JOHNSON CONTROLS
46
FORM 150.72-NM3 (1020)
ISSUE DATE 10/05/2020
SECTION 5 – TECHNICAL DATA
Note: Water Pressure Drop Curves may extend past the minimum and maximum water flow ranges.
HEAT EXCHANGER FLOW, GPM
TABLE 3 – ETHYLENE & PROPYLENE GLYCOL CORRECTION FACTORS
ETHYLENE GLYCOL
% WEIGHT TONS
kW
COMPR
GPM
°
F/
TON
PRESS
DROP FREEZE PT
10
0.985
0.997
24.1
1.034
26
20
0.981
0.996
24.9
1.062
16
30
0.974
0.995
26.1
1.096
5
40
0.966
0.991
27.5
1.134
-10
50
0.957
0.989
29.1
1.172
-32
PROPYLENE GLYCOL
% WEIGHT TONS
kW
COMPR
GPM
°
F/
TON
PRESS
DROP FREEZE PT
10
0.983
0.996
24.2
1.048
27
20
0.974
0.995
24.4
1.086
19
30
0.961
0.990
25.1
1.134
8
40
0.946
0.98
26.0
1.186
-5
50
0.928
0.984
27.2
1.247
-25
CURVE
MODEL YLAA
A
240SE, 195HE, 220HE
B
320SE, 360SE, 260HE, 300HE
C
400SE, 435SE, 350HE, 455HE
D
485SE, 440HE
E
390HE, 515HE
1
10
100
1000
1
10
100
P
re
ss
u
re
D
ro
p
(
kP
a)
Water Flow R ate (l/s)
Y LAA E vaporator P ressure D rop (S I U nits)
A
B
D
C
E
Содержание YLAA0195HE
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