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Carrier 48NLT - Install Venting; Install Gas Piping

Carrier 48NLT
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1"
MIN
Condensate
water
can
be
drained
directly
onto
the
roof
in
rooftop
installations
(where
permitted)
or
onto
a
gravel
apron
in
ground-level
installations.
When
using
a
gravel
apron,
make
sure
it
slopes
away
from
the
unit.
Stop
6
Install
Venting
--
The
vent
cap
assembly
is
shipped
in
the
burner
compartment.
Remove
the
access
door
to
locate
the
assembly.
A
CAUTION
The
venting
system
is
designed
to
ensure
proper
vent¬
ing.
The
vent
cap
assembly
must
be
installed
as
indi¬
cated
in
this
section
of
the
unit
Installation
Instructions.
NOTE:
Screw
holes
in
the
flue
assembly
and
the
unit
flue
panel
are
not
symmetrically
located.
Make
sure
they
are
oriented
properly
when
installing
these
components.
Refer
to
Fig.
6
and
install
the
vent
cap
as
follows:
1.
P
lace
vent
cap
assembly
over
flue
panel.
Orient
screw
holes
in
vent
cap
with
holes
in
flue
panel.
2.
Secure
vent
cap
in
place
by
inserting
the
single
screw
on
the
right
side
of
vent
cap.
3.
Place
the
vent
cap
guard
over
the
vent
cap.
Orient
holes
in
vent
cap
guard
with
holes
in
vent
cap
and
flue
panel.
4.
Secure
the
entire
assembly
with
the
remaining
2
screws
on
the
left
side
of
vent
cap
and
vent-cap
guard
assembly.
Step
7
Install
Gas
Piping
The
gas
supply
pipe
enters
the
unit
through
the
access
hole
provided.
The
gas
connection
to
the
unit
is
made
to
the
Vi-in.
FPT
gas
inlet
on
the
manual
shutoff
or
gas
valve.
Install
a
separate
gas
supply
line
that
runs
directly
from
the
meter
to
the
heating
section.
Refer
to
Table
2
and
the
National
Fuel
Gas
Code
(NFGC)
for
gas
pipe
sizing.
Do
not
use
cast-iron
pipe.
It
is
recommended
that
black
iron
pipe
is
used.
Check
the
local
utility
for
recommendations
concerning
existing
lines.
Choose
a
supply
pipe
that
is
large
enough
to
keep
the
pressure
loss
as
low
as
practical.
Never
use
pipe
smaller
than
the
V
2
-in.
FPT
gas
inlet
on
the
unit
gas
valve.
For
natural
gas
applications,
the
gas
pressure
at
unit
gas
connection
must
not
be
less
than
5
in.
wg
or
greater
than
13
in.
wg
while
the
unit
is
operating.
For
propane
applica¬
tions,
the
gas
pressure
must
not
be
less
than
11
in.
wg
or
greater
than
13
in.
wg
at
the
unit
connection.
When
installing
the
gas
supply
line,
observe
local
codes
pertaining
to
gas
pipe
installations.
Refer
to
the
NFGC
ANSI
(American
National
Standards
Institute)
Z223.1-1988
NFPA
(National
Fire
Protection
Association)
54-1988
(in
Canada,
CAN/CGA
[Canadian
Gas
Association]
B
149.1,
(2)-M86).
In
the
absence
of
local
building
codes,
adhere
to
the
fol¬
lowing
pertinent
recommendations:
1.
Avoid
low
spots
in
long
runs
of
pipe.
Grade
all
pipe
14
inch
in
every
15
ft
to
prevent
traps.
Grade
all
hori¬
zontal
runs
downward
to
risers.
Use
risers
to
connect
to
heating
section
and
to
meter.
2.
Protect
all
segments
of
piping
system
against
physical
and
thermal
damage.
Support
all
piping
with
appropri¬
ate
straps,
hangers,
etc.
Use
a
minimum
of
one
hanger
every
6
ft.
For
pipe
sizes
larger
than
14
in.,
follow
rec¬
ommendations
of
national
codes,
3.
Apply
joint
compound
(pipe
dope)
sparingly
and
only
to
male
threads
of
joint
when
making
pipe
connections.
Use
only
pipe
dope
that
is
resistant
to
action
of
liquefied
petroleum
gases
as
specified
by
local
and/or
national
codes.
Never
use
Teflon
tape.
4.
Install
sediment
trap
in
riser
leading
to
heating
section.
This
drip
leg
functions
as
a
trap
for
dirt
and
condensate.
Install
trap
where
condensate
cannot
freeze.
Install
this
sediment
trap
by
connecting
a
piping
tee
to
riser
leading
to
heating
section,
so
that
straight-through
section
of
tee
is
vertical.
See
Fig.
7.
Then,
connect
capped
nipple
into
lower
end
of
tee.
Extend
capped
nipple
below
level
of
gas
controls.
Table
2
-
Maximum
Gas
Glow
Capacity*
NOMINAL
IRON
PIPE,
SIZE
(in.)
INTERNAL
DIAMETER
(In.)
LENGTH
OF
PIPE,
FTf
10
20
30
40
50
60
70
so
90
100
125
ISO
175
200
Vz
.622
120
97
82
73
66
61
57
E^l
Eai
44
40
%
.824
360
250
200
WiM
Ea
IBM
warn
Ea
84
77
72
1
1.049
680
465
375
mmm
Esa
mm
Ea
mm
135
VU
I
1.380
1400
950
770
Ea
msm
mm
EM
ivi
I
1.610
-1
2100
1460
1180
990
900
810
750
690
650
620
550
500
460
1
I
430
‘Capacity
of
pipe
in
cu
ft
of
gas
per
hr
for
gas
pressure
of
0
5
psig
or
less.
Pressure
drop
of
0.5
in.
wg
(based
on
a
0.60
specific
gravity
gas)
Refer
to
Table
C-4,
NFPA
54-1984
jThis
length
includes
an
ordinary
number
of
fittings
6

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