Miscellaneous
Sheet Metal
Weights
| Hot
Rolled Steel |
| US ga. |
Thickness,
in. |
Wt.,
lb/ft2 |
| 26 |
0.0179 |
0.750 |
| 24 |
0.0239 |
1.000 |
| 22 |
0.0299 |
1.250 |
| 20 |
0.0359 |
1.500 |
| 18 |
0.0478 |
2.000 |
| 16 |
0.0596 |
2.500 |
| 14 |
0.0747 |
3.125 |
|
| Galvanized
Steel |
| US Ga. |
Thickness,
in. |
Wt.,
LB/ft2 |
| 26 |
0.022 |
0.906 |
| 24 |
0.028 |
1.156 |
| 22 |
0.034 |
1.406 |
| 20 |
0.040 |
1.658 |
| 18 |
0.052 |
2.156 |
| 16 |
0.064 |
2.656 |
| 14 |
0.080 |
3.281 |
|
| Aluminum
(35) |
| B&S
Ga. |
Thickness,
in. |
Wt.,
LB/ft2 |
| - - - |
- - - |
- - - |
| - - - |
- - - |
- - - |
| 24 |
0.020 |
0.288 |
| 22 |
0.025 |
0.355 |
| 20 |
0.032 |
0.456 |
| 18 |
0.040 |
0.575 |
| 16 |
0.051 |
0.724 |
| 14 |
0.064 |
0.914 |
|
| Stainless
Steel |
| US Ga. |
Thickness,
in. |
Wt.,
LB/ft2 |
| 28 |
0.016 |
0.66 |
| 26 |
0.019 |
0.79 |
| 24 |
0.025 |
1.05 |
| 22 |
0.031 |
1.31 |
| 20 |
0.038 |
1.58 |
| 18 |
0.050 |
2.10 |
| 16 |
0.063 |
2.63 |
| 14 |
0.078 |
3.28 |
|
Recommended Metal
Gauges for Ducts
| Rectangular
Duct |
Greatest
dimension |
U.S.
Ga. |
B&S
Ga. |
| to 30
in. |
24 |
22 |
| 31-61 |
22 |
20 |
| 61-90 |
20 |
18 |
| 91-up |
18 |
16 |
|
| Round
Duct |
| Diameter
|
Galv.
Steel
US Ga. |
Aluminum
B&S Ga. |
| to 8
in. |
24 |
22 |
| 9-24 |
22 |
20 |
| 25-48 |
20 |
18 |
| 49-72 |
18 |
16 |
|
Conventional duct
fabrication includes "S" clips on small sizes; bar slips or
standing seams on larger sizes. All panels over 18 in. (1 dim) are to
be cross broken.
Adapted from "Numbers",
Bill Holladay and Cy Otterhelm, 1985.
Fuel Comparisons**
This provides
equivalent BTU Data for Various Fuels
| Natural Gas |
1,000,000 BTU
= 10 Therms or |
|
1,000,000 BTU
= (1000 Cu. Ft.) |
| Propane Gas |
1,000,000 BTU
= 46 Lb. or |
|
1,000,000 BTU
= 10.88 Gallon |
| No. 2 Fuel
Oil |
1,000,000 BTU
= 7.14 Gallon |
| Electrical
Resistance |
1,000,000 BTU
= 293 KW (kilowatts) |
| Municipal Steam |
1,000,000 BTU
= 1000 Lbs. Condensate |
| Sewage Gas |
1,000,000 BTU
= 1538 Cu. Ft. to 2380 Cu. Ft. |
| LP/Air Gas |
1,000,000 BTU
= 46 Lb. Propane or |
|
1,000,000 BTU
= 10.88 Gallon Propane or |
|
1,000,000 BTU
= 690 Cu. Ft. Gas/Air Mix |
Fuel Gas Characteristics
| Natural Gas |
925 to 1125
BTU/Cu. Ft. |
.6 to .66 Specific
Gravity |
| Propane Gas |
2550 BTU/Cu.
Ft. |
1.522 Specific
Gravity |
| *Sewage Gas |
420 to 650
BTU/Cu. Ft. |
.55 to .85
Specific Gravity |
| *Coal Gas |
400 to 500
BTU/Cu. Ft. |
.5 to .6 Specific
Gravity |
| *LP/Air Mix |
1425 BTU/Cu.
Ft. |
1.29 Specific
Gravity |
Heat Loss Estimates
The following will
give quick estimates of heat requirements in a building knowing the
cu. ft. volume of the building and design conditions.
