1. Table
A.1
Thermodynamic Properties of Steamu
Table A.1 .1
Saturated Steam: TemBerature Table
Press
T
0.0l
5
10
l5
A
(tl
20
25
30
.13
40
z+
t)
50
5l)
60
o3
70
BO
85
90
95
Sat.
kPa
P
l,iquid
0.61
13
0.8721
1.2276
1.7051
2.339
3.169
4.246
5.628
7.384
9.593
12.349
15.758
19.940
X
31.19
38.58
47.39
57.83
70.14
84.55
25.03
uf
Sat.
Vapor
Ile
0.001 000 206.14
0.001 000 147 .t2
0.001 000 106.38
0.001 001 77 .93
0.001 002 57 .7s
0.001 003 43.36
0.001 004 32.89
0.001 006 25.22
0.001 008 19.52
0.001 010 15.26
0.001 012 12.03
015
017
0.001 020
0.001 023
0,001 026
0.001 029
0.001 033
0.001 036
0.001 040
0.001
0.00i
9.568
7.671
6.197
5.042
4.
l3l
3.407
2.828
2.361
1.982
Sat.
Liquid
U1
Sat.
Evap. Vapor
u'
L[s
.00 2375.3
.3
.2
42.00
6 2.99 2333 .r
'10.97
236 i
2347
2375.3
2382.3
2389.2
2 396. i
83.95 2319.0 2402.9
tB4-88 2304.9 2409,8
1?5.78 2290.8 2416.6
146.67 2276.1 2423.4
167.56 2262.6 2430.1
188.44 2248.4 2436.8
209.32 2234.2 2443.5
:30.21 2219.9 2450.1
251.1 I 2205.5 2456.6
272.02 2l9l.l 2463.1
292.95 2r76.6 2469.6
313.90 2162.0 2475.9
334.86 2147.4 2482.2
355.84 2132.6 2488.4
376.85 21t7.7 2494.5
397.88 2102.7 2500.6
Iinropy
Enthalpy
Internal Energy
Specific Volume
Sat.
Liquid
ht
Sat. Sat.
Evap. Vapor Liquid Evap.
.r/
.!r"
h,t
hrn
.01 2501.3 250r .4
20.98 2489.6 2510.6
42.01 2477 .7 2519.8
62.9S 2465.9 2528.9
83.96 2454.1 2538.1
i04.89 2442.3 2547.2
r25.79 2430.5 2556.3
r46.68 2418.6 2565.3
167.57 2406.7 2s74.:
188.45 2394.8 2583.2
209.33 2382.7 2592.1
230.23 2370.7 2600.9
251 .13 2958.5 2609.6
272.06 2346.2 2618.3
292.98 2333.8 2626.8
313.93 232r.4 2635.3
334.9 I 2308.8 264:.7
355.90 2296.0 2651.9
376.92 2283.2 2660.1
397.96 2270.2 266tt.l
Sat.
VaPor
Jo
.0000 9. I l-r62 9.1562
.0761 tt.9496 9.0257
. l5 l0 8.7498 8.9008
.2245 8.5569 8.78 i 4
.2966 8.3 706 8.6672
.3674.8.1905 8.5580
.4369 8.0164 8.4533
.5053 7 .8478 8.3531
.s725 7.684s 8.2570
.6387 7 .5261 8.1648
.7038 7 .3725 8.0763
.7675 k2234 7.9913
.8312 7 .0784 7.9096
.tj935 {i 9375 7.8310
.9549 6.8004 7.7553
I .() t55 6.6669 7.6824
1.07s3 6.5369 7.6122
I.
l:]43
6.41
02
7
.5445
1.1925 6.2866 7.4791
1.2500 6. 1659 7.4159
,,Aclapted f r.orn
(i. l(e,ves, Philip G. Hill, ancl Joan G. Moore, Stuam rn,les, (New Yot'k:.lolrn wiley & sons'
.|oseph H. I(eenan, l.rederick
Inc..1969).

2. Table A.1 .1 (Continued)
Saturated Steam: Temperature Table
Specific Volume
Internal Ener.gy
Iinthalpy
Entropy
Sat.
L,
Press.
NIPa
Sat.
Liquid
Evap
Sat.
Tg
Liquid
Sat.
U1
Vapor
Sat.
P
Vapor
Sat.
T
Liquid
Sat.
Uy
Evap.
ufs
Vaptir
us
hr
Liquid
h,,,
t,,
Evap
Vapor
.t/
Jn,
.t9
2257.0
2ii76. i
3069
3630
2230 .2
2691.5
4 185
100
105
0.101 35 0.001 044 |.6729
0.120 8? 0.001 048 1.4 t 94
0.143 27 0.001 052 1.2102
0.169 06 0.001 056 l 0366
0.198 53 0.001 060 0.8919
0.2321
0.001 065 0.7 7 06
0.2701
0.001 070 0.6685
I l0
t 15
120
t25
130
135
140
0.313i)
0.3613
i
0.00
075
0.001 080
4I8.94
440.02
461.14
482.30
503.50
t45
0.4151
0.00r 0u5
0.47 58
0.3928
0.3468
0.3071
0.2727
0.5431
0.001 096
0.61 78
t65
0.7005
170
0.7 s 17
0.001 102
0.001 t 0B
0.001 114
0.8920
0.00r 12t
1,0021
0.2168
1.3978
1.5538
0.001 127
0.001 134
0.001 I4t
0.001 149
0.001 157
1.7230
r.9062
0.00I
0.194 05
0.174 09
0.156 54
0.141 05
0.127 36
0.115 2l
0.104 4I
r/5
rB0
185
190
r95
200
205
210
215
220
225
230
235
240
245
250
255
260
265
270
27 5
280
285
290
295
300
305
310
3I5
320
330
340
350
360
':J70
374.14
1
.
t227
1.2544
I
0.00
164
173
l8l
0.2428
2.10,1
0.001
2.318
2.548
0.001 190
0.094 79
0.086 19
2.795
0.00
0.00
r 209
0.07
3.060
3.344
r
199
0.001 219
0.001 229
3.648
3.973
0.00r ?40
4.3 19
5.49!l
0.001
0.001
0.001
0.001
5.942
0.00r
6.4t2
6.909
0.001
0.001
.436
0-aql
7.993
0.001
0.001
0.001
4.688
5.081
7
8.58 r
9.202
9.856
10.547
rr.271
12.845
14.586
16.5 I 3
I8.65
21.03
22.09
r
0.00
0.00
t
r
?51
0.078 49
r
58
37
0.065
0.059 76
0.051 71
0.050 13
0.045 98
0.042 21
0.038 77
263
276
289
302 0.035 64
3r7 0.032 79
332 0.030 17
348 0.027 77
366 0.025 57
384 0.023 rt4
404 0.021 67
425 0.0 r 9 948
447 0.018 350
472 0.0 r 6 867
440.15 2243.7 2683.8
46 I
.3
0
6.0480 7.3549
5.9328 7,2958
5.8202 7.2387
5.7100 7.1833
5.6020 7.1296
5.4962 7.0775
5.3925 7.0269
s.2907 6.9777
482.48 22 t 6.5 2699.0 t.4734
503.71 2202.6 2706.3
5276
524.99 2188.5 27 13.5 l 581.3
546.31 2174.2 2720.5 1.6344
567.69 2159.6 2727.3 | .6870
.6-!)-.n
5rJ9.l3 2144.7 t4lJJ.V ).7391 5.I908
610.63 2129.6 2710.3 1.7507 5.0926 6.9299
6.8833
632.20 2t14,3 2746.5
84r8 4.9960 6.8379
653.84 2098.6 27 52.4
8925 4.9010 6.7935
675.55 2082.6 2758. I
9427 4.8075 6.7502
697.34 2066.2 2763.5
9925 4.7153
719.21 2049.5 2768.7 2.0419 4.6244 6.7078
741.17 2032.4 tt t.).o 2.0909 4.5347 6.6663
763.22 2015.0 2778.2 2. 396 4.4461 6.6256
785.37 1997. I 2782.4 2, I 879 4.3586 6.5857
807.62 1978.8 2786.4 2.2359 4.2720 6.5465
829.98 1960.0 2790.0 2.2835 4. t863 6.5079
852.45 1940.7 97q,) 2.3 3 09 4.r014 6.4698
6.4323
875.04 1921.0, 2796.0 2.3 780 1.0r72 6.3952
897.76 1900.7 2798.5 2.4248 3.9337 6.3585
920.62
943.62
966.78
1009.89
1033.2 r
1056.71
I
080.39
l 04.28
r 28.39
| 52.7 4
t77 .36
1202.25
1227.46
1253.00
r
682.9
166 I .5
1639.6
16t7.2
r594.2
1570.8
r546.7
1522.0
1496.7
1470.6
1443.9
1416.3
1387.9
1358.7
r328.4
.l
t278.92
1297
1305.2
1332.0
1264.7
1231.0
195.9
159.4
I 359.3
I387.1
0.001
1415.5
0.001 499 0.015 488 1444.6
0.001 561 0.012 996 1505.3
0.001
0.001
0.001
0.002
0.003
2518.1
204t.4
4t9.04
918. r4
940.87
963.73
986.74
0.4463
0.001 091
2506.5
2512.4
2523.7
2025.8 2529.3
524.7 4 2009.9 2531.6
546.02 r 993.9 2539.9
567.35 t977.7 2545.0
588.7 4 r 961 .3 2550.0
610. t 8 t914.7 2554.9
631.68 927.9 2559.5
653.24 r-9 I 0.8 2564.r
674.87 1893.5 2568.4
696.56 I876.0 2572.5
718.33 I 858. I 2576.5
7 40.17
r 840.0
2580.2
762.09 l82l .6 2583.7
784. I 0 l 802.9 2587.0
806. t9 r 783.8 2590.0
828.37 1764.4 2592.8
850.65 17 44.7 96q6 C
87i3.04 1724.5 2s97.s
895.53 1703.9 2599.5
0.5822
0.5089
150
155
160
2087.6
2072.3
2057.0
Sat.
121.1
1080.9
638
740
893
213
r 0 797
1570.3
0.008 813 r 6'1r.9
993.7
894.3
/ /o.o
0.006 945
0.004 925
I 844. 0
626.3
384.5
155
0.003 i 55 2029.6
0
0.0
17 25
.2
260 1. I
2602.4
2603.3
2603.9
2604.1
2604.0
2603.4
2602.4
2600.9
2599.0
2596.6
2593.7
2590.2
2586. r
258
r.4
2576.0
2569.9
2563.0
2555.2
2516.4
2536.6
2525.5
2498.9
2464.6
2418.4
1
990. I 2
1013.62
1037.32
106r.23
1085.36
109.73
134.37
159.28
184.5 i
1210.07
1235.99
1262.31
1289.07
13 r 6.3
1344.0
r372.1
r40r.3
r431.0
1461.5
t525.3
235 I .5
1554.2
1670.6
1760.5
2228.5
2029.6
r 890.5
2099.3
1879.9 2800.5 2.47t4 3.8507 6.3221
2.5r78 3.7683 6.2861
1836.5 2803.3 2.q639 3.6r.163 6.2503
1813.8 2804.0 2.6099 3.6047 6.2146
1790.5 2804.2 2.6558'3.5233 6.179r
1766.5 2803.8 2.701b 3.4422 6.1437
174t.7 2803.0 2.7472 3.3ii r2 6.1083
t716.2 2U01.5 2.7 927 3.2 802 6.0730
1689.8 2799.5 2.8383 3.1992 6.0375
r662.5 2796.9 2.8838 3.llBl 6.0019
1634.4 2793.6 2.9294 3.0368 5.9662
1 605. ? 27 89 .7
2.9751 2.955i 5.9301 *
r574.9 2785.0 3.0208 2.8730 5.8938
r543.6 2779.6 3.0668 2.7903 5.8571
I5t1.0 2773.1J 3.1130 2.7070 5.8199
1477.1 2766.2 3.1594 2.6227 5.7821
1441.8 2758. I 3.2062 2.537 5 5.7 437
1404.9 2749.0 3.2534 2.15t t 5.7 045
1366.4 2738.7 3.30r0 2.3633 5.6643
1 3 26.0 27 27 .t
3.3493 2.27 37 5.62 30
1283.5 27 14.5 3.3982 2. r 82 l 5.5804
r 238.6 2700.
