|
The
following definitions, conversion factors, tables, and other information
for and about propane, butane and propane/butane mixtures are compiled
from commonly available sources and are reproduced for convenience only.
While we exercised great caution during the compilation, we can not
guarantee accuracy and urge everybody to verify the correctness of the
data before using them. Also, we appreciate if you alert us of any errors
you find.
|
| Page
Index |
|
| Definitions |
|
|
|
|
| Miscellaneous
Tables |
|
|
|
|
|
Standby
Plant Sizing Chart |
Cost
Savings through Standby Plants |
|
THEORETICAL
COMPATIBLE PROPANE/AIR MIXTURES |
|
The table below shows
Propane/Air mixtures, compatible with natural gas with several different
specific gravities and calorofic values.
All figures are approximate and are given for Propane with specific
gravity of 1.53 and calorific value of 2516 BTU/cuft.
|
|
Natural Gas |
Propane / Air Mixture |
|
SGU |
BTU/cuft |
% LPG |
% Air |
SGU |
BTU/cuft |
|
0.56 |
800 |
47.54 |
52.46 |
1.252 |
1196 |
|
850 |
50.87 |
49.13 |
1.270 |
1280 |
|
900 |
54.24 |
45.76 |
1.287 |
1365 |
|
950 |
57.65 |
42.35 |
1.306 |
1450 |
|
1000 |
61.11 |
38.89 |
1.324 |
1538 |
|
1050 |
64.62 |
35.38 |
1.342 |
1626 |
|
1100 |
68.16 |
31.84 |
1.361 |
1715 |
|
1150 |
71.76 |
28.24 |
1.380 |
1805 |
|
1200 |
75.40 |
24.60 |
1.400 |
1897 |
|
0.58 |
800 |
46.62 |
53.38 |
1.247 |
1173 |
|
850 |
49.88 |
50.12 |
1.264 |
1254 |
|
900 |
53.18 |
46.82 |
1.282 |
1338 |
|
950 |
56.52 |
43.48 |
1.300 |
1422 |
|
1000 |
59.90 |
40.10 |
1.317 |
1507 |
|
1050 |
63.33 |
36.67 |
1.336 |
1593 |
|
1100 |
66.80 |
33.20 |
1.354 |
1681 |
|
1150 |
70.32 |
29.68 |
1.373 |
1769 |
|
1200 |
73.88 |
26.12 |
1.392 |
1859 |
|
0.60 |
800 |
45.76 |
54.24 |
1.243 |
1151 |
|
850 |
48.95 |
51.05 |
1.259 |
1232 |
|
900 |
52.18 |
47.82 |
1.276 |
1313 |
|
950 |
55.45 |
44.55 |
1.294 |
1395 |
|
1000 |
58.76 |
41.24 |
1.311 |
1478 |
|
1050 |
62.12 |
37.88 |
1.329 |
1563 |
|
1100 |
65.51 |
34.49 |
1.347 |
1648 |
|
1150 |
68.95 |
31.05 |
1.365 |
1735 |
|
1200 |
72.43 |
27.57 |
1.384 |
1822 |
|
|
|
Natural Gas |
Propane / Air Mixture |
|
SGU |
BTU/cuft |
% LPG |
% Air |
SGU |
BTU/cuft |
|
0.62 |
800 |
44.93 |
55.07 |
1.238 |
1130 |
|
850 |
48.06 |
51.94 |
1.255 |
1209 |
|
900 |
51.23 |
48.77 |
1.272 |
1289 |
|
950 |
54.43 |
45.57 |
1.288 |
1369 |
|
1000 |
57.68 |
42.32 |
1.306 |
1451 |
|
1050 |
60.97 |
39.03 |
1.323 |
1534 |
|
1100 |
64.29 |
35.71 |
1.341 |
1618 |
|
1150 |
67.66 |
32.34 |
1.359 |
1702 |
|
1200 |
71.07 |
28.93 |
1.377 |
1788 |
|
0.64 |
800 |
44.15 |
55.85 |
1.234 |
1111 |
|
850 |
47.22 |
52.78 |
1.250 |
1188 |
|
900 |
50.32 |
49.68 |
1.267 |
1266 |
|
950 |
53.47 |
