and/or E.A.T.'s above
or below 60°F
Multiply output from
by appropriate
correction factor from
24,000 x 1.29 = 30,960 BTU/HR.
II. FINAL AIR TEMPERATURE
A. For 2 lbs. steam, 60° entering air
Read temperature directly from
(Ref., Std. 24)
B. For capacities calculated in I.B. (above)
Output from I.B./1.085 x CFM from
+
E.A.T. = Final Air Temp
30,960/1.085 x 450 + 40 = 103.4°F.
III. FINAL AIR VOLUME
A. For 2 lbs. steam, 60° entering air
460 + Final Air Temp from
/ 530 x Nom.
CFM from
= Final Air Volume
460 + 109 / 530 x 450 = 483 CFM
B. For final air temperatures calculated in II.B.
(above)
460 + Final Air Temp from II.B. / 530 x Nom. CFM
from
= Final Air Volume
460 + 103.4 / 530 x 450 = 478 CFM
IV. CONDENSATE PER HOUR
A. For 2 lbs. steam, 60° entering air
Read lbs. per hour from
, 24.5 LBS./HR.
(Ref., Std. 24).
B. For capacities calculated in I.B. (above)
Output from I.B. / Latent Heat From
lbs. per hour of condensate
30,960 / 953 = 32.5 LBS./HR.
Table 22. STEAM CORRECTION FACTORS BASED ON 2 PSI (13.8 kPa) STEAM AND 60 Deg. F (16 Deg. C) E.A.T.
ENTERING
AIR TEMP
Deg. F
(Deg. C)
STEAM PRESSURE (SATURATED) - LBS. PER SQ. IN. (kPa)
0
(0)
2
(13.8)
5
(34.5)
10
(68.9)
15
(103.4)
20
(137.9)
30
(206.8)
40
(275.8)
50
(344.7)
75
(517.1)
100
(689.4)
125
(861.8)
150
(1,034.1)
30 -(1)
1.19
1.24
1.29
1.38
1.44
1.50
1.60
1.68
1.70
1.90
2.02
2.11
2.20
40 (4)
1.11
1.16
1.21
1.29
1.34
1.42
1.51
1.60
1.66
1.81
1.93
2.02
2.11
50 (10)
1.03
1.08
1.13
1.21
1.28
1.33
1.43
1.51
1.58
1.72
1.84
1.93
2.02
60 (16)
0.96
1.00
1.05
1.13
1.19
1.25
1.35
1.43
1.50
1.64
1.75
1.84
1.93
70 (21)
0.88
0.93
0.97
1.06
1.12
1.17
1.27
1.35
1.42
1.55
1.66
1.76
1.84
80 (27)
0.81
0.85
0.90
0.98
1.04
1.10
1.19
1.27
1.34
1.47
1.58
1.68
1.76
90 (32)
0.74
0.78
0.83
0.91
0.97
1.02
1.12
1.19
1.26
1.39
1.50
1.59
1.67
100 (38)
0.67
0.71
0.76
0.84
0.89
0.95
1.04
1.12
1.19
1.32
1.42
1.51
1.59
Table 20. Model S Header Type Only (continued)
Unit Size
Output
BTU/
HR*
(kW)
Cond.
lbs./hr.
(kg/hr)
E.D.R.
Sq. Ft.
(sq. m)
Final Air
Deg. °F
(Deg. °C)
Motor HP
(kW)
RPM
Nominal
CFM (m
3
/s)
Outlet FPM
(m/s)
Nom. Amps
@ 115 VAC
†
Nom. Fan
Diam. Inches
(mm)
Summary of Contents for UHPB
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