3.4480 2.0882 5.5362
i 140.6 2665.9 3.5507 1.8909 5.4417
t027 .9 2622.0 3.6594 1.6763 5.3357
893.4 2563.!) 3.7777 1.4335 5.2112
720.5 248r.0 3.9147 1. r379 5.0526
44t .6 233 2.
4. n06 .6865 4.7971
1858.5 ?802.r
r
0
1
2099.3
4.4298
0
4.4298

3. Table A.1.2
Saturated Steam: Pressure Table
Specific Volume
Press.
kPa /
lrT
13
L0
1.5
2.0
2.5
3.0
4.0
5.0
7.5
10
15
20
25
30
40
50
75
Te m p.
oC
Sat.
Sat.
Liquid
Vapor
us
U1
0.61
r 000
0.0 I
0.00
6,98
0.001 000
0.001 001
13.03
17.50
r 001
0.00
2 1.08
0.001 002
24.08
28.96
0.00
32.8rJ
t
003
0.001 004
0.001 005
40.29
0.00I 00ti
45.8I
0.001 010
53.97
0.00r 0i4
60.06
0.001 017
0.001 020
0.001 022
0.001 027
64.97
69.10
7 5.87
B
1.33
0.00
0.150 I I 1.37
0. 175 l 16.06
0.200 120.23
043
048
12.1.()o
|
ul
6.204 27 i.90
5,229 289.20
3.993 317.53
3.240 340.44
2.217 :r8+.31
037
0.001
0.001
0.001
0.00 r
0.(x) I
Sat.
l-iquid
206.14 .00
r 29.21
29.30
87.98 54.71
67.00 73,48
54.25 88.48
45.67 101.04
34.80 12r.45
28.19 i37.81
19.24 r68.78
14.67 i 91.82
10.02 225.92
7 .649 251.38
r 030
0.00I
91.78
Internal Energy
Sat.
Evap. Vapor
ulg
ut,
2375.3 237s.3
2355.7 2385.0
2338.6 2393.3
2326.0 2399.5
2315.9 2404.4
2307.5 2408.5
2293.7 2415.2
2282.7 2420.5
2261.7 2430.5
2246.1 2437.9
2222.8 2448.7
2205.4 2456.7
2191.2 2463.1
2179.2 2468.4
2159.5 2477 .0
2143.4 2483.9
2r12.4 2496.7
Entropy
Entl'ralpy
Sat. Sat.
Evap. Vapor Liquid livap.
hto
h,,
J1
stu
Sat.
Liquid
hI
.0
r
2501.3
2484.9
2470.6
2460.0
29.30
1.4
25t4.2
.0000
250
|
2521t.3
73.48
2533.5
88.49 245r.6 2540.0
54.7
101.05 2444.5
2545.5
2554,4
059
.1957
.2607
.r
.3120
.3545
.4226
Sat.
Vapor
.re
9.1562
8.8697
8.6322
8.4629
9.1562
8.9756
8.8279
8.7237
8.331
8.6432
8.2 23
1
1
8.57
7
6
121.46 2432.9
8.0520 8.4746
137.82 2423.7 25ii 1.5 .4764 7 .9187 8.3951
168.79 2406.0 2574.8 .5764 7 .67 50 8.2515
-19 l .83 2392.8 2584.7 .6493
7.5009 8.1502
225.94 2373.1 2599.1 ./ .7549 7.2Pfi6 B.oo85
251.40 2358.3 2009.7 .8320 7.0766 7.9085
27r.93 2346.3 2618.2 .8931 6.9383 7.8314
289.23 2336.1 2625.3 .9439 6.8247 7.7686
317.58 2319.2 2636.8 1.0259 6.6441 7.6700
340.49 2305.4 26115.9 l 0910 6.5029 7.5939
384.39 227 8.6 2663.0 r.2r30 6.2.134 7.1561
Mlta
100 99.63
25 105.99
0.
0. i
O.?2ir
o o{)
1.6940
t.37 49
t. l 593
trI).)
r.0036
0.8857
o.7!):l:l
0s7
0(i I
( )( t.l
4r7.46
417.36 2088.7 2s06.1
144.t9 2069.3 !5 r3.5
466.94 2052.7 2519.7
186.80 2038. r 2524.9
444.32 2241.0 2685.4
467 .l | 2226.5 2693.6
486.99 2213.6 2700.6
',J':o..ti
t-'2O.72 :
50.1.49 2O25.0 2lt2!t.b
:.to l:1.
i ?r:ttt.r)
2258.0
50,1.70 !20r.()
l1)
l.:l
2675.5
2706.7
!7 r2.
r
1.3026
| .37 40
6.0568 7.3594
5.9104 7.2844
897
.4336
5 .7
484)
5:to I
5.6868 7.1717
5.5970 7.127 I
i7 0(;
5.lt I7ll
7
.2233
7.(l!l7tl
-.!i!#.' .*'.-.'.. *11W
0.250
0.27 5
0.300
0.325
0.350
0.375
0.40
0.45
0.50
0.55
0.60
0.65
0.70
0.7 5
0.80
0.85
0.90
127.41
130.60
I .).1.3 )
136.30
138.88
143.63
0.00I
r47.93
l5r.86
155.4tJ
158.85
r 62.01
164.97
167.78
170.43
172:96
17
5.38
1.10
18.1.09
1.30
1.40
I .50
187.99
191.64
195.07
198.32
l./5
2.00
2.25
2.5
3.0
0.6573
0.6058
0.5620
0.5243
r 070
r 073
r 076
t4r.32
1.00
r
1,20 )
0.7 187
0.00
0.00
0.00
0.001 079
0.001 081
177.69
179.91
0.!15
0.001 067
0.49
i4
084
0.001 088
0.001 093
0.001 097
0.4625
0.001 r 0l
0.3 r 57
04
0.2927
{).2729
0.2556
().2404
0.00
r
'0.001
r
108
0.001 I l2
0.001 I l5
0.00
t
I
0.4 r 40
0.3749
0.3427
l8 0.2270
0.001
0.001
0.001
0.001
0.001
l2 l
0.2 150
124
127
133
0.2042
0.00
l
r
39
205.76
212.42
0.001
0.001
0.001
144
149
154
166
177
218.,r5
0.00I
I B7
223.99
233.90
0.0t)
0.00
0.00r
I 197
i 2 l7
0.r94 44
0.177
0.163
0.151
0.140
53
33
25
0.r3r
84
77
0.
n3
49
0.099
0.088
0.079
0.066
63
75
98
68
535.37 2181.5
548.89 2r72.4
56r.47 2r63.8
573.25 2155.8
584.33 2l48.l
594.81 2140.8
604.74 2133.8
623.25 2120.7
640.23 2 r 08.5
655.93 2097.0
670.56 2086.3
684.18 2076.0
697.22 2066.3
709.47 2057.t)
535.10 2002.1 2537.2
548.59 1991.9 2540.5
561.15 1982.4 2543.6
572.90 1973.5 2546.4
583.95 1965.0 2548.9
594.40 r956.9 255 t.3
604.31 1949.3 2553.6
622.77 1934.9 2557.6
639.68 192 1.6 256r.2
655.32 1909.2 2564.5
669.90 i897.5 2567.4
683.56 1886.5 2570.r
696.44 1876. I 2572.5
708.64 1866.1 2574.7
720.22 1856.6 2576.8
73r.27 1847.4 2578.7
7 4r.83 1838.6 2580.5
751.95 r830.2 2582.1
761.68 r822.0 2583.6
780.09 1806.3 2586.4
797
.29 r 79l.5
8I3.44
1777
.5
828.70 1764.1
843.16' 175r.3
876.46 172t.4
906.44 r693.8
933.83 1668.2
959.rr 1644.0
r004.78 1599.3
2588.8
2591.0
2592.8
2594.5
2597.8
2600.3
2602.0
2603.1
2604.1
1
i6.9
6072
272r.3
1.6408
2725.3
r.67rB
2729.0
2732.4
.7006
27 35.6
.7
2738.6
2743.9
.77 66
r.8207
27 48.7
27 53.0
.8607
.8973
2756.r1
.93r2
2760.3
2763.5
2766.4
:9627
.9C22
27
.7275
528
5.4455
5.3801
5.3201
5.2646
5.2130
5.1647
5. I 193
5.0359
4.9606
4.8920
4.8288
4.7
7
03
4.7158
2.0200 4.6647
72r.rt 2048.0 2769, I 2.0462 4.6166
732.22 2039.4 2771.6 z.0z r o 4,5711
742.83 2031.I 2773.9 2.0946 ,1.5280
753.02 2023.1 27 7 6.1 2.t 172. 4.4869
762.8I 2015.3 2778.1 2.t387 1.4478
781.34 2000.4 2781.7 2.1792 4.3744
798.65 1986.2 2784.8 2.2166 4.3067
814.93 r972.7 2787.6 2.2515 4.2438
830.30 1959.7 2790.0 2.2842 4. 1850
844.89 t947.3 2792.2 2.3150 4. r 298
878.50 1917.9 2796.4 2.3851 4.0044
908.79 1890.7 2799.5 2.447 4 3.8935
936.49 t865.2 280r.7 2.5035 i.7937
962.1I 184r.0 2803. l 2.5547 3.7028
00 8.42 t7 95 .7 2804.2 2.6457 3.5412
7.0527
7.0209
6.9919
6.9652
6.9405
6.9175
6.8959
6.8565
6.8213
6.7893
6.7600
6.733
l"
6.7080
6.6847
6.6628
6.6421
6.6226
6.6041
6.5865
6.5536
6.5233
6.4953
6.4693
6.4448
6.3896
6.3409
6.2972
6.2575
6.1869

4. Table A.'1.2 (Continued)
Table
SaiurateO Steam: Pressure
Pt'ess
uJ
ug
uJ
07
0.001 2:15 0.057
0.001 252 0.049 78
0.001 286 0.039 44
0.001 319 0-032 44
0.001 35i 0.027 37
o.oo1 384 0".j'23-52
242.60
250.40
263.99
27 5.64
285.88
295.06
303.40
1
I'r
6
7
d
I
l0
1l
318. 15
12
13
324.75
330.93
336.75
l4
l5
"19
94
T7
352.37
l8
19
357.06
361.54
20
365.81
2l
22
369.89
373.80
2.0!l
37
2603.7
2602.3
1049.75
i 087.3 1
r
1520.0
1449.3
1384.3
1205.44
0.003 155 0.003
4.t1
Vapor
hu
J/
.)tu
Js
t'i 53.7
2803.4
2801.4
hl
558.3
Virpot"
Evap.
hr,,
Liquid
uq
Liquid
Sat.
VaPor
S:rt.
Evap
Sat'
1714.r
2597.1
t264.2
1207.3
1 151.4
1096.0
1040.7
tr54.23
1640. I
2589.7
2580.5
2569.8
2557.8
2544.4
1323.0
1213.35
1267.00
1316.64
1363.26
1407.56
1450. I
1571 .0
e(9q
R
e ?96'1
2.7964
2.9202 3.0532
2794.3.
2784.3
5.8 89 2
3.1211
2.5364 5.7 432
2.3915 b.6772
9'1444 5.6141
2',705.6
3.2068
3.2858
3.3596
3.4295
2. I 233
5.55z
3.4962
1.9962
1.8718
^
5.4323
.)Ft a
505.1
1441.3
1378.9
1317.1
1255.5
I
t)
3.0267
1
2758.0
e1
L')
1
2724.7
l193.6 2684.9
153 1 .5
I 130.7
1571.1
1610.5
1650. I
1066.5
1000.0
o/).4
2476.8
2455.5
2431.7
2405.0
2374.3
598:1
2338.1
2293.0
2230.6
688.0
583.4
2464.5
507 .5
I / /O.5
1826.3
1888.4
446.2
2334.6
2 I ti5.6
2099.3
869.8
809.0
7
44.8
388.5
194 2
690.3
3.5606
2662.2
9n.9.)
