30
SPLIT SYSTEM PERFORMANCE DATA
EXP
ANDED PERFORMANCE DA
T
A
H
igh
pre
s
su
re i
s
m
e
as
u
re
d
at
t
h
e
l
iq
u
id s
e
rv
ic
e v
a
lv
e
(
th
e
s
m
a
lle
r
v
a
lv
e
).
Lo
w
pre
ss
u
re i
s
m
e
a
s
u
re
d
a
t
th
e
ga
u
g
e po
rt
c
o
n
n
e
c
ti
on
.
C
a
lc
ul
a
tio
ns
are b
a
s
e
d
o
n
n
o
m
in
a
l C
F
M
a
n
d 70
°
F
i
n
do
or dry
b
u
lb
.
AM
P
S
=
O
u
td
oo
r u
n
it
a
m
ps
(
c
om
p.
+
fa
n
)
K
W
=
T
o
ta
l s
y
st
e
m
p
o
w
e
r
M
O
D
E
L
: AS
Z
1
4
0
2
4
1
A
* /
CA*
F
3
6
3
6
*6
A
*+
T
X
V
/
M
B
R8
0
0
**
-1
H
E
A
T
ING
O
P
E
R
A
T
IO
N
O
u
td
oor
A
m
bi
e
n
t
Te
m
p
e
ra
tur
e
65
60
5
5
50
4
7
45
4
0
35
30
25
2
0
17
1
5
1
0
5
0
-5
-1
0
M
B
h
3
0
.22
8
.62
6
.92
5
.1
24
.0
23
.3
2
1
.6
19
.9
1
7
.9
1
6
.6
1
5
.2
14.
4
1
3
.9
1
2.
4
11.
0
9
.6
8.
2
6
.7
D
e
lt
a
T
3
2
.93
1
.12
9
.32
7
.4
2
6
.1
2
5
.32
3
.52
1
.7
1
9
.51
8
.0
1
6
.61
5
.71
5
.11
3
.51
2
.01
0
.5
8
.9
7
.3
K
W
2
.0
8
2.
04
2
.0
0
1.
9
6
1.
94
1.
92
1
.8
9
1.
8
5
1
.87
1
.8
2
1
.78
1.
76
1.
74
1
.7
0
1.
66
1.
62
1
.5
8
1.
54
A
M
P
S
8
.1
7
.9
7
.7
7
.5
7
.4
7
.3
7
.2
7
.1
7
.0
6
.9
6
.8
6
.7
6
.7
6
.6
6
.5
6
.3
6
.2
6
.1
C
O
P
4
.2
44
.0
93
.9
33
.7
4
3
.6
2
3
.5
43
.3
53
.1
6
2
.8
12
.6
5
2
.5
02
.3
92
.3
32
.1
41
.9
41
.7
31
.5
21
.2
8
E
E
R
1
4
.51
4
.01
3
.41
2
.8
1
2
.4
1
2
.11
1
.41
0
.8
9
.6
9
.1
8
.5
8
.2
7
.9
7
.3
6
.6
5
.9
5
.2
4
.4
L
iq
S
u
ct
L
iq
S
u
c
t
Liq
S
u
c
t
L
iq
S
u
c
t
Liq
S
u
c
t
L
iq
S
uc
t
L
iq
S
u
c
t
L
iq
S
u
c
t
Liq
S
u
c
t
L
iq
S
u
c
t
L
iq
S
u
c
t
65
2
5
1
6
5
2
6
4
72
277
80
2
9
1
8
7
3
0
4
9
4
317
10
1
3
31
10
9
3
4
4
1
1
6
358
12
3
3
72
130
38
5
1
3
7
70
2
7
0
6
5
2
8
3
72
297
79
3
1
1
8
7
3
2
4
9
4
338
10
1
3
52
10
8
3
6
5
1
1
5
379
12
3
3
93
130
40
6
1
3
7
75
2
8
9
6
5
3
0
3
72
317
79
3
3
1
8
6
3
4
6
9
4
360
10
1
3
73
10
8
3
8
7
1
1
5
401
12
2
4
15
129
42
9
1
3
7
65
2
4
2
6
5
2
5
5
72
268
79
2
8
1
8
6
2
9
4
9
3
307
10
0
3
20
10
8
3
3
3
1
1
5
346
12
2
3
59
129
37
2
1
3
6
70
2
6
0
6
5
2
7
4
72
287
79
3
0
0
8
7
3
1
3
9
4
327
10
1
3
40
10
8
3
5
3
1
1
5
366
12
2
3
79
129
39
3
1
3
7
75
2
7
9
6
6
2
9
3
73
307
80
3
2
0
8
7
3
3
4
9
4
347
10
1
3
61
10
9
3
7
4
1
1
6
388
12
3
4
01
130
41
4
1
3
7
65
2
3
6
6
5
2
4
9
72
261
79
2
7
4
8
6
2
8
6
9
3
299
10
0
3
12
10
7
3
2
4
1
1
5
337
12
2
3
50
129
36
3
1
3
6
70
2
5
4
6
5
2
6
7
72
280
79
2
9
3
8
6
3
0
6
9
4
318
10
1
3
31
10
8
34
4
1
15
357
12
2
3
70
129
38
3
1
3
6
75
2
7
2
6
5
2
8
6
73
299
80
3
1
2
8
7
3
2
5
9
4
339
10
1
3
52
10
8
3
6
5
1
1
6
378
12
3
3
91
130
40
4
1
3
7
P
re
s
s
u
re
s
s
h
o
w
n
ar
e f
o
r
mos
t
pop
u
la
r m
a
tc
h
i
n
doo
r u
n
it
W
IT
H
N
O
F
R
O
S
T
O
N
O
U
T
D
O
O
R
C
O
IL
. D
u
e
t
o
f
a
c
to
rs
l
ik
e
a
ir
fl
o
w
, c
har
g
e
, i
n
do
o
r co
il
&
f
ro
s
t,
pr
e
s
su
re
s w
il
l v
a
ry
s
ig
n
if
ic
a
n
tl
y
. L
iqu
id
(
s
m
a
ll
) s
e
rv
ic
e v
a
lv
e
pr
es
s
u
re
s
s
h
o
u
ld
be ±
20
ps
ig
&
s
u
c
tio
n (
a
c
c
es
s
p
o
rt
) p
res
s
u
re
s
s
h
o
u
ld
be
±
5
ps
ig
of
t
h
e
v
a
lu
e
s
l
is
ted i
n
t
h
is
c
h
ar
t.
62
52
22
HE
A
T
IN
G
M
O
D
E
42
47
57
67
In
d
o
o
r R
e
tu
rn
Ai
r D
ry
Bu
lb
T
e
m
p
er
a
tur
e
(º
F
)
17
2
7
L
iq
u
id
V
a
lv
e &
C
o
m
p
resso
r S
u
ct
io
n
P
ress
u
re
O
u
td
o
o
r A
ir
D
ry
B
u
lb
T
e
m
p
er
at
u
re
(
ºF
)
32
Indo
or
Ai
r F
lo
w
Ra
te
37
74
0
85
0
96
0
