Trane IntelliPak SAHL Series, Инструкция по установке, эксплуатации и обслуживанию

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RT-SVX36G-EN 125
Unit Start Up
75
/8
9
1
2000
0.
28
0.3
8
.1
0
.08
0.
06
.1
0
.13
.0
6
.11
.0
5
.05
.01
.44
.3
7
.02
.0
7
0
.0
3
1
6000
0.
44
0.5
8
.1
8
.14
0.
11
.1
7
.21
.1
1
.19
.0
7
.07
.02
.63
.5
8
.05
.1
0
0
.0
6
2
0000
0.
63
0.8
2
.2
7
.21
0.
17
.2
4
.31
.1
6
.27
.1
0
.10
.03
.84
.8
2
.10
.1
6
0
.0
9
2
2000
0.
73
0.9
4
.3
3
.25
0.
2
.2
9
.37
.1
9
.3
3
.12
.12
.04
.95
.95
.13
.2
0
0
.1
1
2
4000
0.
84
1.0
7
.4
0
.30
0.
24
.3
3
.42
.2
2
.39
.1
4
.14
.04
1
.0
6 1.
08
.1
6
.2
3
0
.1
3
2
6000
0.
95
1.
2
.4
7
.32
0.
28
.3
9
.49
.2
7
.45
.16
.16
.05
1
.1
7 1.
23
.23
.2
6
0
.1
5
2
8000
1.
07
1.3
3
.5
4
.33
0.
32
.4
4
.55
.3
2
.50
.1
7
.17
.06
1
.2
2 1.
29
.3
0
.3
0
0
.1
7
3
1000
1.
27
1.5
4
.6
0
.40
0.
4
.4
9
.61
.3
9
.5
5
.21
.21
.07
-
-
.37
.3
6
0
.2
1
3
3000
1.
4
1
.6
8
.6
5
.4
6
0
.4
5
.5
2
.6
7
.4
4
.6
0
.24
.2
4
.08
-
-
.4
2
.4
0
0
.2
4
Not
es:
1.
St
ati
c p
res
sure
dro
p
s of ac
ces
so
ry co
mpo
n
en
ts
mu
st
be ad
de
d
to
e
xte
rna
l st
at
ic
p
ress
ure
to
en
te
r f
an
sel
ec
ti
on
ta
b
le
s.
2.
Gas h
eat
se
cti
o
n maxi
mum
te
mpe
ratu
re r
is
e o
f 60
F
.
3.
Throw
aw
ay filt
er
o
p
ti
on li
mited to 3
00 ft/mi
n
face
v
elo
ci
ty
.
4.
Bag
fi
lter opti
on
limit
ed to
740
ft/min fac
e v
el
o
cit
y.
5.
Ho
ri
zo
nt
al ro
o
f cur
b
s as
sume
0
.5
0
" st
at
ic
pres
su
re dr
op
or d
ou
b
le
t
h
e st
andard
ro
of c
u
rb
pres
sur
e dr
op
, w
h
ic
h
ev
er
is
great
er
.
6.
No
addi
ti
o
n
al
pre
ssu
re l
o
ss fo
r mo
de
l SXH
L.
T
a
ble 38.
Component static pr
essu
re
dr
op
s
(i
n. W
.G
.)
Nom (AC/ EC)
Cf
m
Std
Eva
p
orat
or C
o
il
He
at
ing S
yst
em
Filters
Std Ro
of
E
conom
izer
With o
r
Without Exhaust
Re
hea
t
Op
tion
Pre
ssure
Dr
op
Throwaway
Pe
rm
Wir
e
Ba
g a
n
d
Pref
ilter
Cartrid
g
e
and
Pre
filter
Dr
y
We
t
S
F
H
L
SE
HL
SLH
L
SSH
L
St
d.
H
igh
Low
H
ig
h
All kW
Low
H
ig
h
Low
Hig
h
T
a
ble 39.
Component static pr
essur
e
dr
op
s, 90-130 t
o
n (in
.
W
.G.
)
No
m
Cfm Std
Evap
orator Co
il
H
igh C
a
p Eva
p
He
at
ing
S
yste
m
Filters
Std Ro
of
Econ. w/ or w/
out
Exha
ust
T
hrowaway
Perm Wire
Ba
g
and
Pre
filter
Cartrid
g
e
and
P
refilter
Dr
y
Wet
Dr
y
Wet
SF
HL
SE
H
L
S
L
HL
S
S
H
L
St
d.
