Installation Codes - A.O. Smith Burkay HW-300 Installation Operation & Maintenance

IT IS IMPORTANT TO GUARD AGAINST GAS VALVE FOULING FROM
CONTAMINANTS IN THE GAS WAYS. SUCH FOULING MAY CAUSE
IMPROPER OPERATION, FIRE OR EXPLOSION.
IF COPPER SUPPLY LINES ARE USED THEY MUST BE
CERTIFIED FOR GAS SERVICE.
BEFORE ATTACHING THE GAS LINE BE SURE THAT ALL GAS
PIPE IS CLEAN ON THE INSIDE.
TO TRAP ANY DIRT OR FOREIGN MATERIAL IN THE GAS SUPPLY
LINE, A DIRT LEG (SOMETIMES CALLED DRIP LEG or sediment
trap) MUST BE INCORPORATED IN THE PIPING, SEE FIG. 1. The
dirt leg must be readily accessible and not subject to freezing
conditions. INSTALL
RECOMMENDATIONS OF SERVING GAS SUPPLIERS. (Refer to
National Fuel Gas
CAN/CSA-B 149.1-00 Installation Codes.
To prevent damage, care must be taken not to apply too much
torque when attaching gas supply pipe to gas valve gas inlet.
Fittings and unions in the gas line must be metal to metal type.
Apply joint compounds (pipe dope) sparingly and only to the male
threads of pipe joints. Do not apply compound to the first two
threads. Use compounds resistant to the action of liquefied
petroleum gases.
THE BOILER AND ITS GAS CONNECTIONS MUST BE LEAK
TESTED BEFORE PLACING THE BOILER IN OPERATION. Use
soap and water solution or other material acceptable for the
purpose in locating gas leaks. DO NOT USE MATCHES, CANDLES,
FLAME OR OTHER SOURCES OF IGNITION FOR THIS PURPOSE.
DISCONNECT THE BOILER AND ITS MAIN MANUAL GAS
SHUTOFF VALVE FROM THE GAS SUPPLY PIPING SYSTEM
DURING ANY PRESSURE TESTING OF THE GAS SUPPLY
SYSTEM OVER 1/2 PSIG (3.5kPa).. THE GAS SUPPLY LINE MUST
BE CAPPED WHEN NOT CONNECTED TO THE BOILER.
THE BOILER MUST BE ISOLATED FROM THE GAS SUPPLY
PIPING SYSTEM BY CLOSING ITS MAIN MANUAL GAS SHUTOFF
VALVE DURING ANY PRESSURE TESTING OF THE GAS SUPPLY
PIPING SYSTEM AT TEST PRESSURES EQUAL TO OR LESS
THAN 1/2 PSIG (3.5kPa).
PURGING
Gas line purging is required with new piping or systems in which
air has entered.
PURGING SHOULD BE PERFORMED BY PERSONS
EXPERIENCED IN THIS TYPE GAS SERVICE TO AVOID RISK OF
FIRE OR EXPLOSION. PURGE DISCHARGE MUST NOT ENTER
CONFINED AREAS OR SPACES WHERE IGNITION CAN OCCUR.
THE AREA MUST BE WELL VENTILATED AND ALL SOURCES OF
IGNITION MUST BE INACTIVATED OR REMOVED.
1. CORRECT GAS
Make sure the gas on which the boiler will operate is the same as
that specified on the boiler rating plate. Do not install the boiler if
equipped for a different type gas — consult your supplier.
IN ACCORDANCE
Code, ANSI Z223.1
CAUTION
2A. SIZING GAS SUPPLY LINE (For single boiler installations and
for installations of multiples of two or three of same size boilers).
Use table 6, or CAN/CSA B149.1-00 (latest recent edition) to size
iron pipe or equivalent gas supply line. Table 6 is based on a
pressure drop of 0.3 inches of water and a specific gravity of 0.60
approximately that of natural gas. (LP gas has an S.G. of about
1.53). If the service pressure is five inches water column or less,
use one pipe size larger than specified in table 6 in order to minimize
pressure drop in the line.
MAXIMUM CAPACITY OF PIPE IN CUBIC FEET OF GAS PER
HOUR (BASED UPON A PRESSURE DROP OF 0.3 INCH WATER
COLUMN AND 0.6 SPECIFIC GRAVITY GAS)
WITH
Length
and/or
M e t e r s
From Gas
M e t e r 1/2 3/4
3 (10) 132 278 520 1,050 1,600 3,050 4,800 8,500 17,500
6 (20) 92 190 350
9 (30) 73 152 285
12 (40) 63 130 245
15 (50) 56 115 215
18 ((60) 50 105 195
21 (70) 46 96
24 (80) 43 90
27 (90) 40 84
30 (100) 38 79
38 (125) 34 72
45 (150) 31 64
53 (175) 28 59
60 (200) 26 55
*The heating value of Natural Gas is approximately 1,050 Btu/Ft
Propane (LP) Gas has a heating value of approximately 2,500 Btu/Ft
1 cu. meter=35.31 cu. feet.
Where it is necessary to use more than the average number of
pipe fittings i.e. elbows, tees, and valves in gas supply line, use a
pipe larger than specified to compensate for increased pressure
drop.
2B. SIZING GAS SUPPLY LINE (For multiples of over three boilers
of same size or for multiple installations of two or more mixed
sizes).
Capacities in cubic feet per hour of 0.60 specific gravity gas for
different sizes and lengths are shown in table 6. No additional
allowance is necessary for an ordinary number of fittings.
Applications of the gravity factor converts the figures given in table
6 to capacities with another gas of different specific gravity. Such
application is accomplished by multiplying the capacities given in
table 6 by the multipliers shown in table 7.
To determine the size of each section of gas piping in a system
within the range of table 6 proceed as follows:
•
Determine the gas demand of each appliance to be attached
to the piping system. When table 6 is to be used to select the
piping size, calculate the gas demand in terms of cubic feet per
hour for each piping system outlet. The gas demand for an
appliance can be found by dividing its heat input rate by the
gas's heating value.
• Obtain or determine the length of piping from the gas meter or
service regulator to the appliance(s).
10 10 10 10 10
TABLE 6
(Nominal Iron Pipe Size (Inches)
1 1 1/4 1 1/2 2 2 1/2
730 1,100 2,100 3,300 5,900 12,000
590 890 1,650 2,700 4,700
500 760 1,450 2,300 4,100
440 670 1,270 2,000 3,600
400 610 1,150 1,850 3,250
180 370 560 1,050 1,700 3,000
170 350 530 990 1,600 2,800
160 320 490 930 1,500 2,600
150 305 460 870 1,400 2,500
130 275 410 780 1,250 2,200
120 250 380 710 1,130 2,000
110 225 350 650 1,050 1,850
100 210 320 610 980 1,700
3 4
9,700
8,300
7,400
6,800
6,200
5,800
5,400
5,100
4,500
4,100
3,800
3,500
.3 .
3 .