Amana ASZ 14 SEER, Техническое руководство

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37
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
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 &
C
o
m
p
re
sso
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
HE
A
T
IN
G
M
O
D
E
42
47
57
67
In
doo
r R
e
tu
rn
Ai
r D
ry
Bu
lb
T
e
m
p
er
a
tu
re
(º
F
)
17
2
7
P
re
s
s
u
re
s
s
h
o
w
n
a
re fo
r
m
o
s
t
p
o
p
u
la
r m
a
tc
h
i
n
do
o
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
fa
c
to
rs
l
ik
e
ai
rf
lo
w
, c
h
ar
g
e
, i
n
d
o
o
r c
o
il
&
fr
o
s
t,
p
re
s
s
u
re
s
w
il
l v
a
ry
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
hou
ld
be
±
2
0
ps
ig
&
s
u
c
tio
n
(
a
c
c
e
s
s
po
rt
) pr
es
s
u
re
s
s
h
o
u
ld
b
e
±
5
ps
ig
of
the
v
a
lu
e
s
l
is
te
d
i
n
th
is
c
h
ar
t.
62
52
22
M
O
D
E
L
: A
S
Z
1
4
0
6
0
1
A
* /
C
A
*F
4
8
6
0
*6
A
*+
T
X
V /
M
B
E
2
0
0
0
**
-1
H
EA
T
IN
G
O
PER
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
7
1
.66
7
.86
3
.85
9
.7
57
.0
55
.2
5
1
.3
47
.3
4
7
.9
4
4
.2
4
0
.7
38.
4
3
7
.0
3
3.
2
29.
4
2
5
.7
2
1.
9
1
7
.9
D
e
lt
a
T
3
5
.93
3
.93
2
.02
9
.9
2
8
.5
2
7
.62
5
.72
3
.7
2
4
.02
2
.1
2
0
.41
9
.21
8
.51
6
.61
4
.71
2
.81
1
.0
9
.0
K
W
4
.8
3
4.
74
4
.6
4
4.
5
4
4.
48
4.
44
4
.3
5
4.
2
5
4
.42
4
.3
2
4
.21
4.
15
4.
11
4
.0
0
3.
90
3.
80
3
.6
9
3.
59
A
M
PS
24
.7
2
2
.3
2
0
.4
1
8
.8
1
7
.9
17
.4
1
6
.0
14
.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
44
.1
94
.0
33
.8
5
3
.7
2
3
.6
43
.4
53
.2
6
3
.1
72
.9
9
2
.8
32
.7
12
.6
32
.4
32
.2
11
.9
81
.7
41
.4
6
E
E
R
1
4
.81
4
.31
3
.81
3
.1
1
2
.7
1
2
.41
1
.81
1
.1
1
0
.81
0
.2
9
.7
9
.3
9
.0
8
.3
7
.5
6
.8
5
.9
5
.0