|
|
Indoor
Temp (F) - BTU/Cubic Foot |
|
|
Masonry
Wall |
Insulated
Steel Wall |
| Type of
Structure |
|
60 |
65 |
70 |
60 |
65 |
70 |
Single Story
4 Walls Exposed |
|
3.4 |
3.7 |
4.0 |
2.2 |
2.4 |
2.6 |
Single Story
One Heated Wall |
|
2.9 |
3.1 |
3.4 |
1.9 |
2.0 |
2.2 |
Single Floor
One Heated Wall
Heated Space Above |
|
1.9 |
2.0 |
2.2 |
1.3 |
1.4 |
1.5 |
Single Floor
Two Heated Walls
Heated Space Above |
|
1.4 |
1.5 |
1.6 |
0.9 |
1.0 |
1.1 |
Single Floor
Two Heated Walls |
|
2.4 |
2.6 |
2.8 |
1.6 |
1.7 |
1.8 |
| Multistory |
2
Story |
2.9 |
3.1 |
3.4 |
1.9 |
2.1 |
2.2 |
| 3 Story |
2.8 |
3.0 |
3.2 |
1.8 |
2.0 |
2.1 |
| 4
Story |
2.7 |
2.9 |
3.1 |
-
- - |
-
- - |
-
- - |
| 5 Story |
2.6 |
2.8 |
3.0 |
-
- - |
-
- - |
-
- - |
*Before attempting
to operate units on these fuels, contact mfr.
**Chemical Rubber Publishing Co., Handbook of Chemistry and Physics
Estimated Seasonal
Efficiencies of Heating Systems
| Systems |
Seasonal
Efficiency |
| Gas Fired Gravity
Vent Unit Heater |
62% |
| Energy Efficient
Unit Heater |
80% |
| Electric Resistance
Heating |
100% |
| Steam Boiler
with Steam Unit Heaters |
65%-80% |
| Hot Water Boiler
with HYD Unit Heaters |
65%-80% |
| Oil Fired Unit
Heaters |
78% |
| Municipal Steam
System |
66% |
| INFRA Red (High
Intensity) |
85% |
| INFRA Red (Low
Intensity) |
87% |
| Direct Fired
Gas Make Up Air |
94% |
| Improvement
with Power Venter Added to Gas Fired Gravity Vent Unit Heater |
4% |
| Improvement
with Spark Pilot Added to Gas Fired Gravity Vent Unit Heater |
1/2%-3% |
| Improvement
with Automatic Flue Damper and Spark Pilot Added to Gravity Vent
Unit Heater |
8% |
Annual Fuel Use
Annual fuel use
may be determined for a building by using one of the following formulas:
| Electric Hesitance
Heating |
H / ( T
x 3413 x E) x D x 24 x .79 = KWH/YEAR |
| Natural Gas
Heating |
H / ( T
x 100,000 x E) x D x 24 x .6 = THERMS/YEAR |
| Propane
Gas Heating |
H / ( T
x 21739 x E) x D x 24 x .6 = POUNDS/YEAR |
H / ( T
x 91911 x E) x D x 24 x .6 = GALLONS/YEAR |
| Oil Heating |
H / ( T
x 140,000 x E) x D x 24 x .6 = GALLONS/YEAR |
Where:
T = Indoor Design
Minus Outdoor Design
H = Building Heat Loss
D = Annual Degree Days
E = Seasonal Efficiency (See above)
|