<)
r43.4
2029.6
2099.3
0
1.6249
3,7 461
1.4994
3.8079
3.8715
3.9388
4.0139
2409.7
c.J / r
485
1
1.3698
I ,)q9q
.7
t
4A94
3.6848
2509. I
t732.0
5.8133
3.6232
2637.6
2610.5
930.6 2580.6
856.9 2547.2
2087. I
0
155 2029.6
1
5.5134
2.8625
2.6922
1491.3
o9R 9
6.1253
6.0701
3.400i)
3.27 37
2513.7
2496.1
985.0
I
347.44
t6
1045.43
1082.31
I 147.8 I
1257.55
1305.57
1350.5 t
0.001 418 0.020 48
452 0.018 026 1393.04
0.001
0.001 489 0.015 987 1433.7
0.001 527 0.014 263 t473.0
0.00 I 567 0.012 780 1511.1
0.001 6l 1 0.01 I 485 r 548.6
0.001 658 0.010 337 1585.6
0.001 71 0.009 306 1622.7
0.001 770 0.008 364 r 660.2
0.001 840 0.007 489 1698.9
0.001 924 0.006 657 1739.9
0.002 036 0.005 834 1785.6
1
0.002 207 0.004 952 I 842.
742 0.003 568 196 1 ,9
0.002
31 1.06
Table
Liquid
T
3.5
2
Vapor
Sat.
"C
Sat.
Sat.
Evap.
u1s
Sat.
Liquid
''_'r
^
NIPa
P
Sat.
EnttopY
EnthalPY
lnternal EnergY
Specific Volume
,
5.3098
h.2455
5.ll
t
t
5.1 044
5.0228
4.9269
4.8013
.22t6 4.5327
1.0839
4.107 5
4.31 l0
.9130
.6938
4.4298
0
4.4298
A.1 .3
Superheated Vapor
P:
P
.010 MPa (45.81)
:
P:
.050 MPa (81.33)
.10 MPa 199.63)
T
Sat. 14.67 4 2437.9 2584.7
50 14.869 2443.9 2592.6
100 17.196 2515,5 2687.5
150 19.5 l2 2587.9 2783.0
200 21.825 2661.3 2879.5
250 24.126 2736.0 2977.3
300 26.145 28 2. 1 307 6.5
400 31.063 2968.9 3279.6
500 35.679 3t32.:J 3489. t
600 40.295 3 302.5 37 05.4
700 44.9 t r 3479.6 3928.7
800 49.526 3663.8 4159.0
900 54.l4l 3855.0 4396.4
1000 58.7 57 4053.0 4640.6
r 100 63.372
4257 .5 4891.2
r 200 67 .987
4467.9 5147 .8
8.r7 49
4683.7
72.602
P
Sat.
150
200
250
300
.100
.8857
.959ti
r.0803
1.
r988
1.3162
1.5493
:
3.418
3.889
4.356
4.820
5.284
6.209
8.4479
8.6882
8.9038
9. 1 002
9.2s1 3
1
1300
3.240 2483.9 2645.9
8. l 502
9.6077
9.8978
10.r608
10.4028
10.6281
r
5409.7
0.8396
1.0393
t.2287
1.4091
1.581 I
8. 2 2 I 8
:
.7
7
.6947
5.5
327 8.9
307
8.53 73
3488.7
3705.1
3928.5
4158.9
8.8642
9.1546
9.4178
9.6599
9.8852
4396.3 r0.0967
4640.5 10.2964
489r.1 10.4859
5147.7 10.6662
5409.6 10.8382
.30 MPa (133.55)
.6058 2543.6
.6339 2570,8
7.7086
7.8926
6.6
.3
2968.5
3132.0
3302.2
3479.4
9.904 3663.6
10.828 3854.9
11.751 4052.9
12.674 4257.4
13.597 4467.8
14.521 4683.6
2529.5 2706.7 7.1272
2576.9 2768.8 7.2795
2654.4 2870.5 7.5066
327
28 l I
.r34
8.057
B.9B 1
P
2966.7
1.6 2682.5
2585.6 2780.1 7 .9401
2659.9 2871 .1 8.1580
2735.0 2976.0 8.3556
7
.20 MPa (120.23)
273r.2 297r.0
2808.6 3071.8
251
7.5g3g
2725.3
6.9919
7.0778
7.3rt5
.7964 2728.7
.8753 2806.7
I
2967.6
3069.3
7.7022
2965.6
327 5.0
8.0330
.03
1
5
/.5IOO
2506.
l
267
5.5
7
L6958 2506.7 2676.2
r.9364 2582.8 2776.4
2.t72 2658. i 2875.3
2.406 2733.7 2974.3
2.639 28 r 0.4 307 4.3
3.103 2967.9 3278.2
3.565 313r.6 3488,r
4.028 330i.9 3704.7
1.490 3479.2 3928.2
4.952
5.4r4
5.875
6.337
6.799
7.260
P
276r.0
163 2650.7 2865.6
1.6940
.3594
7.3614
7.6t34
7.8343
8.0333
8.2158
8.5435
8.8342
9.0976
9.3398
9.5652
9.7767
3663.5 4 r 58.6
3854.8 4396. r
4052.8 4640.3 9.9764
4257.3 489r.0 10.r659
4467
.7
5147
.6
.1683.5 5409.5
:
10.3463
10.5183
.4() MPa (143.63)
.4625 2553.6 2738.6
.4708 2564.5 2752.8
.5342 2646.8 2860.5
.595 i
2726.1 2564.2
.6548 2804.8 3066.8
.7726 2964.4 3273.4
6.8959
6.9299
7.1706
7.3789
7.5662
7.8985

5. Table A.1.3 (Continued)
Superheated Vapor
"l
I'
ir00
600
700
800
900
i000
l 100
1200
r 300
Sat.
200
250
300
350
400
500
600
700
800
900
I(XX)
l100
r200
1300
:
P
.20 MPa (120.23)
L78t4 3l30.tJ 3187.1 8.5133
2.013 3301.4 3704.0 8.7770
2.244 3478.8 3927.6 9.0194
2.475 3663. r 4158.2 9.2449
2.7 06
3 854.5 4395.8 9.4566
2.937 4052.5 4640.0 9.6563
4257.0 4890.7 9.8458
3. r 68
3.399 4467.5 5147.3 10.0262
3.630 4683.1 5409.3 I0.1982
P : .50 MPa (151 .86)
.37
49
2561.2
.4249 2642.9
.4744 2723.5
.5226 2802.9
.5701 2882.6
.6173 2963.2
.7109 3128.4
.8041 3299.6
.8969 3.177.5
.9896 3662. 1
1.0822 3853.6
LI
27 48.7
2855.4
2960.7
3064.2
3167 .7
321 t.9
8.0873
7.3522
8.5952
4394.7
9.0329
9.2328
405
r.2672
4256.3 4889.9
4466.8 5146.6
4682.5 5408.6
1.3596
|.4521
7.7938
3483.9
3701.7
3925.9
4156.9
.17,47
1
6.8213
7.0592
7.2709
7.4599
7.6329
.1639. I
8.821
1
9.4224
9.6029
9.7749
:
P:.40
.30 MPa (133.55)
1867 3130.0 3486.0 8.325 r
1.3414 3300.8 3703.2 8.5892
r.4957 3478.4 3927.1 8.8319
1.6499 3662.9 4t57 .8 9.0576
1.8041 3854.2 4395.4 9.2692
t.9581 4052.3 4639.7 9.4690
2.lt2t 4256.8 4890.4 9.6585
2.2661 4467 .2 5147 .t 9.8389
2.4201 4683.0 5409.0 10.01l0
l.
P:.60
.7
472
.8245
.9017
.9788
.8893 3 t29.2 3484.9
1.0055 3300.2 3702.4
2756.8
2850.I
2957 .2
3477 .9 3926.5
t.2372 3662.1 4157.3
3061.6 7 .3721
3165.7 7.5464
3270.3 7.7079
3482.8 8.002 r
3700.9 8.2674
3477 .0 3925.3 8.5107
3661.8 4156.5 8.7367
3853.4 4394.4 8.9486
405 I .5 4638.8 9. l4fi.5
1.0559 4256.r 4889.6
1.1330 4466.5 5146.3
1.2101 4682.3 5408.3
8.9244
1.3529 3853.9 4395. l
1.4685 4052.0 4639.4
1.5840 425b.5 4890.2
1.6996 4467.0 5146.8
r.8l5 r 4682.8 5408.8
P:.80
6.7600
6.9665
7.1816
8.1913
8.4558
8.6987
l.l2l5
MPa (158.85)
.3157 2567.4
.3520 2638.9
.3938 2720.9
.4344 2801 ,0
.4742 2881.2
.5137 2962.1
.5920 3127 .6
.6697 3299.r
MPa (143.63)
.2404
.2608
.2931
.3241
.3514
.3843
.4433
9. r362
9.3360
9.5256
9.7060
9.8780
MPa (170.43)
2576.8
2630.6
2715.5
2797.2
2878.2
2959.7
3126.0
2769.
r
2839.3
2950.0
3056.5
3i61.7
3267 .t
3480.6
6.6628
6.8158
7.0384
7.2328
7.4089
7.5716
7.8673
8. r333
8.3770
8 3297.S 36ee:4
.5601 347 6.2 3924.2
.6t8r 3661.r 41 55 .6 8.60 3
.676 r 3852.8 43s3.7 8.8 I 53
.50
r
3
.7340
9.338I
.79
19
.1{t3ft.?
405 l,()
4255.6
4889.
I
.8497 4466.1 5145.9
.9076 4681.8 5407.9
9.5185
9.6906
9.015.?
9.2050
9.3855
9.5575
P : 1.40 MPa (195.07)
P : 1.20 MPa (187.99)
P: 1.00 MPa (179.91)
Saf. .194 44 2583.6 2778.1 6.5865 .163 33 2588.8 2784.8 6.5233 .140 84 2592.8 2790.0 6.4693
200 .2060 2621.9 2827.9 6.6940 .169 30 2612.8 2815.9 6.5898 .t43 02 2603.I 2803.3 6.497 5
250 .2327 2709.9 2942.6 6.924? .r92 34 2704.2 2935.0 ^ 6.8294 .163 50 2698.3 2927.2 6.7467
300 .2575 2793.2 3051.2 7.1225 .2138 2789.2 3045.8 7 .0317 .182 2B 2785.2 3040.4 6.9534
350 .2825 2875.2 3157.7 7.3011 .2345 2872.2 3153.6 7 .2r2r .2003 2869.2 3 r 49.5 7.1360
400 .3066 2957.3 3263.9 7.465r .2548 2954.9 3260.7 7.3774 .2178 2952.5 3257 .5 7.3026 "
500 .3541 3124.4 3478.5 7 .7622 .2946 3 122.8 3476.3 7.6759 .2521 3 l2 1. 3474.1 1.e,C2i
600 .401 I 3296.8 3697.9 8.0290 .3339 3295.6 3696.3 .7.9435 .2860 325y.4 3694.8 7.87l0
700 .447 B 347 5.3 3923. I 8.273 r .3729 3474.4 3922.0 8.1881 .3191r 3473.6 3920.8 8. I 160
800 .4943 3660.4 4154.7 8.4996 .41 l8 3659.7 4 153.8 8.4 l48 .3528 3659.0 4 r53.0 8.3431
900 .5407 3852.2 4392.9 B.7l 18 .4505 3851 .6 4392.2 8.6272 .3861 3851. I 4391 .5 8.5556
r000 .5871 4050.5 4637 .6 B.9l l9 .4892 4050.0 4637.0 8.8274 .4192 4049.5 4636.1 8.7559
9.1017 .5278 1254.6 4888.0 9.0172 .4524 4254.1 4887.5 8.9457
I i00 .6335 4255.1 4888.6
r200 .6798 4465.6 5145.4 9.2822 .5665 4465.1 5144.9 9.1977 .4855 4464.7 5t44.4 9. 1262
1300 .7261 .1681.3 5407 .4 9.4543 .6051 4680.9 5407.0 9.3698 .5186 4680.4 5406.5 9.2984
P : 2.00 MPa (212.42)
P: 1.80 MPa (207.15)
P: 1.60 MPa (201.41)
Sat. .123 80 2596.0 2794.0 6.42t8 .ll0 42 2598.4 2797.r 6.379'4 .099 63 2600.3 2799.5 6.3409
225 .r32 87 2644.7 2857.3 6.5518 .116 73 2636.6 2846.7 6.4808 .1.03 77 2628.3 2 83 5.8 6.4147
250 .l4l 84 2692.3 2919.2 6.6732 .t24 97 2686.0 2911.0 6.6066 .r11 44 2679.6 2902.5 6.5453
300 .158 62 2781.1 3034.8 6.8844 .140 2r 2776.9 3029.2 6.8226 .t25 17 2772.6 3023.5 6.7664
350 .174 56 2866.1 3145.4 7.0691 .154 57 2863.0 3141.2 7.0100 .138 57 2859.8 3137.0 6.9563
7 .r27
r400 .190 05 2950.1 3254.2 7.2374 .-.168 47 2947.7 3250.9 7 .t794 .15l 20 2945 2 3247.6 7.4317|
3r16.2 346?