46.53 |
1.283 |
1345 |
|
1000 |
56.65 |
43.35 |
1.300 |
1425 |
|
1050 |
59.87 |
40.13 |
1.317 |
1506 |
|
1100 |
63.13 |
36.87 |
1.335 |
1588 |
|
1150 |
66.44 |
33.56 |
1.352 |
1672 |
|
1200 |
69.78 |
30.22 |
1.370 |
1756 |
|
0.66 |
800 |
43.41 |
56.59 |
1.230 |
1092 |
|
850 |
46.42 |
53.58 |
1.246 |
1168 |
|
900 |
49.47 |
50.53 |
1.262 |
1245 |
|
950 |
52.55 |
47.45 |
1.262 |
1322 |
|
1000 |
55.68 |
44.32 |
1.295 |
1401 |
|
1050 |
58.84 |
41.16 |
1.312 |
1480 |
|
1100 |
62.04 |
37.96 |
1.329 |
1561 |
|
1150 |
65.27 |
34.73 |
1.346 |
1642 |
|
1200 |
68.55 |
31.45 |
1.363 |
1725 |
|
|
Properties of |
Natural Gas |
Propane |
Butane |
|
Chemical formula |
|
CH4 |
C3H8 |
C4H10 |
|
Boiling point of liquid at atmospheric pressure |
°F |
-258.7 |
-44 |
32 |
|
Specific Gravity of vapor (Air = 1) |
|
0.6 |
1.53 |
2.00 |
|
Specific Gravity of liquid (Water = 1) |
|
0.6 |
0.51 |
0.58 |
|
Calorific value @ 60 °F |
BTU/cuft |
1012 |
2516 |
3280 |
|
BTU/gal |
|
91,690 |
102,032 |
|
BTU/lb |
|
21,591 |
21,221 |
|
Latent heat of vaporization |
BTU/gal |
712 |
785.0 |
808.0 |
|
Liquid weight |
lbs/gal |
2.5 |
4.24 |
4.81 |
|
Vapor volume from 1 gallon of liquid at 60 °F |
cuft |
|
36.39 |
31.26 |
|
Vapor volume from 1 lb. of liquid at 60 °F |
cuft |
|
8.547 |
6.506 |
|
Combustible limits |
% of gas in air |
5 - 15 |
2.4 - 9.6 |
1.9 - 8.6 |
|
Amount of air required to burn 1 cuft. of gas |
cuft |
9.53 |
23.86 |
31.02 |
|
Ignition temperature in air |
°F |
1200 |
920 - 1020 |
900 - 1000 |
|
Maximum flame temperature in air |
°F |
3568 |
3595 |
3615 |
|
Octane Number |
|
100 |
Over 100 |
92 |
|
All data is approximate. For actual properties of
any particular batch, contact your fuel supplier. |
|
Approximate
Vapor Pressure in psig |
|
Temperature |
Propane
----> To
----> Butane |
|
° F |
° C |
100% |
95/5* |
80/20 |
60/40 |
50/50 |
40/60 |
20/80 |
100% |
|
-40 |
-40.0 |
3.6 |
1.3 |
|
|
|
|
|
|
|
-30 |
-34.4 |
8 |
5.5 |
4.5 |
|
|
|
|
|
|
-20 |
-28.9 |
14 |
11 |
9.2 |
4.9 |
1.9 |
|
|
|
|
-10 |
-23.3 |
20 |
17 |
16 |
9 |
6 |
3.5 |
|
|
|
0 |
-17.8 |
28 |
24 |
22 |
15 |
11 |
7.3 |
|
|
|
10 |
-12.2 |
37 |
32 |
29 |
20 |
17 |
13 |
3.4 |
|
|
20 |
-6.7 |
47 |
41 |
36 |
28 |
23 |
18 |
7.4 |
|
|
30 |
-1.1 |
58 |
52 |
45 |
35 |
29 |
24 |
13 |
|
|
40 |
4.4 |
72 |
63 |
58 |
44 |
37 |
32 |
18 |
3 |
|
50 |
10.0 |
86 |
77 |
69 |
53 |
46 |
40 |
24 |
6.9 |
|
60 |
15.6 |
102 |
93 |
80 |
65 |
56 |
49 |
30 |
12 |
|
70 |
21.1 |
127 |
109 |
95 |
78 |
68 |
59 |
38 |
17 |
|
80 |
26.7 |
140 |
128 |
125 |
90 |
80 |
70 |
46 |
23 |
|
90 |
32.2 |
165 |
149 |
140 |
112 |
95 |
82 |
56 |
29 |
|
100 |
37.8 |
196 |
172 |
168 |
137 |
123 |
100 |
69 |
36 |
|
110 |
43.3 |
220 |
197 |
185 |
165 |
