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18
t
Fig. 40 — Enthalpy Changeover Setpoints
Fig. 41 — EconoMi$er IV Controller
CONTROL
CURVE
A
B
C
D
CONTROL POINT
APPROX. °F (°C)
AT 50% RH
73 (23)
70 (21)
67 (19)
63 (17)
12
1
4
16
1
8
2
0
22
2
4
26
28
30
32
3
4
36
3
8
40
42
44
46
9
0
1
0
0
80
70
6
0
50
40
30
20
10
ENT
HA
LPY—B
TU
P
ER
PO
UN
D DR
Y A
IR
85
(29)
90
(32)
95
(35)
100
(38)
105
(41)
110
(43)
35
(2)
35
(2)
40
(4)
40
(4)
105
(41)
110
(43)
45
(7)
45
(7)
50
(10)
50
(10)
55
(13)
55
(13)
60
(16)
60
(16)
65
(18)
65
(18)
70
(21)
70
(21)
75
(24)
75
(24)
80
(27)
80
(27)
85
(29)
90
(32)
95
(35)
100
(38)
APPROXIMATE DRY BULB TEMPERATURE— °F (°C)
A
A
B
B
C
C
D
D
REL
ATIVE HU
M
IDITY
(%
)
HIGH LIMIT
CURVE
TR1
24 Vac
COM
TR
24
Vac
HOT
1
2
3
4
5
EF
EF1
+
_
P1
T1
P
T
N
EXH
2V
10V
EXH
Set
Set
2V
10V
2V
10V
DCV
DCV
Free
Cool
B
C
A
D
SO+
SR+
SR
SO
AQ1
AQ
DCV
Min
Pos
Open
Max
N1