. 500 .2203 3119.5 3472.0 7.5390 - .195 50 31 17.9 3469.8 7 .4825 125_68 3290.9 3690..6 7.7024
I
199
600 .2500 3293.3 3653.2 7.8080 .2220 3292.r 3691.7 7 .7 523 99,)60
3470.9 3917 .4 7.9487
700 .2794 3472.7 3919.7 8.0535 .2482 347r.8 3918.5 ? qoR'l
1
.
.

6. Table A.1.3 (Continued)
Superheated Vapor
800
900
1000
I 100
1200
1300
P: 1.60 MPa (201.41)
.3086 3658.3 4152.1 8.2808
8.4935
.337 7
3 85 0.5 4390.8
.3668 4049.0 4635.8 8.6938
.3958 4253.i 4887.0 8.8837
.4248 4464.2 5143.9 9.0643
.4538 4679.9 5406.0 9.2364
P
:2.50
MPa (223.99)
Sat. .079 98 2603.1 2803.1 6.2575
225 .080 27 2605.6 2806.3 6.2639
250 .087 00 2662.6 2880.1 6.4085
300 .098 90 2761.6 3008.8 6.6438
350 .109 76 2851.9 3126.3 6.8403
400 .120 10 2939.1 3239,.3 7.0148
450 .130 14 3025.5 3350.8 7,1746
500 .139 98 3l 12.1 3462.t 7.3234
600 .1 59 30 3288.0 3686.3 7.5960
700 .r7B 32 3468.7 3914.5 7.8435
800 .197 16 3655.3 4148.2 8.0720
900 .215 90 3847.9 4387.6 8.2853
1000 .2346 4046.7 4633.1 8.4861
1100 .2532 425r.5 4884.6 8.6762
1462.1 514t.7 8.8569
1200 .27 r 8
4677.8 5404.0 9.0291
l 300 .2905
P
:
P
.
1
.
.
P:6.0
6.2285
6.3615
6.5821
6.7690
6.9363
7.0901
7.3688
7.6198
7.8502
8.0647
8.2662
8.4567
8.6376
8.8100
MPa (275.64)
Sat. .032 44 2589.7 2784.3
300 .036 lri 2667.2 2884.2
350 .042 23 2789.6 3043.0
400 .047 39 2892.9 3t77.2
450 .05214 2988.9 3301.8
500 .056 65 3082.2 3422.2
550 .061 0r 3174.6 3540.6t
600 .065 25 3266.9 3658.4.
700 .07i1 52 3453.1 3894.2
800 .081 60 3643. r 4132.7
900 .089 58 3837.8 4375.3
1000 .097 49 4037.8 4622.1
1100 .105 36 4243.3 4875.4
.044 06
.047 30
47
24
93
.044
.048
16
14
7
.05
95
7.4234
7.6566
7.8727
8.0751
8.266
r
:4 5 uegz.+ot
2600.1 2798.3
2650.3 2863.2
l'J
98
r
6.0 t
6. t40
.039
:
.14
5.0 MPa (263.99)
2597
.l
2794.3
5.9734
.04r
3
.027
.029
.035
.039
I.roI /
2100 MPa (212.42)
11 263 t.3 2838.3 6.0544
.051 35 27 r2.0 2943.1
6.2828 .045 32 2698.0 2924.5 6.2084
.058 40 2B 17.8 3080.6
6.513 I
.051 94 2808.7 3068.4 6.4493
.064 7 b 2913.3 3204.7
6.7047 .0578r 2906.6 3 r 95.7 6.6459
.070 74 3005.0 3323.3
6.8746 .063 30 2999.7 3316.2 6.8186
.076 5l 3095_3 3439.6
7.030L_--O68 57 3091.0 3433.8 6.9759
.087 65
2 76.0 367 0.5
7.3110 .07869 3273.0 3666.5 7.2589
.098 47 3459.9 3903.0
7.563r .0BB 49 3457.6 3900.1 7.5122
.r09 1l 3648.3 4139.3
7.7942 .098i1 3646.6 4137 .l 7 .7 440 *
.119 65 3842.2 4380.6
8.009r .r07 62 3840.7 4378.8 7.9593
.130 l3 4041.6 4627 .2
8.2 108 .t t7 07 4040.4 4625 .7 B. l6 r 2
.140 56 4246.8 4879.3
8.4015 .126 48 4245.6 4878.0 8.3520
.150 98 4457 .5 5136.9
8.5825 . 135 87 4456.3 5135.7 8.5331
. 161 39
4673.1 5399.4 8.7549 .145 26 4672.0 5398.2 8.7055
P : 7.0 MPa (285.88)
P : 8.0 MPa (295.06)
5.8892
6.0674
6.3335
6.5408
6.7193
6.8803
.0288..
:
1
P
6.0701
P
1.80 MPa i207. I51
.2742 3657.6 4151.2 8.2258 .2467 3657.0 4 r 50.3 B. 1765
.3001 3849.9 4390.1 8.43 86 .27 00 3 849.3 4389.4 8.3895
.3260 4048.5 4635.2 8.6391 .2933 4048.0 4634.6 8.5901
.3518 4253.2 4886.4 8.8290 .3166 4252.7 4885.9 8.7800
.3776 4463.7 5143.4 9.0096 .3398 4463.3 5142.9 8.9607
.4034 4679.5 5405.6 9.18r8 .3631 4679.0 5405. r 9.1329
P: 3.50 MPa 1242.60)
P: 3.00 MPa (233.90)
.066 68 2604.1 2804.2
6.1869 .057 07 2603.7 2803.4 6.1253
6.2872 .058 72 2623.7 2829.2 6.1749
.070 58 2644.0 2855.8
6.5390 .068 42 2738.0 2977.5 6.446r
.081 l4 2750.1 2993.5
.09053 2843.7 3115.3 6.7428 .076 78 2835.3 3104.0 6.Orzs
.099 36 2932.8 3230.9
6.9212 .084 53 2926.4 3222.'3 6.8405
30i5.3 3337.2 7,0052
7 .0834 .091 96
07 87 3020.4 3344.0
.116 19 3108.0 3456.5
7.2338 .099 r 8 3103.0 3450.9 7.r572
7.5085 .l 13 24 3282.1 3678.4 7.4339
.t32 43 3285.0 3682.3
7.7571 .126 99 3464.s 3908.8 7.6837
.148 38 3466.5 3911.7
7.9862 .140 56 stsr.s 414J.7 7.gtz4
.164 14 3653.5 4145.9
8.1999 .154 02 3845.0 4384.r 8.1276
.179 80 3846.5 4385.9
8.4009 .167 43 4044.1 4630.1 8.3288
.195 41 4045.4 4631.6
8.5912 . 180 80 4249.2 4881 .9 8.5192
.210 98 4250.3 4883.3
8.7720 .194 15 4459.8 5139.3 8.7000
.226 52 4460.9 5140.5
8.9442 .207 4tl 4675.lt lt'lo l.l U.8723
.242 06 4676.6 5402.8
4.0 MPa (250.40)
S:rt. .049 78 ?602.3 2801 .4
275 .054 57 2667.9 2886.2
300 .058 8,1 2725.3 2960.7
350 .066 45 28?6.7 3092.5
400 .073 4l 2919.9 3213.6
450 .080 02 3010.2 3330.3
500 .086 43 3099.5 3445)'
600 .098 85r 3279.I 3674.4
700 . l0 95 3462.1 3905.9
800 .122 87 3650.0 4141.5
900 i 34 69 3843.6 4382.3
1000 .t46 45 1042.9 4628.7
r 100 . l5B 17 4248.0 4880.6
1200 .169 87 4458.6 5 i 38. i
1300 18 r 56 4671.3 5400.5
:
I
37
.tr55 r)5
.062 83
.069 8 t
.076 69
.083 50
.090 27
2580.5 2772.r
2632,2 2838.4
2769.4 3016.0
2878.6 3158.I
2978.0 3287.r
3073.4 3410.3
3167.2 3530.9
3260.7 3650.3
3448.5 3888.3
3639.5 4128.2
383
5.0 437 r.8
4035.3 4619.8
4240.9 4872.8
5.8133 .023 52
5.9305 .024 26
6.2283 .029 95
6.4478 .034 32
6.6327 .038 17
6.7975 .04t 75
6.9486 .045 r ri
7.0894 .048 ,{5
7.3476 .054 r.il
7.5822 .060 1)7
7.7591 .067 02
8.0020 .073 0 r
8.1933 .078 96
2569.8
2590.9
2747.7
2U63.8
2966.7
3064.3
3159.8
!254.4
3443.9
3636.0
2 75
8.0
2785.0
2987.3
3138.3
3272.0
3398.3
3521.0
3642.0
3882.4
4123.8
3832. l 4368.3
4032.8 4616.9
4238.6 4870.3
5.7 432
5.7906
6.1301
6.3634
6.555 r
6.7240
6.8778
7.0206
7.2812
7.5r73
7.7351
7.9384
8.r300

7. Table A.1.3 (Continued)
Superheated Vapor
7-
P
1200
.113
r
.t 2
300
Sat.
325
350
400
450
500
550
600
650
700
800
900
r 000
I 100
r200
1
:
6.0 MPa (275.64)
2l 4454.0 5133.3
06 4669.6 5396.0
P : 9.0 MPa (303.40)
.B
P
8.4474
.097
8.6199
.103
:
03 445r.7 5130.9 8.3747
77 4667.3 5353.7 8.5473
P : 10.0 MPa (31 1.06)
3343.6 3755.3
3439.3 3876.5
3632.5 4119.3
.059 50 3829.2 4364.8
.064 85 4030.3 4614.0
.070 16 4236.3 1867.7
.075 44 4447.2 5126.2
1300 .080 72 4662.7 5389.2
5.6772 .018 026 2544.4 2724.7
5.8712 .019 861 2610.4 2809.1
6.0361 .022 42 2699.2 2923.4
6.2854 .026 41 2832.4 3096,5
6.4844 .029 75 2943.4 3240.9
6.6576 .032 79 3045.8 3373.7
6.8142 .035 64 3144.6 3500.9
6.9589 .038 37 324t.7 3625.3
7.0943 .041 0r 3338.2 3748.2
7.2221 .043 58 3434.7 3870.5
7.4596 .048 59 3628.9 4rt4.8
7.6783 .053 49 3826.3 436r.2
7.882r .058 32 4027.8 4611.0
8.0740 .063 l2 4234.0 4865.1
8.2556 .067 89 4444.9 5123.8
8.4284 .072 65 4460.5 5387.0
1']:
P
Sat.
350
400
450
500
550
600
650
700
800
900
1000
1100
r
200
1300
.020 48
2557
.023 27
.025 80
2646.6 2856.0
2724.4 2956.6
2848.4 31 17.8
2955.2 3256.6
3055.2 3386.1
3152.2 351 1.0
.029 93
.033 50
.036 77
.039 87
.042 85
.045 74
.048 57
.054 09
l
42.r
3633.7
15.0 MPa (342.24)
.010 337 2455.5 2610.5
.011 470 2520.4 2692.4
5.3098
649 2740.7 2975.5
445 2879,5 3156.2
.020 80 2996.6 3308.6
.022 93 3104.7 3448.6
.024 91 3208.6 3582.3
.026 80 3310.3 37 t2.3
.028 6r 3410.9 3840.1
.032 10 3610.9 4092.4
.035 46 3811.9 4343.8
.038 75 1015.4 4596.6
.042 00 4222.6 4852.6
.04b 23 4433.8 5rr2.3
.048 45 4649.1 5376.0
P :25.0 MPa
5.88 r
.015
.018
375 .001 973
400 .006 004
425 .007 88 r
450 .009 162
500 .01 l 123
550 .0r2 724
600 .014 137
650 .0t5 433
700 .016 646
800 .018 912
900 .021 045
1000 .023 i 0
ll00
3248.