148 |
130 |
80 |
45 |
|
* HD5, Commercial Grade Propane |
|
|
|
Temperature
Conversion Table |
|
°F |
°C |
|
- 50 |
- 45.6 |
|
- 40 |
- 40.0 |
|
- 30 |
- 34.1 |
|
- 20 |
- 28.9 |
|
- 10 |
- 23.3 |
|
0 |
- 17.8 |
|
+ 10 |
- 12.2 |
|
20 |
- 6.7 |
|
30 |
- 1.1 |
|
32 |
0 |
|
40 |
+ 4.4 |
|
50 |
10.0 |
|
60 |
15.6 |
|
70 |
21.1 |
|
80 |
26.7 |
|
90 |
32.2 |
|
100 |
37.8 |
|
110 |
43.3 |
|
120 |
48.9 |
|
130 |
54.4 |
|
140 |
60.0 |
|
150 |
65.6 |
|
160 |
71.1 |
|
170 |
76.7 |
|
180 |
82.2 |
|
190 |
87.8 |
|
200 |
93.3 |
|
212 |
100 |
Formula:
Degrees C = (°F - 32) x 5/9
Degrees F = 9/5 x °C +
32
|
|
|
BTU
content of common fuels |
|
|
Per Pound |
Per Gallon |
|
Propane |
21,591 |
91,690 |
|
Butane |
21,221 |
102,032 |
|
Gasoline |
20,930 |
110,250 |
|
Fuel Oil #1 |
16,960 |
135,425 |
|
Diesel |
18,500 |
142,800 |
|
|
|
Butane
Equivalents |
|
Unit |
BTU |
Pound |
Therm |
Decitherm |
Cuft. |
Gallon |
|
1 Pound = |
21,221 |
1 |
0.212 |
2.12 |
6.50 |
0.208 |
|
1 Therm = |
100,000 |
4.714 |
1 |
10 |
30.64 |
0.98 |
|
1 Decitherm = |
10,000 |
0.4714 |
0.1 |
1 |
3.06 |
0.098 |
|
1 Cuft. = |
3,280 |
0.1537 |
0.032 |
0.32 |
1 |
0.03199 |
|
1 Gallon = |
102,032 |
4.81 |
1.02 |
10.20 |
31.26 |
1 |
|
| |
|
|
|
General
Information |
|
1 Lb. Steam |
970 BTU |
|
1 Boiler HP (per hr) |
33,475 BTU |
|
1 Kilowatt Hour |
3,412 BTU |
|
1 Gallon, Water |
8.337 lbs |
|
1 Cubic Foot, Water |
7.481 gallons |
|
1 Cubic Foot |
1,728 cubic inches |
|
1 Gallon |
231 cubic inches |
|
|
|
Propane
Equivalents |
|
Unit |
BTU |
Pound |
Therm |
Decitherm |
Cuft. |
Gallon |
|
1 Pound = |
21,591 |
1 |
0.216 |
2.16 |
8.58 |
0.239 |
|
1 Therm = |
100,000 |
4.622 |
1 |
10 |
39.7 |
1.10 |
|
1 Decitherm = |
10,000 |
0.4622 |
0.1 |
1 |
3.97 |
0.110 |
|
1 Cuft. = |
2,516 |
0.1164 |
0.025 |
0.25 |
1 |
0.027 |
|
1 Gallon = |
91,690 |
4.24 |
0.917 |
9.17 |
36.39 |
1 |
|
|
Specific
Gravity and Heat Content by Volume of LP Gas-Air Mixtures
|
|
Propane - Air Mixtures |
|
% Propane |
%
Air |
Specific
Gravity |
Gross BTU/cuft |
|
100 |
0 |
1.530 |
2516 |
|
95 |
5 |
1.504 |
2390 |
|
90 |
10 |
1.477 |
2264 |
|
85 |
15 |
1.451 |
2139 |
|
80 |
20 |
1.424 |
2013 |
|
75 |
25 |
1.398 |
1887 |
|
70 |
30 |
1.371 |
1761 |
|
65 |
35 |
1.345 |
1635 |
|
60 |
40 |
1.318 |
1510 |
|
59 |
41 |
1.313 |
1484 |
|
58 |
42 |
1.307 |
1459 |
|
57 |
43 |
1.302 |
1434 |
|
56 |
44 |
1.297 |
1409 |
|
55 |
45 |
1.292 |
1384 |
|
54 |
46 |
1.286 |
1359 |
|
53 |
47 |
1.281 |
1333 |
|
52 |
48 |
1.276 |
1308 |
|
51 |
49 |
1.270 |
1283 |
|
50 |
50 |
1.265 |
1258 |
|
49 |
51 |
1.260 |
1233 |
|
48 |
52 |
1.254 |
1208 |
|
47 |
53 |
1.249 |
1183 |
|
46 |
54 |
1.244 |
1157 |
|
45 |
55 |
1.239 |
1132 |
|
40 |
60 |
1.212 |
1006 |
