Amana ASZ 14 SEER, Техническое руководство

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33
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
iq
S
u
ct
Liq
S
u
c
t
L
iq
S
uc
t
L
iq
S
u
c
t
Liq
S
u
c
t
L
iq
S
uc
t
L
iq
S
u
c
t
Liq
S
u
c
t
L
iq
S
uc
t
L
iq
S
u
c
t
Liq
S
u
c
t
65
2
3
5
6
1
2
4
3
69
251
76
2
5
9
8
4
2
6
6
92
274
99
2
8
2
107
29
0
1
15
298
12
2
3
06
130
31
4
1
38
70
2
5
3
6
1
2
6
1
69
269
76
2
7
6
8
4
2
8
4
91
292
99
3
0
0
107
30
8
1
14
316
12
2
3
23
130
33
1
1
37
75
2
7
1
6
1
2
7
9
68
287
76
2
9
5
8
4
3
0
3
91
311
99
3
1
8
106
32
6
1
14
334
12
2
3
42
129
35
0
1
37
65
2
2
7
6
1
2
3
5
68
242
76
2
5
0
8
3
2
5
7
91
265
98
2
7
3
106
28
0
1
14
288
12
1
2
96
129
30
3
1
36
70
2
4
4
6
1
2
5
2
68
259
76
2
6
7
8
4
2
7
5
91
282
99
2
9
0
106
29
7
1
14
305
12
2
3
12
129
32
0
1
37
75
2
6
2
6
1
2
7
0
69
277
77
2
8
5
8
4
2
9
3
92
300
99
3
0
8
107
31
5
1
15
323
12
2
3
30
130
33
8
1
37
65
2
2
2
6
0
2
2
9
68
236
76
2
4
4
8
3
2
5
1
91
258
98
2
6
6
106
27
3
1
14
281
12
1
2
88
129
29
6
1
36
70
2
3
8
6
1
2
4
6
68
253
76
2
6
0
8
4
2
6
8
91
275
99
2
8
3
106
29
0
1
14
297
12
2
3
05
129
31
2
1
37
75
2
5
5
6
1
2
6
3
69
270
76
2
7
8
8
4
2
8
5
92
293
99
3
0
0
107
30
7
1
14
315
12
2
3
22
130
32
9
1
37
P
re
s
s
u
re
s
s
h
o
w
n
a
re f
o
r
m
o
s
t
popu
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
f
a
c
to
rs
l
ik
e
ai
rf
lo
w
, c
h
a
rge,
i
n
d
o
o
r c
o
il
&
f
ro
s
t,
pr
es
s
u
re
s
w
il
l
v
a
ry
s
ign
if
ic
an
tl
y
. Li
qui
d (
s
m
a
ll
) s
e
rv
ic
e
v
a
lv
e
pr
e
s
s
u
re
s
s
h
ou
ld
be
±
2
0
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
b
e
±
5
ps
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
do
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
mp
er
at
u
re
(
ºF
)
32
Indo
or
Ai
r F
lo
w
Ra
te
37
1
090
1
250
1
410
M
O
D
E
L
: A
S
Z
1
40
3
6
1
B
* /
A
R
*F
3
74
3
1
6B
*
H
E
A
T
IN
G OP
E
R
A
T
IO
N
O
u
td
oo
r Am
bi
e
n
t
T
e
m
p
e
ra
tu
re
6
5
6
0
5
5
50
4
7
4
5
4
0
35
30
25
2
0
17
15
1
0
5
0
-5
-1
0
M
B
h
41.
5
3
9
.3
3
7.
0
3
4.
6
33
.0
32
.0
2
9
.7
2
7
.4
2
4
.9
2
3
.0
2
1
.2
20.
0
1
9
.3
1
7.
3
15.
3
1
3
.4
1
1.
4
9
.3
D
e
lt
a T
30.
7
2
9
.1
2
7.
4
2
5.
6
2
4.
4
2
3
.7
2
2.
0
2
0.
3
1
8
.5
1
7.
0
1
5.
7
14.
8
1
4
.3
1
2.
8
11.
3
9
.9
8.
4
6
.9
K
W
2.
95
2.
90
2
.8
5
2
.79
2.
76
2.
74
2
.6
9
2
.64
2
.93
2
.8
6
2
.80
2.
76
2.
74
2
.6
8
2.
61
2.
55
2
.4
9
2
.4
3
A
M
P
S
11.
8
1
1
.0
1
0.
3
9
.8
9.
4
9
.3
8.
8
8
.4
8
.0
7
.7
7
.4
7
.2
7.
1
6
.8
6
.4
6
.1
5.
7
5
.2
C
O
P
4
.1
1
3
.9
6
3
.8
0
3
.6
2
3
.4
9
3
.4
1
3
.2
3
3
.0
4
2
.4
9
2
.3
5
2
.2
1
2
.1
2
2
.0
6
1
.8
9
1
.7
1
1
.5
3
1
.3
4
1
.1
3
E
E
R
14.
0
1
3
.5
1
3.
0
1
2.
4
1
1.
9
1
1
.7
1
1.
0
1
0.
4
8
.5
8
.0
7
.6
7
.2
7
.0
6.
5
5
.9
5.
2
4
.6
3
.8