27
.025
12
1
t798.7
1848.0
2430.1
2609.2
2720.7
2884.3
3017.5
2580.2
2806.3
2949.7
3162.4
3335.6
3491.4
3137
.9
3251.6 3637 .4
3361.3 3777.5
3574.3 4047.r
3783.0 4309.1
3990.9 4568.5
4200.2 4828.2
.007
:
920 2390.2 2528.8
.0r2 447 2685.0 2902.9
6.1404 .0r5 174
6.3443 .017 358
6.5199 .019 288
6.6776 .021 06
6.8224 .022 74
6.9572 .024 34
7 .2040 .027 38
7 .4275 .030 3l
7.6348 .033 16
7.8283 .035 97
8.0108 .038 76
8.1840 .041 b4
2844.2 3109.7
2970.3 3274.1
3083.9 342r.4
3191.5 3560.1
3296.0 3693.9
3398.7 3824.6
3601.8 4081.1
3804.7 4335.1
4009.3 4589.5
4216.9 4846.4
4428.3 5106.6
4643.5 5370.5
P
4.0320
5.1418
5.4723
5.6744
5.9592
6.1765
6.3602
6.5229
6.6707
6.9345
7.1680
7.3802
7.5765
.001
.002
.005
.006
.008
789 2
790
303
735
678
.010 168
.011
.012
.013
.015
:30.0
.090
P
.013
1737.8
2067.4
2455.1
2619.3
2820.7
2970.3
5.9443 .016 126 2624.6 2826.2 5.71l8
6.2120 .020 00 2789.3 3039.3 6.0417
6.4190 .022 99 2912.5 3199.8 6.2719
6.5966 .025 60 302r.7 3341 .8 6.461B
6.7561 .028 0l 3125.0 3475.2 6.6290
6.9029 .030 29 3225.4 3604.0 6.7810
7.0398 .032 48 3324.4 3730.4 6.9218
7.1687 .034 60 3422.9 3855.3 7.0536
7.4077 .038 69 3620.0 4103.6 7.2965
7.6272 .042 61 3819.1 4352.5 7.5182
7.8315 .046 58 4021.6 4603.8 7.1237
8.0237 .050 4:5 4228.2 4858.8 7.9165
8.2055 .054 30 4439.3 5l I8.0 8.0987
8.3783 .058 t 3 4654.8 538 r.4 8.27 t7
P:20.0
r419
.005
5.7213 .009 942
6.0184 .012 695
6.2383 .014 768
6.4230 .016 555
6.5866 .018 178
6.7357 .0r9 693
6.8736 .021 r 3
7.1244 .023 85
7.3507 .026 45
7.5589 .028 97
7 .7
53r
7.9360
8.1093
.03 1 45
.033
3221.0
33 35.
37 45.6
.019 196
3555.5 4024.2
3768.5 4291.9
3978.8 4554.7
9l
.036 36
2619.3 2818. l 5.5540
2806.2 3060.1 5.9017
2542.9 3238.2 6. l40l
3062.4 3393.5 6.3348
74.0 3537.6
328r.4 3675.3
3386.4 3809.0
3592.7 4069.7
3797.5 4326.4
4003.1 4582.5
3r
42r | .3 4840
4422.8
4638.0
P
.020 903
4816.3
tB
MPa (365.81)
834 2293.0 2409.7 4.9269
5.1504 .003 428
5.4424 .004 96r
5.7905 .006 927
6.0342 .008 345
6.2331 .009 527
6.4058 .010 575
6.5606 .0ii 533
6.8332 .013 278
596
661
623
4i89.2
5.
26r4.2
3r
B
r2.5 MPa (327.89)
495 2505.1 2673.8 5.4624
3.9305 .001 700
3081.1
8.31 15
8.4842
5, / 5Crd
179r.5
446
00.5
-
2l5l.l 4.4728 .002 r 00
2821.4
MPa (295.06)
89 1449.5 5 128.5
B0 4665.0 5391.5
MPa
3275.4
3443.9
3598.9
.0r7 448
5.6r4r
.084
17.5 MPa (354.75)
5.442r
1
P:8.0
7.0 MPa (285.U8)
3
.2
5r01.0
5365. r
:35.0
r702.9
i 914. I
2253.4
2498.7
27 51.9
292 t.0
3062.0
3189.8
3309.8
3536.7
.0 14 BB3
37 54.0
7.2867 .016 4r0
7 .4845 .017 895
3966.7
7
.07
4r78.3
6.5048
6.6582
6.7993
7.0544*
7.2830
7.4925
7
.687 4
7.8707
8.0442
MPa
1762.4
1987.6
2373.4
2672.4
2994.4
32 13.0
3395.5
3559.9
37 13.5
3.8722
4.2126
400
6.7450
r.5
454t.t
4.7747
5.1962
5.6282
5.9026
6. r 179
6.30 i 0
6.463 I
1274.9 6.9886
7
.2064
4804.6 7.4057

8. Table A.1.3 (Continued)
Superheated VaPor
P
P
500
l)5u
600
650
700
800
I
900
000
I i00
I 200
I
300
P:30.0
MPa
.001 640 7
.001 907 7
.002 532
.003 693
.005 622
.006 984
.008 094
.009 063
.009 941
:40.0
P:50.0
MPa
1742.8
1854.6 1930.9
2096.9 2198.1
2512.8
2365.1
2678.4 2903.3
IOi /.
r
2869.7
3022.6
3158.0
3283.6
3517.8
3149.r
3.8290
4.r135
4.5029
4.9459
5.4700
5.7785
3346.4 6.01l4
3520.6 6.2054
368
r.2
6.3750
3739.4
.012 962
.014 324
,0t5 642
.016 940
.018 229
3978.7 6.6662
4257.9 6.9150
39b4.6
.01 1 523
4527
4167.4
4380. r
4594.3
.6
7.1356
4793,r 7 .3364
5057.7 7.5224
5323.5 7.6969
P
MPa
.001 559 4
.00r 730 I
.002 007
.002 486
.003 892
.005 I l8
.006 I 12
.006 966
.007 727
.009 076
.010 283
.011 411
.012 496
.013 561
.014 616
16.6 3.7639
1874.6 4.003.
1959,7 2060.0 4.2734
2159.6 2284.0 4.5884
2525.5 2720.t 5.1726
2763.6 3019.5 5.5485
2942.0 3247 .6 5.8178
3093.5 3441.8 6.0342
3230.5 3616.8 6.2189
3479.8 3933.6 6.5290
3710.3 4224.4 6.7882
3930.5 450r.1 7.0146
4t45.7 4770.5 7.2184
4359.1 5037.2 7.4058
4572.8 5303.6 7.5808
r7B8.
r
35,0 MPa
P:60.0
MPa
r638.6
:
4390.7 5068.3 7.5910
4605.1 5333.6 7.7653
4401.3 5079.0 7.6692 .019360
4616.0 5344.0 7.8432 .020 815
4412.0 5089.9 7.1605 .022 589
4626.s 5354.4 7.9342 .024 266
1200 .027 rr
1300 .029 10
375
400
425
450
:25.0
17
MPa
1699.5 3.7 r4r
1843.4 3.9318
2001.7 4.1626
1609.4
.001 502 B
.001 633 5
.001 B16 5
.002 085
.002 956
.003 956
.004 834
,005 595
.0p6 272
,007 459
.008 508
.009 480
.010 409
t745.4
1892.7
2r79.0 4.412
2053.9
2390.6
2658.8
286 l. I
3028.8
3t77.2
5.8829
6.0824
6.4109
6.6805
6.9127
1
r.5
4475.2
4748.6
4124.1
50t7
4338.2
4551.4
.012 215
5.344r
5.6452
3889.
419
3441.5
3681.0
3906.4
.01 1 317
4.932r
2567.9
2896.2
3151.2
3364.5
3553.5
7.1 195
.2
7.3083
5284.3 7.4837
Table A.1 .4
Compressed Liquid
1':5N4Pa(263.99)
P
: l0 MPa (31 1.06)
P:
15 MPa (342.24)
't
Sat. .00 I 285 9
0 .000 997 7
20 .000 999 5
40 .001 005 6
60 .001 014 !)
80 .001 026 8
100 .001 041 0
r20 .001 057 6
r40 .001 076 8
160 .001 098 B
r 80 .001 124 0
200 .001 r53 0
220 .001 186 6
240 .001 226 4
260 .001 274 I
280
300
320
340
1147.8 1t54.2
.00t 452 4
5.04
83.65 88.65
166.95 17 L97
250.23 255.30
t33.72 338.85
2.9202
.0001
.2956
.5705
.8285
1.0720
417.52 422.72 1.3030
501.80 507.09 1.5233
586.76 592. l5 1.7343
672.62 678. r 2 t.9375
759.63 765.25 2.1341
848.1 853.9 2.3255
938.4 944.4 2.5128
t031.4 1037.5 2.6979
r 127.9 1134.3
2.8830
.000
.000
.001
.001
.001
.04
995
997
2
003 4
012
024
.00r 038
.001
2
7
5
5
054I
.00r 073 7
.001 095
3
.001 119 9
.001 148 0
.001 180
.001
.001
.001
.001
218
5
7
264
5
321 6
397
2
1393.0
.09
83.36
1407.6
10.04
93.33
166.35 176.38
249.36 259.49
332.59 342.83
4t6.r2
426.50
500.08 510.64
584.68 595.42
670.r3 681.08
756.65 767.84
844.5 856.0
934.1 945.9
1026.0
ll2l.l
1220.9
1328.4
1038.
r
t133.7
1234.1
1342.3
3.3596
.0002
.2945
.5686
.8258
1.0688
1.2992
1.5189
1.7292
1.9317
2.1275
2.3178
2.5039
2.6872
2.8699
3.0548
3.2469
.001
.000
.000
.001
.001
.001
.001
.001
.001
.001
658 I
992 8
995 0
001 3
010 5
022
2
036 I
052 2
070 7
091
B
.001 r15I
.001 r43 3
.00r
174 8
.001 2ll4
.001 255 0
.001 308 4
.001 377 0
.001 472 4
631 1
..001
1585.6
.15
83.06
1610.5
15.05
3.6848
.0004
97.99
.2934
165.76 r 80.78
i
r.48
4t4.7 4
48.5
33
2
498.40
582.66
263.67
346.81
430.28
514.19
598.72
.5666
.8232
1.0656
t.2955
t.5t45
| 1r4,)
667.7r .684.09
1.9260
753.76 770.50
2.12r0
2.3t04
841.0 858.2
929.9 947.5
1020.8 r039.0
il r4,6 133.4
t212.5 1232.1
13 r 6.6 1337 .3
t43t.1 1453.2
1567 .5 159 r.9
1
2.4953
4.677 r
4.8576
3.0393
3.2260
z+247
3.6546
*

9. Table A.1.4 (Continued)
Compressed Liquid
P:20
P:
MPa (365.81)
P:
30 MPa
50 MPa
T
Sat.
