Page 523 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition

Applied Process Design 489

Table 7-20 (continued)
Properties of Flammable Liquids, Gases, and Solids

Exnlosive limits in air, Auto- Specific Vapor / Water I i;uitable /
�. by vol. ignition gradty density �lei ting Boiling aulu- ext in-
temperature, (water (air point. °F range, °F 9 � \· Hazard
point or , bi!lt�· J �uishing.
Lower Upper •F = 1.0) 1.0) · \?P It)' I l l · agents i I
I
----
3.6 46 612 0 832 .48 -97 132 D. G, !
I. 3, 4
3 100 804 0.887 I. 52 - 168 51 -,,-,-,--i I B. I>, G. I
"'
0.918 3.00 18 322 "' I, 3 , B, D. G
2.7 16. 851 0. 924 2.55 - 112 130 s I 2. 3 I B, D, G
----- --------- - 3 -1
0.821 4. 42 , . . . . . . . . 325 -,- , -1-2- . B, n, G
0.942 5.03 - 40 47 2 sl 11, 2, 3 B
... : : I 0.908 4. 98 - 180 440 al !, 2. 3 B
0.834 4 49 - I 05 359 •I I I, 2, 3 B, D. G
- 37 i
0. 873 ---- ____ 390 __ sl ! I, 2. 3 ------
5.93
B, D, G
I, 3
,,
B,
212°F
.5' 752 I. 03 4 07 i_309 ---1-- D, G
.8 18. 570 0.839 2. 11 - 234 96 st , 3, 4 D. G
I. 484 - 40 318 i I 2a, 3 1 D, G
I. 156 - 15 295 , la. 3 I D. G
0.916 4 00 . 280 "' 1, 2. 3 1 B, D, G
----- --- ---·--------
3.8 :; .50 I. 105 3. 14 -152 190 sl 2. 3 D. r.
3.0 . 1'94. 0.900 2. 59 63 al 2, 3, 4 I D. G
I. 090 5.04 -41 367 d I, 3 B, u, G
I 040 5.35 99 514 2. 3 B
608
I 180
9.60
----- ---- ----- ----- --- I, 2. 3 ! B
.8 II 890 0.891 3.52 -99 210 sl 2, 3 I B, n, r.
I. 2. 3
. 9' 24 0.851 4. 35 < -110 347 sl 2a,3 I B, D. (;
B,I>,G,I
s
0. 747
147
0.936 7.22 - 114 334 d 3 D, G
I. 253 5.60 207 I, 3 B, I)
--- --------
I. 17 91 93 439 I, 2, 3 I B, D
I. 2. 3 , C
I. 31 -369 - 305 ct 4 . .\, E. F
73 806 I, 07 -134 -(> VS D, G. H. l
-----
795 I. 080 .03 I 207 I, 3 D,G
213
I, 3
I. 218
1114
· a·. ii .. 5.6 445-560 0.78-0.85 . 59 47 340-355 i "" 2. 3 D,G
B. D. G
I. 3 6.0 350-625 <1.0 <590 2. 3 B. D,G
B, D,G
500-705 0.80-0.90 340-640 --- ---- ---------
2. 3
. 3 6.0 490-545 0.81 380-650 2, 3 B, D. (;
5 505 0.84-0.98 425-760 I, 2, 3 B, n, G
5 765 . 0. 92-1. 06 I. 2, 3 B, D,G
5 0.92-1.07 I, 2, 3 B, D,G
2.3
------ 14. 0.937 2. 35 - 122 88 --- --- B, D, Fl, F2, G. H, I
2. I @ 257°F 600 I. 161 3.31 -34 322 I. 2, 3 B, D, F6
I. 8 16. 3 736 I . 129 3.37 -18 340 1, la, 3 B, D, H
.. .. 35' . 4 . 915 I .050 3. 35 -94 295 la, 3 B, D
j
D, H, I
4
5.3 32 ,ioo 0. 47 4 D, H, I
4.4 34 0. 44 . . . . . . . . . . . 4 D, H. I
0.38 4 0, H, I
j'_ S-:-i,'.5' \j..:1·i > 1000 0.50 4 4 D, H, !
0.61
D, H, I
4.7 33 637 0.47 4 D, H. I
17-35 70-80 0. 86 4 D, H. l
7.0 72 ........... 0.57 4 D, G, H, !
5.5 36 0.63 .. 599.:.i,49 .. 4 D, G, H, l
6.0 13. 5 .. 'i,4{j.:i,9ri I. 2, 3 B,D, H
. }-I .4 6.0-7.6 700 0.71-0.76 0-4.0 <-76 91-403 1-2._3_1 �� --
.3-1 . 4 6.0-7.6 700 0. 70-0. 75 3 . 0-4.0 <-76 91-401 2, 3 · B, D. G
6.0-7.6 800-880 0.70-0.71 3.0-4.0 <-76 108-318 2. 3 I B. D, G
6.0-7.6 800-880 0.70-0.71 3.0-4.0 <-76 107-319 2, 3 B, D, G
739 I. 26 3. 17 64 554 I. 3 B, D
812 I. 161 7.52 - 108 496 I, la, 3 I B. D
-3---,
1. 227 4.07 14 350 d B. D
600 0.92 >550 I. 2, 3 I B, D
550 0. 89 >550 i I. 2, 3 , B. D
----- -i--, � 1
700+ 0.99 . >550 B, D
:
700+ 0.97 · a: s.i · .... 1j<i. . >550 sl I, 2, 3 B, D
0.848
588
I, 2. 3 I B
.2 6.7 '4jj .. 0.688 3.45 -131 209 \ 2. 3 B, D. G
6 0. 725 3.45 -182 176-195 , 2. 3 I B, D, G
By permission, Factory Mutual Engineering Corp./McGraw-Hill Book Co., Handbook of Industrial Loss Prevention, 2nd Ed., 1967, pp.
42-16 and 42-17 [32]. This is only partial selected listing of reference.