Goodman SSZ 14 SEER, Technical Manual, Page: 33 / 39

33
SPLIT SYSTEM HEATING PERFORMANCE
EXP
ANDED PERFORMANCE DA
T
A
H
igh
pr
e
s
su
re
i
s
m
e
as
u
red
at
t
h
e
s
u
c
ti
o
n
s
e
rv
ic
e
v
a
lv
e
(
t
h
e
l
a
rg
e
r
v
a
lv
e)
.
Lo
w
p
re
ss
u
re
i
s
m
e
as
u
re
d
at
t
h
e
g
a
u
ge p
o
rt
c
o
n
nec
ti
on
.
C
a
lc
u
la
tio
ns
ar
e
b
a
s
e
d
on
n
o
m
in
a
l C
F
M
a
n
d
70
°
F
i
ndo
or
d
ry
b
u
lb
.
A
M
P
S
=
O
u
td
o
o
r
un
it
am
p
s
(
c
o
m
p
.+
fa
n
)
K
W
=
T
o
ta
l s
y
ste
m
p
o
w
e
r
M
O
D
E
L
: S
S
Z
1
406
0
1
A
*
/ C
A
*F
48
60*
6A
*+
T
X
V
/
M
B
R
2000
**
-1
H
E
A
T
IN
G
O
P
E
R
A
T
IO
N
O
u
td
oo
r A
m
bi
e
n
t
T
e
m
p
e
ra
tur
e
65
60
5
5
50
4
7
45
4
0
3
5
3
0
25
2
0
17
15
1
0
5
0
-5
-1
0
M
B
h
7
1
.66
7
.86
3
.85
9
.7
57
.0
55
.2
5
1
.3
4
7
.3
4
7
.9
4
4
.2
4
0
.7
38.
4
3
7
.0
3
3
.2
2
9.
4
2
5
.7
2
1.
9
17.
9
D
E
LT
A
T
35.
9
3
3
.9
3
2
.0
2
9
.9
2
8
.5
2
7
.6
2
5.
7
2
3.
7
2
4
.0
2
2.
1
2
0.
4
19.
2
1
8
.5
1
6
.6
1
4.
7
1
2
.8
1
1.
0
9
.0
K
W
4.
83
4.
74
4
.6
4
4.
5
4
4.
4
8
4.
44
4
.3
5
4
.25
4
.42
4
.3
2
4
.21
4.
15
4.
11
4
.0
0
3
.9
0
3
.8
0
3
.6
9
3.
59
A
M
PS
24.
7
2
2
.3
2
0
.4
1
8
.8
1
7
.9
1
7
.4
1
6.
0
1
4.
8
1
3
.9
1
2.
9
1
2.
0
11.
5
1
1
.3
1
0
.4
9
.2
8.
2
7
.1
5
.7
C
O
P
4
.3
4
4
.1
9
4
.0
3
3
.8
5
3
.7
2
3
.6
4
3
.4
5
3
.2
6
3
.1
7
2
.9
9
2
.8
3
2
.7
1
2
.6
3
2
.4
3
2
.2
1
1
.9
8
1
.7
4
1
.4
6
E
E
R
14.
8
1
4
.3
1
3
.8
1
3
.1
1
2
.7
1
2
.4
1
1.
8
1
1.
1
1
0
.8
1
0.
2
9
.7
9
.3
9
.0
8.
3
7
.5
6.
8
5
.9
5
.0
L
iqS
u
ct
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
L
iq
S
u
c
t
L
iqS
u
c
t
L
iq
S
u
c
t
L
iqS
u
c
t
65
2
6
0
5
8
2
7
5
65
290
72
3
0
5
8
0
3
2
1
87
336
94
3
5
1
102
36
6
1
09
381
11
7
3
97
124
41
2
1
31
70
2
8
0
5
7
2
9
5
65
311
72
3
2
6
7
9
3
4
2
87
357
94
3
7
3
101
38
8
1
09
404
11
6
4
19
124
43
5
1
31
75
3
0
0
5
7
3
1
6
65
332
72
3
4
8
7
9
3
6
4
86
380
94
3
9
6
101
41
2
1
08
428
11
6
4
43
123
45
9
1
31
65
2
5
2
5
7
2
6
6
64
281
72
2
9
5
7
9
3
1
0
86
324
94
3
3
9
101
35
4
1
08
369
11
5
3
83
123
39
8
1
30
70
2
7
0
5
7
2
8
5
65
300
72
3
1
5
7
9
3
3
0
87
345
94
3
6
0
101
37
5
1
09
390
11
6
4
05
123
42
0
1
30
75
2
9
0
5
8
3
0
5
65
321
72
3
3
6
8
0
3
5
2
87
367
94
3
8
3
102
39
8
1
09
413
11
6
4
28
124
44
4
1
31
65
2
4
5
5
7
2
5
9
64
274
72
2
8
8
7
9
3
0
2
86
316
93
3
3
1
101
34
5
1
08
359
11
5
3
74
123
38
8
1
30
70
2
6
35
72
7
8
6
5
29
3
7
2
3
0
77
93
2
2
8
7
33
7
94
3
5
1
101
36
6
1
08
38
0
11
6
3
95
12
3
41
0
1
30
75
2
8
2
5
8
2
9
8
65
313
72
3
2
8
8
0
3
4
3
87
358
94
3
7
3
102
38
8
1
09
403
11
6
4
18
124
43
2
1
31
1
580
1
800
2
030
L
iq
u
id
V
a
lv
e &
Co
m
p
resso
r
S
u
ct
io
n
P
ress
u
re
O
u
td
o
o
r
A
ir
Dr
y Bu
lb
T
e
m
p
erat
u
re
(
ºF
)
32
Indo
or
Ai
r F
lo
w
Rat
e
37
HE
AT
IN
G
M
O
DE
42
47
57
67
In
d
o
o
r R
e
tu
rn
Ai
r D
ry
Bu
lb
T
e
m
per
a
tu
re
(º
F
)
17
2
7
P
re
s
s
u
re
s
s
h
ow
n
a
re
f
o
r
m
o
s
t
p
o
p
ul
ar
m
a
tc
h
in
d
o
or
un
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
tor
s
l
ik
e
a
ir
fl
o
w
,
c
h
a
rg
e
,
in
d
o
o
r co
il
&
f
ro
s
t,
p
re
s
su
re
s
w
il
l va
ry
s
ign
if
ic
ant
ly
. Li
qui
d (
s
m
a
ll
)
s
e
rv
ic
e v
a
lv
e
pr
es
s
u
re
s
s
h
ou
ld
b
e
±
2
0
p
s
ig
&
s
u
c
ti
o
n
(
a
c
c
e
s
s
p
o
rt
) pr
es
s
u
re
s
s
h
o
u
ld
be
±
5
ps
ig
of
t
h
e
v
a
lu
es
l
is
te
d i
n
t
h
is
c
h
ar
t.
62
52
22