Goodman Mfg VC8 User Manual

Page of 48
21
C
IRCULATING
 A
IR
 
AND
 F
ILTERS
P
ROPANE
 G
AS
 T
ANKS
 
AND
 P
IPING
I
F
 
THE
 
GAS
 
FURNACE
 
IS
 
INSTALLED
 
IN
 
A
 
BASEMENT
AN
 
EXCAVATED
 
AREA
 
OR
 
CONFINED
 
SPACE
IT
 
IS
 
STRONGLY
 
RECOMMENDED
 
TO
 
CONTACT
 
A
 
PROPANE
 
SUPPLIER
 
TO
 
INSTALL
 
A
 
GAS
 
DETECTING
 
WARNING
 
DEVICE
 
IN
 
CASE
 
OF
 
A
 
GAS
 
LEAK
.
S
INCE
 
PROPANE
 
GAS
 
IS
 
HEAVIER
 
THAN
 
AIR
ANY
 
LEAKING
 
GAS
 
CAN
   
SETTLE
 
IN
 
ANY
 
LOW
 
AREAS
 
OR
 
CONFINED
 
SPACES
.
P
ROPANE
 
GAS
 
ODORANT
 
MAY
 
FADE
MAKING
 
THE
 
GAS
 
UNDETECTABLE
   
EXCEPT
 
WITH
 
A
 
WARNING
 
DEVICE
.
• 
• 
WARNING
A gas detecting warning system is the only reliable way to
detect a propane gas leak. Rust can reduce the level of odorant
in propane gas.  Do not rely on your sense of smell.  Contact a
local propane gas supplier about installing a gas detecting
warning system.  If the presence of gas is suspected, follow
the instructions on Page 3 of this manual.
All propane gas equipment must conform to the safety stan-
dards of the National Board of Fire Underwriters, NBFU Manual
58.
For satisfactory operation, propane gas pressure must be 10
inch WC at the furnace manifold with all gas appliances in
operation. Maintaining proper gas pressure depends on three
main factors:
1. Vaporization rate, depending on temperature of the liquid,
and “wetted surface” area of the container or containers.
2. Proper pressure regulation. (Two-stage regulation is
recommended for both cost and efficiency).
3. Pressure drop in lines between regulators, and between
second stage regulator and the appliance. Pipe size will
depend on length of pipe run and total load of all
appliances.
Complete information regarding tank sizing for vaporization, rec-
ommended regulator settings, and pipe sizing is available from
most regulator manufacturers and propane gas suppliers.
Since propane gas will quickly dissolve white lead and most
standard commercial compounds, special pipe dope must be
used. Shellac-based compounds resistant to the actions of
liquefied petroleum gases such as Gasolac
®
, Stalactic
®
,
Clyde’s
®
 or John Crane
®
 are satisfactory.
Refer to the following illustration for typical propane gas instal-
lations and piping.
200 PSIG
Maximum
5 to 15 PSIG
(20 PSIG Max.)
Continuous
11" W.C.
Second Stage
Regulator
First Stage
Regulator
Propane Gas Installation (Typ.)
P
ROPANE
 G
AS
 P
IPING
 C
HARTS
3/8"
1/2"
5/8"
3/4"
7/8"
1/2"
3/4"
10
730
1,700
3,200
5,300
8,300
3,200
7,500
20
500
1,100
2,200
3,700
5,800
2,200
4,200
30
400
920
2,000
2,900
4,700
1,800
4,000
40
370
850
1,700
2,700
4,100
1,600
3,700
50
330
770
1,500
2,400
3,700
1,500
3,400
60
300
700
1,300
2,200
3,300
1,300
310
80
260
610
1,200
1,900
2,900
1,200
2,600
100
220
540
1,000
1,700
2,600
1,000
2,300
125
200
490
900
1,400
2,300
900
2,100
150
190
430
830
1,300
2,100
830
1,900
175
170
400
780
1,200
1,900
770
1,700
200
160
380
730
1,100
1,800
720
1,500
Sizing Between First and Second Stage Regulator*
Maximum Propane Capacities listed are based on 2 psig pressure drop at 10 psig setting.
Capacities in 1,000 BTU/hour.
Nominal Pipe Size
Schedule 40
Tubing Size, O.D. Type L
Pipe or
Tubing
Length,
Feet
3/8"
1/2"
5/8"
3/4"
7/8"
1-1/8"
1/2"
3/4"
1"
1-1/4" 1-1/2"
10
39
92
199
329
501
935
275
567
1,071 2,205 3,307
20
26
62
131
216
346
630
189
393
732
1,496 2,299
30
21
50
107
181
277
500
152
315
590
1,212 1,858
40
19
41
90
145
233
427
129
267
504
1,039 1,559
50
18
37
79
131
198
376
114
237
448
91
1,417
60
16
35
72
121
187
340
103
217
409
834
1,275
80
13
29
62
104
155
289
89
185
346
724
1,066
100
11
26
55
90
138
255
78
162
307
630
976
125
10
24
48
81
122
224
69
146
275
567
866
150
9
21
43
72
109
202
63
132
252
511
787
200
8
19
39
66
100
187
54
112
209
439
665
250
8
17
36
60
93
172
48
100
185
390
590
Pipe or
Tubing
Length,
Feet
Nominal Pipe Size
Schedule 40
Tubing Size, O.D. Type L
Sizing Between Second Stage and Appliance Regulator*
Maximum Propane Capacities listed are based on 2 psig pressure drop at 10 psig setting.
Capacities in 1,000 BTU/hour.
C
IRCULATING
 A
IR
 
AND
 F
ILTERS
N
EVER
 
ALLOW
 
THE
 
PRODUCTS
 
OF
 
COMBUSTION
INCLUDING
 
CARBON
 
MONOXIDE
TO
 
ENTER
 
THE
 
RETURN
 
DUCT
 
WORK
 
OR
 
CIRCULATION
 
AIR
 
SUPPLY
.
WARNING
Duct systems and register sizes must be properly designed for
the CFM and external static pressure rating of the furnace.
Ductwork should be designed in accordance with the recom-
mended methods of “Air Conditioning Contractors of America”
Manual D.
A duct system must be installed in accordance with Standards
of the National Board of Fire Underwriters for the Installation of
Air Conditioning, Warm Air Heating and Ventilating Systems.
Pamphlets No. 90A and 90B.