.002 036
0 .000 990 4
20 .000 992 8
40 .000 999 2
60 .001 008 4
80 .001 019I
100 .001 033 7
r20 .001 049 6
140 .001 067 8
160
180
200
220
240
260
280
300
320
340
360
.001088 5
.001 I 12 0
.001 138 8
.001 169 3
.001
.001
.001
.001
.001
.001
204
246
296
359
443
568
.00r 822
1785.6
.19
82.77
I05.l /
247.68
330.40
413.39
496.76
580.69
tlb5.J5
7
50.95
837.7
925.9
016.0
6
t
2
1108.6
5
t204.7
6
I
7
14t5.7
4
1539.7
1702.8
6
306.1
1826.3 4.0139
20.01 .0004
102.62 .2923
185.r6 .5646
267.85 .8206
350.80 l.0624
434.06 r.2917
6 1.5 102
.04 | .7 r93
687. r 2 1.9204
5r7
.7
602
773.20 2.1147
860.5 2.3031
949.3 2.4870
1040.0 2.6674
1133.5 2.8459
1230.6 3.0248
1333.3 3.2071
1444.6 3.3979
1571.0 3.6075
1739.3 3.8772
380
Table
.25
.000 985 6
.000 988 6
.000 995 l
.001 004 2
.001 015 6
.001 029 0
.001 044 5
.001 062 I
.001 082 1
.00r 104 7
.001 130
.00i
29.82
82.17 I I 1.84
164.04 193.89
246.06 276.r9
328.30 358.77
410.78 44r.66
493.59 524.93
576.88 608.75
660.82 693.28
745.59 778.73
.0001
.2899
.5607
.8r54
1.0561
t.2844
1.5018
1.7098
1.9096
2.1024
831.4 865.3 2.2893 .001 I l4
2
159 0
.001 140
8
9
18.3
953. I
.001 230 3
.00r 275 5
.001 330 4
.001 399 7
.001 492 0
.001 626 5
.001 869 I
l190.7
1229.0
1287.9
1390.7
1501.7
1626.6
l 78 I
1327 .8
2.47rr
3.r74r
3.3539
3.5426
167 5.4 3.7494
1837.5 4.0012
.4
735.69 790.25 2.0794
819.7 875.5 2.2634
904.7 961.7 2.4419
990.7 1049.2 2.6158
1078.r 1138.2 2.7860
1t67.2 1229.3 2.9537
1258.7 1323.0 3.1200
1353.3 1420.2 3.2868
1452.0 1522.r 3.4557
1556.0 r630.2 3.6291
t667.2 1746.6 3.8101
2.6490 .001 170 2
2.8243 .001 203 4
2.9986 .001 241 5
1432.7
1546.5
.001
.001
.001
.001
.001
49.03 -.0014
1.00 130.02 .2848
r61.86 211.21 .5527
242.98 292.79 .8052
324.34 374.70 1.0440
405.88 456.89 r.2703
487.65 539.39 r.4857
569.77 622.35 1.6915
652.4t 705.92 1.8891
B
6
1006.9 1042.6
1097.4 l 134.3
.001 192 0
.20
.000 976 6
.000 980 4
.000 987 2
.000 996 2
.001 007 3
.001 020 I
.001 034 8
.001 051 5
.001 070 3
.001 091 2
286 0
338 8
403 2
483 8
588 4
A.1 .5
Saturated Solid-Vapor
lnternal Energy
Specifrc Volume
'lemp. Press. Sat. Sat.
oC
kPa Solid Vapor
P ziX103
T
7)o
.0i
0
-2
-4
-6
-8
- l0
-12
* t4
* 16
- 1B
-20
*22
-24
-26
-28
-30
*32
-34
-36
-38
-40
1.0908 206. I
1.0908 206.3
,5t76 1.0904 241.7
1.0901 283.8
.4375
.3689 1.0898 334.2
.3102 1.0894 394.4
Sat.
Solid
Enthalpy
Sat.
Subl. Vapor
ltis
Ui
08.7
08.8
Sat.
Solid
1ls
Sat. Sat.
Subl. Vapor Solid
hin
hi
2834.8
2834.8
2710.2 2372.6 -337.62 2835.3
*341.78 2835.7
-34t.7 B 271r.6 2369.8
2712.9 2367 .0 -345.91 2836.2
-345.91
-350.02 2714.2 2364.2 -350.02 2836.6
.2602 l.0891 466.7 -354.09 2715.5 2361.4 -354.09 2837.0
.2176 1.0888 553.7 -358.14 2716.8 2358.7 -358.14 2837.3
. 1815
1.0884 658.8 -362.15 2718.0 2355.9 -362.r5 2837.6
. 1510
1.088I 786.0 -366. r4 2719.2 2353.1 -366.14 2837 .9
.1252 1.0878 940.5 -370.10 2720.4 2350.3 *370. l0 2838.2
.1035 1.0874 1 128.6 -374.03 2721.6 2347.5 -374.03 2838.4
*377.93 2722.7 2344.7
.0853
1 .0871 1358.4
-377.93 2838.6
.0701
1.0868 1640.1 -381.80 2723.7 2342.0 -381.80 2838.7
.057 4 1.0864 1986.4 -385.64 2724.8 2339.2 -385.64 2838.9
.0469 t.0861 2413.7 -389.45 2725,8 2336.4 -389.45 2839.0
.038I 1.0858 2943
-393.23 2726.8 2333.6 -393.23 2839.0
.0309 1.0854 3600
-396.98 2727.8 2330.8 -396.98 2839.1
.0250 1.0851 4419
-400.7 t 2728.7 2328.0 -400.7 | 2839.1
.0201
1.0848 5444
-404.40 2725.6 2325.2 -404.40 2839.1
.0i61 1.0844 6731
-408.06 2730.5 2322.4 -408.06 2839.0
.0 I 29
r.0841 8354
-4tt.70 273r.3 2319.6 -4t 1.7 0 2838.9
.61 13
.6108
-333.40
-333.43
-337.62
27
2 7
237 5.3
237 5 .3
-333.40
-.)
3 J.
a.l
Entropy
Vapor
i
ris
J9
1.221
10.378
10.378
10.456
10.536
h!
2501.4
250r.3
2497.7
2494.0
2490.3
2486.6
2482.9
2479.2
2475.5
247 r.8
.f
-
Sat.
Subl.
-1.221
- .237
- .253
- r.268
- 1.284
- .299
- .315
- 1.33 r
1
1
r
9.1 56
Y.L5/
9.219 *
9.283
9.348
0.616
10.698
10.781
9.414
1
1
i
-1.346
0.865
r 0.950
r.036
-t.377
r.2r2
9.550
9.619
9.690
9.762
9.835
9.909
9.985
l.
9.481
2468.1
2464.3
-
2460.6
2456.9
2453.2
244s.5
2445,8
- 1.393
* r.408
* t.424
- 1.439
1.302
1.394
2442,1
-L47|
- 1,486
- I .501
*
t.t t3
| .51 I
r2.073
r
-1.532
12.176
t0.644
2438.4
2434.7
2430.9
2427,2
1.362
- r.+55
123
l.486
r,580
r.676
t.872
r.972
10.062
i0.l4r
10.221
10.303
10.386
r0.470
0.556

10. Table A.2
Thermodynamic Properties of Ammoniau
Table A.2.1
Saturated Ammonia
Specific Volume
Enthalpy
kJ/kg
m'/kg
Abs.
Evap.
kPa
OC
Liquid
a1
Sat.
Vapor
7)s
Sat.
Press.
Temp.
ule
D
40.88
45.96
-5r.J
*48
-46
_A A
J 1.55
5 i.b9
64.42
-al
-40
-38
79.80
88.54
98.05
-JO
-34
*32
-30
-28
-26
*24
-22
-20
108.37
I 19.55
131.64
144.7 0
158.78
r73.93
190.22
-i8
207 .7
246.5
290.85
3r5.25
34r.25
-8
-6
-+
-z
0
2
4
6
B
14
t6
t8
20
22
24
26
28
30
32
34
36
3B
40
42
44
46
48
50
i
267.95
-10
l0
l2
|
226.45
-16
*14
-12
,
368.90
358.27
429.44
462.49
497.49
534.5r
5/.r.oat
614.95
658.52
704.44
752.79
803.66
857.12
913.27
972.r9
0.001
0.001
0.001
0.001
0.001
0.001
0.00 i
0.001
0.001
0.001
0.001
0.001
0.001
0.00 i
0.001
0.001
0.001
0.001
0.001
0.001
424
429
434
439
444
449
454
460
465
470
476
481
487
492
498
504
510
515
52r
528
0.001 534
0.001 540
0.001
0.001
0.001
0.001
546
553
559
566
0.001
0.001
0.001
0.001
573
580
587
594
0.001 601
0.00 r 608
0.00i 616
0.001
0.001
0.001
0.001
0.001
623
631
639
647
655
i 033.97
0.001 663
1098.71
r 166.49
1237.41
0.001 671
0,001 680
0.001 689
t3I1.55
0.00
1389.03
0.001 707
0.001 716
1469.92
1554.33
1642.35
1734.09
1829.65
1929. i3
2032.62
0.00
r 698
r 726
0.001 735
0.001 745
u.t)u
I
/ 5r)
0.001 766
0.001 777
2.6239 2.6254
2.3518 2.3533
2.1 126 2.rr40
1.9018 1.9032
.7 r55
r.7 t7 0
1.5506 i.5521
r.4043 i.4058
|.2742 1.2757
1 1582 l.1597
1.0547 1.0562
0.9621 0.9635
0.8790 0.8805
0.8044 0.8059
0.7373 0.7388
0.6768 0.6783
0.6222 0.6237
0.5728 0.57 43
0.5280 0.5296
0.4874 0.4889
0.4505 0.4520
1
Entropy
kJ/kg K
Sat.
Sat.
Liquid
ht
Sat.
Vapor
Liquid
ho
Evap.
j,
L
-44.3
-35.5
-26.6
- r 7.8
-8.9
0.0
8.9
17.8
26.8
35.7
44.7
53.6
62.6
7r.6
80.7
89.7
98.8
r07.8
l r6.9
126.0
1372.4 -0.1942
t4t6.7
1411.3
1405.8
1400.3
r
t394.7
1389.0 0.0000
1392.2 0.0380
1395.4 0.0757
1398.5 0. I I32
1401.6 0.1504
1404.6 0.1873
t407.6 0.2240
1410.5 0.2605
r4r3.4 0.2967
1416.2 0.3327
r419.0 0.3684
t42r.7 0.4040
1424.4 0.4393
1427.0 0.4744
1429.5 0.5093
1383.3
1377.6
1371.8
365.9
1360.0
1354.0
1347.9
1341.8
1335.6
1329.3
1322.9
1316.5
13t0.0
1303.5
0.4169
0.3863
0.3583
0.3328
0.3094
0.2879
0.2683
0.2502
0.2335
0.2182
0.2040
0.1910
0.1789
0 .167 7
0.41 85
r35.2
r
144.3
I
296.8
290. I
1432.0
0.3878
0.3599
0.3343
0.3109
0.2895
I CJ.5
1283.3
1276.4
1436.8
1439.1
269.4
r44t.3
t262.4
t255.2
t443.5
0.1477
0.1388
0. 1305
0.1228
0.1 156
0.1089
0.1027
0.0969
0.0914
0.0863
0.08i5
0.077 |
0.0728
0.0689
0.0652
0.0617
0.1494
0.r574_-
0,2698 ,
0.2517.
0.235IJ
0.2198
0.2056
0.1926
0.1805
0. I 693
0. r590
0.
r405
0.t322
0.1245
0.1 173
0.1 106
0.1044
0.0986
162.7
171.9
181.1
190.4
199.6
208.9
218.3
227.6
237.0
246.4
255.9
265.4
274.9
284.4
294.0
303.6
1218. I
1.t55.
1210.4
1202.6
194.7
186.7
178.5
1456.8
1458.5
1460.0
170.3
t464.3
162.0
153.6
145.0
136.4
127.6
118.7
109.7
1465.6
1466.8
1467.9
00.5
1472.2
1091.2
r472.8
391.5
401.5
108 r .7
1473.2
r072.0
t+t.).5
4rt.5
1062.2
1052.0
r47 3.7
3t3.2
322.9
332.6
342.3
0.0880
0.0833
0.0788
37
38
"Adapted from National Bureau of Standards Circular No. 142,
t240.6
1445.6
1447.6
1449.6
145I.5
352.1.
0.0707
0.0669
0.0635
1248.0
r434.4
1233.2
1225.7
0.0931
0.0746
r
361.9
r.7
r.6
421.7
TabLes
1
-0.1547
1379.2 -0. I 156
1382.5 -0.0768
1385.8 *0.0382
i 389.0
I
375.8
1453.3
_t
146 l .5
r
462.9
r469.0
1469.9
1470.8
r47 t.5
r473.7
of Therrnotlynamic Properties
Evap.
Sat.
Vapor
sfs
Js
6.3502 6. l56l
6.2696 6.1.149
6. 1902 6.0746
6. I r20
6.0352
6.0349 5.9967
5.9589 5.9589
5.8840 5.9220
5.8101 5.8858
5.7372 5.8504
5.6652 5.8156
5.5942 5.7815
5.5241 5.748r
5.4548 5.7 r53
5.3864 5.6831
5.3188 5.6515
5.2520 5.6205
5.1860 5.5900
5.1207 5.5600
5.0561 5.5305
4.9922 5.5015
0.5440 4.9290 5.4730
0.5785 4.8664 5.4449
0.6128 4.8045 5.4t73
0.6469 4.7432 5.3901
0.6808 4.6825 5.3633
4.6223 5.3369
0.7 r45
0.7481 4.5627 5.3108
0.7815 4.5037 5.2852
4.4451 5. 5 99
0.8 48
0.8479 4.387 | 5.2350
0.8808 4.3295 5.2 104
0.9136 4.2725 5.1861
0.9463 4.2159 5. 1621
0.9788 4.1597 5. 1385
1.0112 4.1039 5.lr5l
t.0434 4.0486 5.0920
1.0755 3.9937 5.0692
1.1075 3.9392 5.0467
1.1394 3.8850 5.0244
1.1711 3.8312 5.0023
1.2028 3.7777 4.9805
r.2343 3.7246 4.9589
1.2656 3.6718 4.9374
n2969 3.6192 4.9161
1.328 r
3.5669 4.8950
1.3591 3.5148 4.8740
1.3901 3.4630 4.8530
1.4209 3.4112 4.8322
1.4'518 3.3595 4.81 l3
1.4826 3.30',19 4.7905
1.5135 3.2561 4.7696
1
oJ Ammonta.