|
35 |
65 |
1.186 |
881 |
|
30 |
70 |
1.159 |
755 |
|
25 |
75 |
1.133 |
629 |
|
20 |
80 |
1.106 |
503 |
|
15 |
85 |
1.080 |
377 |
|
10 |
90 |
1.053 |
252 |
|
5 |
95 |
1.027 |
126 |
|
0 |
100 |
1.000 |
0 |
|
|
|
Butane - Air Mixtures |
|
% Butane |
%
Air |
Specific
Gravity |
Gross BTU/cuft |
|
100 |
0 |
2.000 |
3280 |
|
95 |
5 |
1.950 |
3116 |
|
90 |
10 |
1.900 |
2952 |
|
85 |
15 |
1.850 |
2788 |
|
80 |
20 |
1.800 |
2624 |
|
75 |
25 |
1.750 |
2460 |
|
70 |
30 |
1.700 |
2296 |
|
65 |
35 |
1.650 |
2132 |
|
60 |
40 |
1.600 |
1968 |
|
59 |
41 |
1.590 |
1935 |
|
58 |
42 |
1.580 |
1902 |
|
57 |
43 |
1.570 |
1870 |
|
56 |
44 |
1.560 |
1837 |
|
55 |
45 |
1.550 |
1804 |
|
54 |
46 |
1.540 |
1770 |
|
53 |
47 |
1.530 |
1738 |
|
52 |
48 |
1.520 |
1706 |
|
51 |
49 |
1.510 |
1672 |
|
50 |
50 |
1.500 |
1640 |
|
49 |
51 |
1.490 |
1607 |
|
48 |
52 |
1.480 |
1574 |
|
47 |
53 |
1.470 |
1542 |
|
46 |
54 |
1.460 |
1509 |
|
45 |
55 |
1.450 |
1476 |
|
40 |
60 |
1.400 |
1312 |
|
35 |
65 |
1.350 |
1148 |
|
30 |
70 |
1.300 |
984 |
|
25 |
75 |
1.250 |
820 |
|
20 |
80 |
1.200 |
656 |
|
15 |
85 |
1.150 |
492 |
|
10 |
90 |
1.100 |
328 |
|
5 |
95 |
1.050 |
164 |
|
0 |
100 |
1.000 |
0 |
|
|
|
Propane (30%) Butane (70%) |
|
%
LPG |
%
Air |
Specific
Gravity |
Gross BTU/cuft |
|
100 |
0 |
1.859 |
3051 |
|
95 |
5 |
1.816 |
2898 |
|
90 |
10 |
1.773 |
2746 |
|
85 |
15 |
1.730 |
2593 |
|
80 |
20 |
1.687 |
2441 |
|
75 |
25 |
1.644 |
2288 |
|
70 |
30 |
1.601 |
2136 |
|
65 |
35 |
1.559 |
1983 |
|
60 |
40 |
1.515 |
1831 |
|
59 |
41 |
1.507 |
1800 |
|
58 |
42 |
1.498 |
1769 |
|
57 |
43 |
1.490 |
1739 |
|
56 |
44 |
1.481 |
1709 |
|
55 |
45 |
1.473 |
1678 |
|
54 |
46 |
1.464 |
1647 |
|
53 |
47 |
1.455 |
1617 |
|
52 |
48 |
1.447 |
1587 |
|
51 |
49 |
1.438 |
1555 |
|
50 |
50 |
1.430 |
1525 |
|
49 |
51 |
1.421 |
1495 |
|
48 |
52 |
1.412 |
1464 |
|
47 |
53 |
1.404 |
1434 |
|
46 |
54 |
1.395 |
1404 |
|
45 |
55 |
1.387 |
1373 |
|
40 |
60 |
1.344 |
1220 |
|
35 |
65 |
1.301 |
1068 |
|
30 |
70 |
1.258 |
915 |
|
25 |
75 |
1.215 |
763 |
|
20 |
80 |
1.172 |
610 |
|
15 |
85 |
1.129 |
458 |
|
10 |
90 |
1.086 |
305 |
|
5 |
95 |
1.043 |
153 |
|
0 |
100 |
1.000 |
0 |
|
All data
is based on the
following assumptions: |
|
Propane
Vapor |
SGU = 1.53
2516 BTU/cuft |
|
Butane
Vapor
|
SGU = 2.00
3280 BTU/cuft |
|
Engineering
Units Conversion Factors |
|
Multiply |
By |
To Obtain |
|
Pressure |
|
Atmospheres |
atm |
1.0332 |
Kilogram per cm2 |
|
atm |
14.70 |
Pounds per square inch |
|
atm |
404.17 |
Inches of Water |
|
Inches
of Mercury |
inHg |
0.0142 |
Pounds per square inch |
|
inHg |
0.4912 |
Feet of Water |
|
Inches
of Water |
inWC |
1.133 |
Pounds per square inch |
|
inWC |
0.0735 |
Inches of Mercury |
