34
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
: A
S
Z
1
4
0381
A
* -
A
S
P
T
42C
14A
*
H
E
A
T
IN
G
OP
E
R
A
T
IO
N
O
u
td
oor
A
m
bi
e
n
t
Te
m
p
e
r
a
tur
e
65
6
0
55
5
0
47
4
5
40
3
5
30
2
5
20
1
7
15
1
0
5
0
-5
-1
0
M
B
h
4
2.
7
40.
5
3
8
.1
35.
6
34
.0
32.
9
3
0
.6
28.
2
2
5
.7
23.
7
2
1
.8
20.
6
1
9
.8
17.
8
1
5
.8
13.
8
11.
7
9
.6
T
/R
3
3.
7
31.
9
3
0
.0
28.
1
2
6
.8
26.
0
2
4
.1
22.
2
2
0
.2
18.
7
1
7
.2
16.
2
1
5
.6
14.
0
1
2
.4
10.
8
9
.3
7.
6
K
W
2
.46
2.
40
2.
35
2.
29
2.
25
2.
23
2.
17
2.
1
1
2.
10
2.
0
4
1.
98
1.
9
4
1.
92
1.
8
6
1.
80
1.
7
4
1.
68
1.
6
2
A
M
P
S
1
3
.4
12.
3
1
1
.5
10.
7
1
0
.3
10.
1
9
.5
8
.9
8
.5
8
.1
7
.7
7.
4
7
.3
6.
9
6
.4
5.
9
5
.4
4.
8
C
O
P
4
.5
7
4
.4
2
4
.2
6
4
.0
7
3
.9
4
3
.8
6
3
.6
6
3
.4
6
3
.1
7
3
.0
0
2
.8
4
2
.7
2
2
.6
5
2
.4
4
2
.2
3
2
.0
0
1
.7
6
1
.4
8
G
oodm
an M
anu
fa
c
tur
in
g
C
o
m
pany
, L.
P
. r
e
s
e
rv
es
t
he r
igh
t t
o
d
is
c
o
n
tin
u
e
, or
c
hang
e a
t
any
t
im
e
,
s
pec
if
ic
at
ions
or
de
s
igns
w
it
h
o
u
t
no
itc
e
or
w
ith
out
in
c
u
rr
in
g
A
bov
e
in
fo
rm
a
tio
n i
s
f
o
r n
o
m
ina
l C
F
M
a
nd
70
degr
e
e
in
door
dr
y
b
u
lb
.
In
s
tant
an
eous
c
a
pac
it
y
Li
q
S
uc
t
L
iq
S
u
c
t
Li
q
S
uc
t
L
iq
S
u
c
t
Li
q
S
uc
t
L
iq
S
u
c
t
Li
q
S
u
c
t
L
iq
S
u
c
t
Li
q
S
uc
t
L
iq
S
u
ct
Li
q
S
uc
t
70
253
61
261
69
269
76
276
84
284
91
292
99
300
107
308
11
4
316
122
323
130
331
137
75
271
61
279
68
287
76
295
84
303
91
31
1
9
9
318
10
6
326
11
4
334
122
342
129
350
137
65
227
61
235
68
242
76
250
83
257
91
265
98
273
106
280
11
4
288
121
296
129
303
136
70
244
61
252
68
259
76
267
84
275
91
282
99
290
106
297
11
4
305
122
312
129
320
137
75
262
61
270
69
277
77
285
84
293
92
300
99
308
107
315
11
5
323
122
330
130
338
137
65
222
60
229
68
236
76
244
83
251
91
258
98
266
106
273
11
4
281
121
288
129
296
136
70
238
61
246
68
253
7
6
260
84
268
91
275
99
283
106
290
11
4
297
12
2
305
129
312
137
75
255
61
263
69
270
76
278
84
285
92
293
99
300
107
307
11
4
315
122
322
130
329
137
1090
1250
1410
17
27
Li
qui
d
V
a
lv
e
&
C
o
m
p
re
s
sor
S
u
c
ti
o
n
P
re
s
su
re
32
Indoor
Ai
r F
lo
w
Ra
te
37
HE
A
TI
N
G
M
O
D
E
42
47
57
67
In
door
R
e
tur
n
Ai
r D
ry
B
u
lb
Te
m
per
at
ure
(
°
F)
O
u
td
o
o
r
Ai
r Dr
y
Bu
lb
T
e
m
p
e
ra
tu
re
(
F)
P
res
s
u
re
s
s
how
n
a
re
fo
r m
o
s
t pop
ul
ar
m
a
tc
h
indo
or
uni
t
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
ct
or
s
li
ke
ai
rf
lo
w
, c
har
ge
, i
ndo
or
c
o
il
&
f
ros
t, p
res
s
u
re
s
w
ill
v
a
ry
s
igni
fi
c
antl
y
.
L
iqui
d (
s
m
a
ll)
s
e
rv
ic
e
v
a
lv
e pr
es
s
u
re
s
s
h
o
u
ld
b
e
±
2
0
ps
ig
&
s
u
c
tion (
a
c
c
es
s
po
rt
)
pre
s
s
u
re
s
s
h
o
u
ld
be ±
5
ps
ig
of
the v
a
lu
es
li
s
ted
in
t
h
is
c
har
t.
62
52
22