2

11. Table 4.2.2
Superheated Ammonia
Abs. Press.
Temperature,
kPa
oC
(S:rt. Temp.)
OC
-20
h
(-46.54)
J
u
75
h
(-3e. l8)
s
a
100
h
(-33.61)
J
125
a
h
(*29.08)
.t
u
150
h
(-25.23)
J
|
u
200
(- 18.86)
250
0.6199
h
1465.5
5.6863 5.7737
0.491 0 0.5135
1436.6
1461.0
5.5609 5.6517
0.4243
a
h
(-13.67)
u
300
i456.3
h,
(*9.23)
.t
350
s
u
h
.
u
450
h
(r.26)
J
20
500
(,1. 14)
600
(9.29)
70()
(13.81)
800
( 17.86)
7/
h
.'
7)
h
r
7/
h
.'
u
h
J
u
900
(21.54)
L
.t
a
000
(24.9 l )
1
1
200
(30.96)
0.700r 0.726r 0.75r9
1488.4
1510.9 1533.2 1555.5 t5t Lt
5.9342 6.0091 6.0813 6.1512
0.5568 0.5780 0.5989 0.6196
1 5 5 2.9 r57 5.4
r 507.6 1530.3
5.8165 5.8928 5.966 r 6.0368
0.4613 0.4192 0.4968 0.5 r43
t504.2 r527.4 1550.3 r573.0
5.7186 5.7563 5.8707 5.9423
0.3929 0.40B6 0.4239 0.4391
5.8559
0.5354
t484.5
5.7365
0.4430
r480.6
h
J
u
h
.
5t,
40
30
60
0.2698 0.2813 0.2926 0.3036 0.3144
1489.9 1515.0 1539.5 1563.4 1587. I
5.43t1 5.5157 5.5950 5 6704 r.7425
0.2217 0.237 t.2414 u.2508 0.2600
1482.4 1508.6 1533.8 1558.5 1582.7
5.3222 5.4102 1t.4923 5.5697 5.6436
0. 187,1 0. 1963 0.2048 0.2 l3 I 0.2212
1474.5 1501.9 1528. i t553.4 1578.2
5.2259 5.3 I 79 5.4029 5.4826 5.558'.
0.1615 0.1696 0.1773 0.1848 0.1920
1466.3 1495.0 1522.2 r548.3 1573.7
5.1387 5.2351 5.3232 5.4053 5.4827
0.1488 0.1559t 0.t627 0. 1693
1488.0
5. I 593
0.1321
1480.6
rsr6.2 |543.0
I569.I
5.2508 5.3354 5.4r47
1388;,.0.t450 0. l5ll
1510.0 1537 .7 1564.4
5.0889 5.1840 5.2713 5.3525
0.
0.il29 0.il85 0.1238
1497 .1 1526.6 1554.7
5.0629
5.
1560
5.2416
1524.4
5.7
0.7774
1547.6
70
60
5U
2.8473 2.9464 3.0453 3.1441
t520.4 154t.7 1563.0 1584.5
6.6360 6.7073 6.7766 6.844r
1.8932 r.9597 2.0?61 2.0923
1518.9 1540.3 1561.8 1583.4
6.4339 6.5058 6.5756 6.6434
1.4160 r.4664 1.5165 1.5664
r5r7.3 1538.9 1560.5 1582.2
6.2894 6.3618 6.432t 6.5003
1.1297 l . 1703 1.2107 1.2509
r 559.3 1581. l
l5_t5./ I5J/.J
6.1763 6.2494 6.3201 6.3887
0.9388 0.9729 1.0068 1.0405
1514.1 1536. l 1558.0 1580.0
6.0831 6.1568 6.2280 6.2970
1451.5 147 6.5 1500.7
5.4600 5.5502 5.6342
0.3 1 25 0.327 4 0.3417
t146.5 472.4 1497.2
5.3803 5.4735 5.5597
0.2752 0.2887 0.3017
t441.3 1468.I 1493.6
5.3078 5.4042 5.4926
h
(*5.35)
40
30
0.6738
5.5493 5.6366
0.3605 0.3770
1)
400
(- 1 .8e)
0.647
t442.0
J
20
IO
10
2.4474 2.5481 2.6482 2.7479
1435.8 1457.0 t47B.l 1499.2
6.3256 6.4077 6.4865 6.5625
1.6233 1.6915 1.7591 r.8263
1433.0 1454.7 1476.r 1497.5
6.1 190 6.2028 6.2828 6.3597
l.2ll0 1.2631 r.314b 1.3654
1430.1 1452.2 147 4.r 1495.7
5.9695 6.0552 6. r366 6.2144
0.9635 1.0059 r.0476 1.0889
1427.2 1449.8 t4'72.0 1493.9
5.85 r 2 5.9389 6.0217 6. r 006
0.7984.0.8344 0.8697 0.9045
1424.1 1447.3 1469.8 1492.1
5.7526 5.8424 5.9266 6.0066
u
50
-
3.2427
1606.
r
80
3.34 I 3
1627.8
100
3.4397
r649.7
6.9099 6.9743 7.0372
2.
1
584
1
2.2244 2.2903
1626.9
1648.9
6.7096 6.7742
6.8373
1605.
163
1.7155 1.8145
1648.0 1692.6
6.5668 6.6316 6.6950 6.8177
1.2909 r.3309 | .37 07 t .450 I
1603.0 1625.0 1647 .2 l69l .B
6.4555 6.5206 o)se+z 6.7072
| .07 40 1 .r07 4 1.1408 1.2072
1602.0 t624,1 1646.3 l69l.l
6.3641 6.4295 6.4933 6.6167
0.8029 0.8282 0.8533 0.9035
1599.9 1622.2 1644.6 1689.6
6.2189 6.2849 6.3491 6.4732
0.640 r 0.6605 0.6809 0.7212
1597.8 1620.3 1642.8 1688.2
6. 1052 6.r717 6.2365 6.3613
0.53 r 6 0.5488 0.5658 0.5997
1595.7 16r8.4 r64l.r 1686.7
6.01 r 4 6.0785 6.1437 6.2693
0.45,1I 0.4689 0.4837 0.5129
I .6
1604.
1570.7
t35 5.7890 5.8615
r
r
.6659
1626.0
1593.6
r639.3 1685.2
6.0647 6. 19 t 0
0.4220 0.4478
1616.5
5.93
5.9990
0.4090
r
4
0.3959
r591.r1 1614.5 I 637.6 I 683.7
5.6405 5.7 r73 5.7907 5.8613 5.9296 5.9957 6.1228
0.3143 0.3266 0.3387 0.3506 0.3624 0.3740 0.3971
1542.2 1565.9 1589.3 1612.6 1635.8 1682.2
1518.2
5.5752 5.6532 5.7275 5.7989 5.8678 5.9345 6.0623
0.3556
1521.3
70
0.3692 0.3826
1544.9 1568.3
t00
80
i60
140
120
180
0.3251 0.3357 0.3565 0.3771 0.3975
i610.6
1634.0
r
680.7
17 27
.5
5.8120 5.8793 6.0079 6. I 30 I
0.269 r. 0.278 r 0.2951 0.3 130
1606.6 1630.4 ),677.7 1724.9
5.7 t44 5.7826 5.9129 6.0363
0.229r 0.2369 0.2522 0.2672
1602.6 1626.8 1674.6 1722.4
5.6303 5.6997 5.8316 5.9562
0.199 l 0.2060 0.2196 0.2329
1598.6 1623.1 1671.6 1719.8
5.5562 5.6268 5.7 603 5.886 I
0.r7 57 0. l 820 0.1942 0.2061
t594.4 1619.4 1668.5 17 17 .1
5.4897 5.56r4 5.6968 5,8237
0. r 570 0.1627 0.1739 0.1847
1590.3 1615.6 1665.4 17 r4.5
5.4292 5.5021 5.6352 5.7674
0.1289 0.1338 0.1434 0.1526
1581.7 1608.0 1659.2 r 709.2
5.3215 5.3970 5.5379 5.6687
|
-a A a
6.2472
0.3302
1772.4
ti.l54l
.
0.2821
17 7 0.2
6.07,19
0.2459 0.2589
1768.0 1816.4
6.0057 6.1202
0.2 i
78
0.2294
176tt.7 1814.4
5.9442 6.0594
0.1954 0.2058 0.2162
t763.4
18 t
2.4
1861.7
5.BBB8 6.0047 6.1 159
0.16r6 0.1705 0.1792
r 758.9 1808.5 1858.2
5.79r9 5.9091 6.0214
.

12. able 4.2.2 (Conl.inued)
Superheated Ammonia
T
Abs. Press.
Temperature, "C
kPa
(Sat. Temp.)
1400
h
U
I
.t
u
1
800
h
(45.39)
40
70
15
80
132
u
h
.t
4.97
r40
r20
100
0,1297 0.1376
0.1452
1804.5
5.8273
0.1 125 0.1 195 0.1263
1698.5 17 49.7 1800.5
j.5084 5.6355 5.7555
'0.0992 0.1055 0.1 1 l6
1693.1 t745.1 1796.5
5.4409 5.5699 5.6914
0.0885 0.0943 0.0999
r687.6 1740.4 1792.4
5.3793 5.5104 5.6333
0.1
1573.0
1652.8
r 703.9 r7 54.3
5.4501 25.5836 /5.7087
5.1419
0.0820
1600.2
5.3053
0.0977
r 592.3
5.2232
0.0856
1554.6
1584.
I639.8
5.2270
0.0937
1564.0
l
0.1216
r60
0.1088
0.1053
1646.4
5.3722
0.0926
5.1482 5.30i8
0.0688
0.0760 0.0824
r47 6.r
1512.0 1544.9 1575.6 r633.2
4.7834 4.8930 4.9902 5.0786 5.237 |
4.8693
0.0648
.t
2000
(4e.38)
60
5(.'
0.0944 0.0995 0.1042
1483.4 r515.1 1544.7
4.9534 5.0530 5.1434
0.0851 0.0895
1502.9
1534.4
4.9584 5.0543
0.0739 0.0781
i 490.0
1523.5
J
600
(4 r .05)
30
u
h
(36.28)
20
5.0635
0.0725
180
0.1528
1854.7
5.9406
0.1330
1851.2
5.8699
Q.lr77
1847 .7
5.8069
0.1054
1844.1
5.7499
Table A.3
Thermodynamic Properties of Freon-12 (Dichlorodifluoromethane)"
Table A.3.1
Saturated Freon-l2
Entlopy
kJ/kg K
Enthalpy
kJ/kg
Specific Volume
m3/kg
Abs.
-I'ernp.
.CP
-90
-85
-80
-7 5
-70
-65
-60
-55
-50
-45
-40
-35
-30
-25
-20
-15
* l0
-5
0
5
Press
Sat.
Sat.
Sat.
Sat.
Sat.
MPa
Liquid
Evap.
Vapor
Liquid
Evap.
Vapor
Liquicl
u!
als
ltt
ht
h,,,
h,,
.S1
0.0028
0.0042
0.0062
0.0088
0.0123
0.0168
0.0226
0.0300
0.0391
0.0504
0.0642
0.0807
0.
i004
0.1237
0.1509
0.1826
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.2 191
0.000
0.2610
0.3086
0.3626
0.000
0.000
0.000
608
612
617
622
627
632
637
642
648
654
659
666
672
679
685
693
700
708
716
724
4.4t4
937
4.115 545
3.036 704
2.137 728
3.037
1.537 030
r.126 654
1.537 651
1.127 280
0.840 534
0.637 274
0.841 166
0.490 358
0.382 457
0.302 029
0.241 251
3 16
2.r38 345
0.637 910
0.491 000
0.383 105
0.302 682
0.24
r 910
0.194 732
0.195 398
0.r58 703
0.159 375
0.131 i66
0.108 847
0.091 0l B
0.130 487
0.108 162
0.090 326
0.075 946
0.064 255
0.054 673
0.046 761
0.076 646
0.064 963
0.055 389
0.047 485
-43.243
*38.968
-34.688
-30,401
103
1.793
-26.
