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LPG Data |
Definitions
and Technical Data
for LPG, Natural Gas and LPG/Air Mixtures |
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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. |
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Page
Index
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| Definitions |
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| Miscellaneous
Tables |
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| Standby
Plant Sizing Chart |
Cost
Savings through Standby Plants |
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Download these tables as PDF File |
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THEORETICAL
COMPATIBLE PROPANE/AIR MIXTURES |
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The table below shows
Propane/Air mixtures, compatible with natural gas with several different
specific gravities and calorific 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 |
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|
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 |
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|
Properties of |
Natural Gas |
Propane |
Butane |
|
Chemical formula |
|
CH4 |
C3H8 |
C4H10 |
|
Boiling point of liquid at atmospheric pressure |
°F
°C |
-259
-162 |
-44
-42 |
32
0 |
|
Specific Gravity of vapor (Air = 1) |
|
0.6 |
1.53 |
2.00 |
|
Specific Gravity of liquid (Water = 1) |
|
0.6 |
0.51 |
0.58 |
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Calorific value @ 60 °F (15°C) |
BTU/cuft
kcal/m3 |
1012
9005 |
2516
22,390 |
3280
29,190 |
|
BTU/gal
kcal/liter |
|
91,690
6,100 |
102,032
6,790 |
|
BTU/lb
kcal/kg |
|
21,591
11,995 |
21,221
11,790 |
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Latent heat of vaporization |
BTU/gal
kcal/kg |
|
785 |
808 |
|
Liquid weight |
lbs/gal
kg/liter |
|
4.24
0.508 |
4.81
0.576 |
Vapor volume from 1 gallon of liquid at 60 °F
Vapor volume from 1 liter of liquid at 15 °C |
cuft
m3 |
|
36.39
0.272 |
31.26
0.234 |
Vapor volume from 1 lb. of liquid at 60 °F
Vapor volume from 1 kg of liquid at 15 °C |
cuft
m3 |
|
8.547
0.534 |
6.506
0.406 |
|
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
Amount of air required to burn 1 m3 of gas |
cuft
m3 |
9.53 |
23.86 |
31.02 |
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Ignition temperature in air |
°F
°C |
1200
650 |
920 - 1020
490 - 550 |
900 - 1000
480 - 540 |
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Maximum flame temperature in air |
°F
°C |
3568
1964 |
3595
1980 |
3615
1991 |
|
Octane Number |
|
100 |
Over 100 |
92 |
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All data is approximate. For actual properties of
any particular batch, contact your fuel supplier. |
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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 |
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|
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|
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|
-30 |
-34.4 |
8 |
5.5 |
4.5 |
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|
|
|
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|
-20 |
-28.9 |
14 |
11 |
9.2 |
4.9 |
1.9 |
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|
|
|
-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 |
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* HD5, Commercial Grade Propane |
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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 |
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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 |
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Butane
Equivalents |
|
Unit |
BTU |
Pound |
Therm |
Dekatherm |
Cuft. |
Gallon |
|
1 Pound = |
21,221 |
1 |
0.212 |
0.0212 |
6.50 |
0.208 |
|
1 Therm = |
100,000 |
4.714 |
1 |
0.1 |
30.64 |
0.98 |
|
1 Dekatherm = |
1,000,000 |
47.14 |
10 |
1 |
306.4 |
9.8 |
|
1 Cuft. = |
3,280 |
0.1537 |
0.032 |
0.0032 |
1 |
0.03199 |
|
1 Gallon = |
102,032 |
4.81 |
1.02 |
0.1020 |
31.26 |
1 |
|
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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 |
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Propane
Equivalents |
|
Unit |
BTU |
Pound |
Therm |
Dekatherm |
Cuft. |
Gallon |
|
1 Pound = |
21,591 |
1 |
0.216 |
0.0216 |
8.58 |
0.239 |
|
1 Therm = |
100,000 |
4.622 |
1 |
0.1 |
39.7 |
1.10 |
|
1 Dekatherm = |
1,000,000 |
46.22 |
10 |
1 |
397 |
11.0 |
|
1 Cuft. = |
2,516 |
0.1164 |
0.025 |
0.0025 |
1 |
0.027 |
|
1 Gallon = |
91,690 |
4.24 |
0.917 |
0.0917 |
36.39 |
1 |
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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 |
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