Hi
g
h
Low
H
ig
h
A
ll kW
Low
H
ig
h
L
ow
High
90
27
000
0.
40
0.
53
0.
60
0.
80
-
0
.2
5
0
.13
0
.2
6
0
.3
1
0
.22
0
.3
2
0
.1
1
0
.1
3
-
0.
68
0.
65
-
0
.2
32
000
0.
53
0.
70
0.
80
1.
03
-
0
.3
1
0
.16
0.
35
0
.4
1
0.
3
0.
43
0.
14
0.
16
-
0.
84
0.
84
-
0.
31
37
000
0.
67
0.
88
1.
01
1.
32
-
0
.3
9
0
.23
0.
45
0
.5
2
0.
4
0.
55
0.
17
0.
19
-
1.
02
1.
04
-
0.
41
42
000
0.
83
1.
08
1.
25
1.
62
-
0
.4
6
0
.29
0.
56
0
.6
5
0.
5
0.
68
0.
21
0.
22
-
1.
19
1.
06
-
0.
52
45
000
0.
93
1.
20
1.
40
1.
80
-
0
.5
2
0
.32
0
.6
3
0
.7
3
0
.58
0
.7
6
0
.2
4
0
.2
4
-
-
-
-
0
.6
3
10
5
31
000
-
-
0.
63
0.
83
-
0
.2
8
0
.17
0
.3
3
0
.3
9
0
.29
0
.4
-
0
.1
3
-
0.
82
0
.8
-
0.
22
35
000
-
-
0.
77
1.
01
-
0
.3
6
0
.21
0
.4
1
0
.4
8
0
.36
0
.5
-
0
.1
6
-
0.
96
0.
96
-
0
.3
2
39
000
-
-
0.
92
1.
20
-
0
.4
2
0
.26
0
.4
9
0
.5
7
0
.44
0
.6
-
0
.1
9
-
1.
09
1.
12
-
0
.4
4
43
000
-
-
1.
08
1.
40
-
0
.4
5
0.
3
0.
57
0
.6
6
0
.53
0.
71
-
0.
22
-
1.
22
1
.3
-
0.
54
46
000
1.
21
1.
56
-
0
.5
5
0
.34
0
.6
5
0
.7
5
0
.61
0
.7
9
-
0.
24
-
-
-
0
.6
4
115
/
13
0
31
000
0.
76
1.
00
-
-
-
0
.2
8
0
.17
0
.3
3
0
.3
9
0
.29
0
.4
-
0
.1
3
-
0.
82
0
.8
-
0.
22
35
000
0.
92
1.
21
-
-
-
0
.3
6
0
.21
0
.4
1
0
.4
8
0
.36
0
.5
-
0
.1
6
-
0.
96
0.
96
-
0
.3
2
39
000
1.
10
1.
44
-
-
-
0
.4
2
0
.26
0
.4
9
0
.5
7
0
.44
0
.6
-
0
.1
9
-
1.
09
1.
12
-
0
.4
4
43
000
1.
30
1.
68
-
-
-
0
.4
5
0.
3
0.
57
0
.6
6
0
.53
0.
71
-
0.
22
-
1.
22
1
.3
-
0.
54
46
000
1.
45
1.
86
-
-
-
0
.5
5
0
.34
0
.6
5
0
.7
5
0
.61
0
.7
9
-
0.
24
-
-
-
-
0.
64
Not
es:
1.
St
ati
c p
res
sure
dro
p
s of ac
ces
so
ry co
mpo
n
en
ts
mu
st
be ad
de
d
to
e
xte
rna
l st
at
ic
p
ress
ure
to
en
te
r f
an
sel
ec
ti
on
ta
b
le
s.
2.
Gas h
eat
se
cti
o
n maxi
mum
te
mpe
ratu
re r
is
e o
f 60
F
.
3.
Throw
aw
ay filt
er
o
p
ti
on li
mited to 3
00 ft/mi
n
face
v
elo
ci
ty
.
4.
Bag
fi
lter opti
on
limit
ed to
740
ft/min fac
e v
el
o
cit
y.
5.
Ho
ri
zo
nt
al ro
o
f cur
b
s as
sume
0
.5
0
" st
at
ic
pres
su
re dr
op
or d
ou
b
le
t
h
e st
andard
ro
of c
u
rb
pres
sur
e dr
op
, w
h
ic
h
ev
er
is
great
er
.
6.
No
addi
ti
o
n
al
pre
ssu
re l
o
ss fo
r mo
de
l SXH
F.