|
inWC |
0.5781 |
Ounces per square inch |
|
Kilo Pascals |
kPa |
0.01 |
bar |
|
KG per cm2 |
kg/cm2 |
14.22 |
Pounds per square inch |
|
Pounds per square inch |
psi |
0.06804 |
Atmospheres |
|
psi |
0.07031 |
Kilogram per cm2 |
|
psi |
0.145 |
kPa |
|
psi |
0.06897 |
bar |
|
psi |
2.036 |
Inches of Mercury |
|
psi |
27.67 |
Inches of Water |
|
Length
|
|
Centimeters |
cm |
0.3937 |
Inches |
|
Feet |
ft |
0.3048 |
Meters |
|
Feet |
ft |
30.48 |
Centimeters |
|
Feet |
ft |
304.8 |
Millimeters |
|
Inches |
in |
2.54 |
Centimeters |
|
Inches |
in |
25.4 |
Millimeters |
|
Kilometers |
km |
0.6214 |
Miles |
|
Meters |
m |
1.094 |
Yards |
|
Meters |
m |
3.281 |
Feet |
|
Meters |
m |
39.37 |
Inches |
|
Miles, nautical |
mls |
1853.0 |
Meters |
|
Miles, statute |
mls |
1609.0 |
Meters |
|
Miles, statute |
mls |
5280 |
Feet |
|
Miles, statute |
mls |
63360 |
Inches |
|
|
|
Multiply |
By |
To Obtain |
|
Length (continued)
|
|
Yards |
yrd |
0.9144 |
Meters |
|
Yards |
yrd |
91.44 |
Centimeters |
|
Volume
|
|
Cubic centimeter |
cm3 |
0.061023 |
Cubic inches |
|
Cubic feet |
cuft |
7.48 |
Gallons (US) |
|
Cubic feet |
cuft |
28.316 |
Liters |
|
Cubic feet |
cuft |
1728 |
Cubic inches |
|
Cubic feet |
cuft |
0.037037 |
Cubic yards |
|
Cubic feet |
cuft |
0.028316 |
Cubic meters |
|
Gallons (UK) |
gal |
1.20095 |
Gallons (US) |
|
Gallons (US) |
gal |
0.13368 |
Cubic feet |
|
Gallons (US) |
gal |
0.83267 |
Gallons (Imperial) |
|
Gallons (US) |
gal |
3.785 |
Liters |
|
Gallons (US) |
gal |
231 |
Cubic inches |
|
Liters |
l |
0.03531 |
Cubic feet |
|
Liters |
l |
0.2642 |
Gallons (US) |
|
Liters |
l |
1.057 |
Quarts (US) |
|
Liters |
l |
2.113 |
Pints (US) |
|
Pints (US) |
pnt |
0.4732 |
Liters |
|
Miscellaneous
|
|
BTU |
BTU |
252.0 |
Calories |
|
Calories |
kcal |
3.968 |
BTU |
|
Kilogram |
kg |
2.205 |
Pounds |
|
Kilowatt Hour |
kWh |
3412 |
BTU |
|
Ounces |
oz |
28.35 |
Grams |
|
Pounds |
lb |
0.4536 |
Kilograms |
|
Pounds |
lb |
453.5924 |
Grams (metric) |
|
Pounds |
lb |
21600 |
Propane BTU |
|
Definitions |
Several characteristics affect Liquified Petroleum Gas (LPG) as a
replacement fuel. These include:
- Flame Velocity and Color
- Specific Gravity
- Calorific Value
- BTU Measurement (Wobbe Index)
1. Flame
Velocity and Color
Because of the different number of carbon
atoms in propane, propane-air mixtures produce a flame that is more yellow
in color than that of natural gas. However, the yellow tips are not of any
consequence and do not affect burner operation or efficiency. Flame
velocities of LPG are near equal to that of natural gas. Therefore, there is
no significant flame lift difference between natural gas and propane-air
mixtures.
