Trane Gas Unit Heaters Installation Manual Page 17

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Installation: Piping
GKND-SVX01B-EN 17
Pipe Installation
1. Install the gas piping in accordance with applicable
local codes.
2. Check gas supply pressure. Each unit heater must be
connected to a gas supply capable of supplying its full
rated capacity as specified in Tab le 4, p. 18. A field LP
tank regulator must be used to limit the supply
pr
essure to maximum of 14 in. wc (3.5 kPa). All piping
should
be sized in accordance with the latest edition of
ANSI Standard Z223.1 National Fuel Gas Code; in
Canada, according to CAN/CanGa-CGAB149. See
Tab l e 1, p. 10, Ta b l e 3, p. 17, and Ta bl e 4, p. 18 for
correct gas supply piping size.
If gas pressure is excessive on natural gas applications,
install
a pressure regulating valve in the line upstream
from the main shutoff valve.
3. To prevent the mixing of moistur
e with gas, run the
take-off piping from the top, or side, of the main gas
pipe.
4. Optional two-stage units are supplied with a
com
bination valve which includes:
a. Manual “A” valve
b.
Manual “B” valve
c. Solenoid valve
d. Pilot safety
e. Pressure regulator
Table 3. Gas pipe size
(a)
Nominal
Iron Pipe
Size, in.
Internal
Diameter,
in. (mm)
Length of Pipe, ft (m)
10 20 30 40 50 60 70 80 90 100 125 150 175 200
(3.0) (6.1) (9.1) (12.2) (15.2) (18.3) (21.3) (24.4) (27.4) (30.5) (38.1) (45.7) (53.3) (61.0)
1/2 0.622 175 120 97 82 73 66 61 57 53 50 44 40 37 35
(16) (4.96) (3.40) (2.75) (2.32) (2.07) (1.87) (1.73) (1.61) (1.50) (1.42) (1.25) (1.13) (1.05) (0.99)
3/4 0.824 360 250 200 170 151 138 125 118 110 103 93 84 77 72
(21) (10.2) (7.08) (5.66) (4.81) (4.28) (3.91) (3.54) (3.34) (3.11) (2.92) (2.63) (2.38) (2.18) (2.04)
1 1.049 680 465 375 320 285 260 240 220 205 195 175 160 145 135
(27) (19.3) (13.2) (10.6) (9.06) (8.07) (7.36) (6.80) (6.23) (5.80) (5.52) (4.96) (4.53) (4.11) (3.82)
1-1/4 1.380 1400 950 770 660 580 530 490 460 430 400 360 325 300 280
(35) (39.6) (26.9) (21.8) (18.7) (16.4) (15.0) (13.9) (13.0) (12.2) (11.3) (10.2) (9.20) (8.50) (7.93)
1-1/2 1.610 2100 1460 1180 990 900 810 750 690 650 620 550 500 460 430
(41) (59.5) (41.3) (33.4) (28.0) (25.5) (22.9) (21.2) (19.5) (18.4) (17.6) (15.6) (14.2) (13.0) (12.2)
2 2.067 3950 2750 2200 1900 1680 1520 1400 1300 1220 1150 1020 950 850 800
(53) (112) (77.9) (62.3) (53.8) (47.6) (43.0) (39.6) (36.8) (34.5) (32.6) (28.9) (26.9) (24.1) (22.7)
2-1/2 2.469 6300 4350 3520 3000 2650 2400 2250 2050 1950 1850 1650 1500 1370 1280
(63) (178) (123) (99.7) (85.0) (75.0) (68.0) (63.7) (58.0) (55.2) (52.4) (46.7) (42.5) (38.8) (36.2)
3 3.068 11000 7700 6250 5300 4750 4300 3900 3700 3450 3250 2950 2650 2450 2280
(78) (311) (218) (177) (150) (135) (122) (110) (105) (97.7) (92.0) (83.5) (75.0) (69.4) (64.6)
4 4.026 23000 15800 12800 10900 9700 8800 8100 7500 7200 6700 6000 5500 5000 4600
(102) (651) (447) (362) (309) (275) (249) (229) (212) (204) (190) (170) (156) (142) (130)
Notes:
1. Determine the required ft
3
/h by dividing the rated heater input by 1000. For SI / Metric measurements: Convert unit Btu/h to kilowatts. Multiply the
unit input (kW) by 0.0965 to determine m
3
/h.
2. FOR NATURAL GAS: Select the pipe size directly from the table.
3. FOR PROPANE GAS: Multiply the ft
3
/h (m
3
/h) value by 0.633; then use the table.
4. Refer to the metric conversion factors listed in “General Safety Information,” p. 7 for more SI unit measurements/conversions.
(a)Maximum capacity of pipe in cubic feet of gas per hour (cubic meters per hour) for gas pressures of 0.5 psig (3.5 kPa) or less, and a pressure drop of
0.5 inch water column (124.4 Pa) (based on a 0.60 specific gravity gas).
WARNING
Hazard of Explosion!
Adequately support the piping to prevent strain on the
gas manifold and controls. To prevent explosion, fire, or
gas leaks, support piping so that piping does not sag or
put pressure on the burners internal to the unit. Failure
to follow these recommendations could result in death
or serious injury or equipment or property-only-
damage.
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