35
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
L
iqS
u
ct
L
iq
S
u
c
t
L
iqS
u
c
tL
iq
S
u
c
t
L
iqS
u
c
t
L
iq
S
u
c
t
L
iqS
u
c
t
L
iq
S
u
c
t
L
iqS
u
c
t
L
iq
S
u
c
t
L
iqS
u
c
t
65
2
4
5
6
2
2
5
4
69
263
7
6
2
7
2
8
4
2
8
1
91
290
98
2
9
9
105
30
8
1
13
317
12
0
3
26
127
33
6
1
34
70
2
6
3
6
2
2
7
2
69
282
7
6
2
9
1
8
3
3
0
0
91
309
98
3
1
8
105
32
7
1
12
336
12
0
3
45
127
35
4
1
34
75
2
8
2
6
1
2
9
2
69
301
7
6
3
1
0
8
3
3
1
9
90
328
98
3
3
8
105
34
7
1
12
356
11
9
3
65
126
37
4
1
34
65
2
3
7
6
1
2
4
6
68
254
7
6
2
6
3
8
3
2
7
1
90
280
97
2
8
9
104
29
8
1
12
306
11
9
3
15
126
32
4
1
33
70
2
5
5
6
2
2
6
3
69
272
7
6
2
8
1
8
3
2
9
0
90
298
98
3
0
7
105
31
6
1
12
325
11
9
3
33
126
34
2
1
34
75
2
7
3
6
2
2
8
2
69
291
7
7
3
0
0
8
4
3
0
8
91
317
98
3
2
6
105
33
5
1
13
344
12
0
3
52
127
36
1
1
34
65
2
3
1
6
1
2
3
9
68
248
7
6
2
5
6
8
3
2
6
5
90
273
97
2
8
2
104
29
0
1
12
299
11
9
3
07
126
31
6
1
33
70
2
4
86
22
5
7
6
9
26
5
7
6
2
7
4
8
3
2
8
2
90
291
98
2
9
9
1
0
5
30
8
1
12
31
6
11
9
3
25
12
6
33
4
1
34
75
2
6
6
6
2
2
7
5
69
283
7
6
2
9
2
8
4
3
0
1
91
309
98
3
1
8
105
32
6
1
12
335
12
0
3
44
127
35
2
1
34
P
res
s
u
re
s
s
h
o
w
n
ar
e
f
o
r
m
o
s
t
po
pu
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
to
f
a
c
to
rs
l
ik
e
ai
rf
lo
w
, c
har
g
e
, i
n
d
o
o
r co
il
&
f
ro
s
t,
p
ress
u
re
s w
il
l
var
y
s
igni
fi
c
a
n
tl
y
. L
iqu
id
(
s
ma
ll
) s
e
rv
ic
e v
a
lv
e
pr
e
s
s
u
re
s
s
h
o
u
ld
b
e
±
20
ps
ig
&
s
u
c
ti
o
n (
a
c
c
es
s
p
o
rt
) pr
es
s
u
re
s
s
h
o
u
ld
be
±
5
p
s
ig
of
t
h
e
v
a
lues
l
is
ted i
n
t
h
is
c
har
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
mp
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
mp
er
at
u
re
(
ºF
)
32
Indo
or
Ai
r F
lo
w
Ra
te
37
1
180
1
350
1
520
M
O
D
E
L
: AS
Z
1
4
0
4
2
1
A
* /
CA*
F
4
8
6
0
*6
A*
+
T
X
V
/
M
B
R2
0
0
0
**
-1
6
5
H
E
A
T
ING
O
P
E
R
A
T
IO
N
O
u
tdoor
Am
b
ie
n
t
Te
m
p
e
ra
tur
e
65
6
0
5
5
50
4
7
45
4
0
35
30
25
2
0
17
15
1
0
5
0
-5
-1
0
M
B
h
5
1
.54
8
.84
5
.94
2
.9
41
.0
3
9
.7
3
6
.9
3
4
.0
3
4
.3
3
1
.6
2
9
.1
2
7
.5
2
6
.5
2
3
.8
2
1
.1
1
8
.4
1
5
.7
1
2
.8
D
e
lt
a
T
3
4
.13
2
.33
0
.42
8
.4
2
7
.1
2
6
.32
4
.42
2
.52
2
.72
0
.9
1
9
.31
8
.21
7
.51
5
.71
3
.91
2
.11
0
.4
8
.5
K
W
3.
4
0
3.
3
3
3
.2
7
3.
2
1
3.
17
3
.14
3
.0
8
3.
0
2
3.
07
3
.0
0
2
.9
4
2.
9
0
2.
87
2
.8
1
2.
7
4
2.
6
8
2
.6
1
2.
5
4
A
M
P
S
1
5
.2
1
4
.1
1
3
.2
1
2
.4
1
2
.0
1
1
.8
1
1
.1
1
0
.6
1
0
.1
9
.7
9
.2
9
.0
8
.9
8
.5
7
.9
7
.5
6
.9
6
.3
C
O
P
4
.4
44
.2
84
.1
13
.9
2
3
.7
9
3
.7
03
.5
03
.3
03
.2
63
.0
8
2
.9
02
.7
82
.7
02
.4
82
.2
52
.0
11
.7
61
.4
8
E
E
R
1
5
.21
4
.61
4
.01
3
.4
1
2
.9
1
2
.61
2
.01
1
.31
1
.21
0
.5
9
.9
9
.5
9
.2
8
.5
7
.7
6
.9
6
.0
5
.1