2. Specific Gravity
The density of gas, relative to air, is
called specific gravity. The specific gravity of air is defined as 1. Since
propane gas has a specific gravity of 1.5, propane-air mixtures have a
specific gravity of greater than 1. The chart on the right indicates heat
value in BTU per cubic foot, kcal per cubic meter, and the specific
gravities of various propane-air mixtures.
|
Propane
- Air Mixtures |
|
BTU/cuft
Kcal/Nm3 |
% Propane
by Volume |
% Airby Volume |
% Oxygenby Volume |
Specific Gravityof
Mixture |
|
1700
15,130 |
66.67 |
33.33 |
6.694 |
1.349 |
|
1650
14,685 |
64.70 |
35.30 |
7.378 |
1.338 |
|
1600
14,220 |
62.74 |
37.26 |
7.787 |
1.328 |
|
1550
13,795 |
60.78 |
39.22 |
8.197 |
1.318 |
|
1500
13,350 |
58.82 |
41.18 |
8.606 |
1.308 |
|
1450
12,950 |
56.86 |
43.14 |
9.016 |
1.297 |
|
1400
12,450 |
54.90 |
45.10 |
9.246 |
1.287 |
|
1350
12,015 |
52.94 |
47.06 |
9.835 |
1.277 |
|
1300
11,580 |
50.98 |
49.02 |
10.245 |
1.267 |
|
1250
11,135 |
49.02 |
50.98 |
10.654 |
1.257 |
Different heat values
result primarily from differences in specific gravity. The higher the
specific gravity, the heavier the gas. Since burner orifices, flow meters,
regulators, etc. have fixed openings, they allow less flow of heavier gas
and therefore must have a higher heat value to provide the same energy
input as a lighter gas.
Most natural gas has an
average heat value of approximately 1050 BTU/cuft (9350 kcal/m³) and a
specific gravity of 0.6 (nominal). Compatible propane-air replacement
should have a heat value of approximately 1450 BTU/cuft (12,467 kcal/m³)
and a specific gravity of 1.297.
3. CALORIFIC VALUE
The calorific value is the measurement of
the amount of heat or energy produced, and is measured either as gross
calorific value or net calorific value. The difference being the latent heat
of condensation of the water vapor produced during the combustion process.
Gross calorific value assumes all water produced during the combustion
process is fully condensed. Net calorific value assumes the water leaves
with the combustion products without being fully condensed.
Since most gas burning appliances cannot
utilize the heat content of the water vapor, gross calorific value is of
little interest. Fuel should be compared based on the net calorific value.
This is especially true for natural gas, since increased hydrogen content
results in high water formation during combustion.
4. WOBBE INDEX
The Wobbe Index, a critical factor when
analyzing Propane-Air plant requirements, is a function of gas quality and
allows matching one gas (in this case, natural gas) to a replacement gas (in
this case, Propane-Air). If the two different gases have an identical Wobbe
Index, they will produce an equal amount of heat and combustion products and
will require the same amount of combustion air. Burners, adjusted for a
specific calorific value and fitted with a replacement orifice to match a
lower Wobbe Index, result in minor combustion changes. Substituting a gas
for one with a higher Wobbe Index, generally allows a narrow acceptance
range. Flame characteristics determine the acceptance range for the
replacement gas.
The Wobbe index is defined as:
Wobbe Index = Gross Heating Value / (Square root of
Specific Gravity)
and is used to compare the energy input
into an appliance with different composition fuel gases. If two fuels have
identical Wobbe indices, then for a given burner pressure, the energy
input will also be identical. |
|