-2
*17.469
-13. 129
-8.772
r
89.6
I
B
I
185.6
2
183.625
r81.640
179.651
r53.224
177
160. I 84
.653
t75.641
r73.611
155.536
157
.857
162.512
171.558 r67.r63
8.854
r74.076
4.416
13.315
17.800
22.3t2
26.851
31.420
36.022
40.659
t69.479
167.368
165.222
r63.037
160.810
158.534
156.207
153.823
151.376
148.859
185.243
187.397
189.518
0.75
r
9
0.1418
0. I 585
0.535
0.0187
'
.
0.8051
0.7779
0.7269
0.7027
0.6795
0.6570
0.6352
0.6141
0.5936
0.5736
0.5542
-0.0000
r7 r.784
l83.058
34
-0.0190
169.479
176.352
178.610
180.846
0.83
-0.058I
-0.0384
164.840
-4.396
-0.000
rs
-0.0782
48.640
0.0371
0.0552
0.0730
0.0906
0. l 079
0. I 250
Sat.
Vapor
f,l
1.0352
0.9970
0.9609
0.9266
0.8940
0.8630
-0.2084
-0. 1854
*0. 1630
150.9?4
r
r
-0.141I
-0.1 197
*0.0987
146.37 5
187.608
Evap.
r
0.8268
0.8I l6
0.7979
0.7855
0.7744
0.7643
0.7 552
0.7470
0.7396
0.7329
0.7269
0.7214
0.7165
0.7
r2r
0.7082
0.7046
0.7014
0.6986
0.6960
0.6937

13. Table A.3.1 (Continued)
Specific Volume
E,nthalpy
rn3/kg
'fernp.
"CP
l0
r5
20
25
30
35
40
45
50
55
60
65
70
75
B0
85
90
95
t00
t05
t10
t12
Abs.
Pless
MPa
Sat.
k
Entr'opy
kf/ks
]/ks
Sat.
Sat.
Sat.
Sat..
t.iquicl
Evap
Vapor
Liquid
Evap.
Vapor
UJ
tfs
Liquid
Tt
hl
hr,,
h,r
0.034 67 r
0.030 028
0.65 r 6
0.000 733
0.000 743
0.000 752
0.000 763
0.026 09 r
0.7 449
0.000 774
0.022 734
0.847 7
0.000 786
0.000 798
0.000 81 I
0.000 826
0.0i9
K
0.4233
0.4914
0.5673
0.9607
1.084y
1.2 I 93
1.3663
1.5259
1.6988
i.8858
2.087 4
2.3046
2:5380
2.7885
3.0569
0.000
8.11
0.000 858
0.000 877
0.000 897
0.000 920
0.000 946
0.040 180
855
0.017 373
0.015 220
0.0r3 344
0.01 1 701
0.010 253
0.008 97 i
0.007 828
0.006 802
0.005 875
0.000 976
i
0.005 029
0.00
012
0.001 056
0.004 246
3.3140
0.001 I 13
0.002 790
3.6509
3.9784
0.001 197
0.002
0.001
0.000
4.
I
155
0.001 364
0.001 792
0.003 508
0.040
0 035
914
413
45.337
t46.265
50.058
54.828
59.653
64.539
69.494
7 4.527
79.647
84.868
143.586
140.812
780
854
0.023 508
0.020 641
0.018 l7l
0.016 032
0.014 170
0.012 542 90.201
0.011111 95.665
0.009 847 I01.279
0.008 725 107.067
0.007 723 I13,058
0.006 82r 1t9.291
0.006 005 I 25.818
0.005 258 132.708
0.004 563 140.068
0.003 903 I48.076
0.030
0.026
045 0.003 242
098 0.002 462
005 0.001 797
I 5 /.Ud5
168.059
17
4.920
r37
.933
srq
191.60?
193.644
195.641
197.586
199.475
134.936
t 3 1.805 201.299
128.525 203.05 t
125.074 204.722
121.430 .-f0o.zse
l
7.565
Evap.
Sat.
Vapor
Jq
0.1750 0.5165 0.6916
914 0.4983 0.6897
0.2076 0.4803 0:6879
0.2237 0.4626 0.6863
0.2397 0.4451 0.6848
0.2557 0.4277 0.6834
0.27 16 0.4104 0.6820
0.2875 0.3931 "0.6806
0. r
0.3
034
0.3
758
0.6792
r.658
r.768
211.726
209.843
0.3194 0.3582 0.6777
0.3355 0.3405 0.6760
0.35 I8 0.:224 0.6742
0.3683 0.3038 0.6721
0.3851 0.2845 0.6697
0.4023 0.2644 0.6667
0.420 I
0.2430 0.663
0.4385 0.r20() 0.6585
0.4579 0.1946 0.6526
0.4788 0. r 655 0.6444
49.014
28.425
206.099
0.5023
0. I
196.484
0.5322
0.07
175.07r
0.5651
l
207
.7
66
113.443 209.109
r09.024 2r0.303
104.255 2l 1.321
99.068 212.126
93.373 212.665
87.047 212.865
79.907 212.614
7
6
0.151
1
296
42
0.0004
',Copyright 1955 and 1956, E. I. du Pont de Nemours & Conrpany, Inc. Reprinted by pernlission. Adapted f rrrrn linglish unit.s
0.63
l9
0.6064
0.5655

14. Table A.3.2
Suoerheated Freon-12
'I"emp.
u
h
s
u
h
J
kJ/kg
kJ/kg K
m'/kg
kJ/kg
kJikg K
m3/kg
0.05 MPa
-20.0
- 10.0
0.0
10.0
20.0
30.0
40,0
50.0
60.0
70.0
80.0
90.0
0.341
0.3s6
0.370
0.384
0.398
0.10 MPa
181.042
0.79).2
/
0.8133
0.8350
0.8562
0.8770
0.8974
0.9175
857
227
508
716
863
0.412 959
204.469
210.557
0.427 0r2
2r6.733
0.441 030
222.997
229.344
0.455
0.468
0.482
0.496
0r7
978
917
838
rt1r). t 5
192.567
198.471
0.9372
242.282
0.9565
0.9755
0.9942
248.868
1.0126
235.77 4
0.167
0.175
0.182
0.189
0.197
0.204
0.211
0.218
0.225
0.233
0.240
0.247
70r
222
994
277
506
691
839
I
11
r59
208.446
397
227.735
234.291
240.910
247.593
254.339
261.147
0.9332
0.9512
0.ur
0.1 t5 055
0.1 1 8 690
0.r22 304
0.
0.
125 901
129 483
2r4.Br4
22r.243
0.9
1
49
.097
0.100
0.103
0
98.762
836
I
971
205.428
046
2I
072
2t8.779
225.488
232.230
059
0.056 014
0.057 941
0.059 846
0.061 731
0.063 600
0.065 455
0.067 298
2.095
239.012
245.837
252.707
259.624
266.590
273.605
r 99
0.035 646
0.7423 0.037 464
0.7639 0.039 214
0.7849 0.040 91i
0.8054 0.042 565
0.8253 0.044 184
0.8448 0.045 774
0.8638 0.047 340
0.8825 0.048 886
0.9008 0.050 415
0.9187 0.051 929
0.9364 0.053 430
0.7
207.580
214.745
0.038 673
278.720
285.946
0.039 764
221.854
228.931
235.997
243.066
250.146
257.247
264.37 4
27 r.531
0.7148
0.7373
0.7590
0.7799
0.8002
0.8 I 99
0.8392
0.8579
0.8763
0.8943
0.91l9
0.9292
0.022 830
0.024 068
0.025 247
0.026 380
0.027 477
0.028 545
0.029 5BB
0.030 612
0.031 619
0.032 612
0.033 592
0.034 563
r84.6r9
190.660
r96.762
202.927
209.160
215.463
221.83tt
228.277
234.789
|
24r.37
248.020
0.057 150
0.059 984
0.062 734
r
87.583
0.07B 200
239.97
|
673 246.723
127 253.530
0.085 566 260.391
0.080
0.9171
0.083
0.9352
0.6999
0.7230
10.656
0.7452
217.484
0.7667
224.315
0.787 5
23l.l6l
0.8077
0.8275
0.8467
0.8656
0.8840
0.036 285
0.9021
0.9 198
0.042 907
244.932
251.869
258.845
265.862
272.923
0.030 422
0.031 966
0.033 450
0.034 887
0.037 653
0.038 995
0.040 316
0.041 619
0.044
181
205.924
0.7016
0.019 744
0.7248
220.558
227.766
0.7 469
0.020 912
0.022 0 r 2
0.7682
0.7888
0.8088
0.8283
0.023
0.024
0.025
0.026
0.8472
0.026 937
0.8657
0.8838
0.027 851
0.028 751
0.90 r 6
0.029 639
0.9 189
0.030 515
234.94r
944 160
256.428
263.61 3
270.820
278.055
285.320
0.8853
0.9038
0.9220
16
i54
r
202.1
209.
216. 14
223.104
230.062
237
.027
244.009
251.016
258.053
265"124
272.231
0.7063
0.7291
0.751 I
0.7723
0.7929
0.8129
0.8324
0.8514
0.8700
0.8882
0.9061
0.90 MPa
2t3.290
242.t01
0.8665
0.60 MPa
203.814
238.031
0.6984
0.073 r 85
5 7.05
0.8987
2
0.8787
0.8980
0.9169
0.9354
0.07
0.065 418
0.068 049
0.070 635
.160
196.935
0.8591
194.034 0.7216
200.490 0.7 440
206.969 0.7658
213.480 0.7869
220.030 0.8075
226.627 0.8276
233.273 0.8473
253.936
260.770
247
0.7318
0.7543
0.7763
0.7977
0.8186
0.8390
0.30 MPa
0.80 MPa
0.70 MPa
0.026 761
0.028 100
0.029 387
0.030 632
0.031 843
0.033 027
0.034 189
0.035 332
0.036 458
0.037 572
0.7628 0. l 14 7 16
0.7849 0.119 866
0.8064 0.124 932
0.8275 0.129 930
0.8482 0.134 873
0.8684 0.139 768
0.8883 '0.144 625
0.9078 0.149 450
0.9269 0.154 247
0.9457 0.159 020
0.9642 0.163 774
0.50 MPa
0.40 MPa
0.045
0.047
0.050
0.052
0.054
0.740r
188.644 0.7139
r94.969 0.7366
201.322 0.7587
0.7801
207 .7 15
214.153 0.80 t 0
220.642 0.82 r4
227.r85 0.U4 r 3
233.785 0.8608
240.443 0.8800
327
238
134
kf/kg K
0.15 MPa
0.25 MPa
202.135
189.669
195.878
40.0
50.0
60.0
70.0
80.0
90,0
100.0
I 10.0
120.0
130.0
140.0
r 50.0
222.42r
228.815
235.285
241.829
248.446
044
0.096 418
0.092 550
20.0
30.0
40.0
50.0
60.0
70.0
80.0
90.0
100.0
r 10.0
120.0
130.0
2r6.t04
955
0.100 228
0.103 989
0.107 710
0.088 608
90.0
l 10.0
85.707
l9 I .628
r 97.628
203.707
209.866
r
0.7320 0.069 752
0.7543 0.073 024
0.7760 0.076 218
0.7972 0.079 350
0.8 r 78
0.082 43 I
0.8381 0.085 470
0.8578 0.088 474
0.8772 0.091 449
0.8962 0.094 398
0.0
10.0
100.0
179.861
647
0.20 MPa
20.0
30.0
40.0
50.0
60.0
70.0
80.0
hs
kJ/kg
a
m,r/kg
.C
062
072
051
005
204.t70
21,r.765
2r9.2r2
226.564
233.856
24r.r13
248.355
255.593
262.839
270.100
277.38r
284.687
,N
0.6982
0.7131
0.7358
0.7575
0.7
7
85
0.7987
0.8184
0.8376
0.8562
0.8745
0.8923
0.9098
"

15. Table A.3.2 (Continued)
Suoerheated Freon-12
'fernp
.C
u
h
5
u
m'/kg
kJ/kg
kJ/kg K
m'/kg
i62
10
225.3r9
0.018 366
0.019 410
0.020 397
0.021 341
0.022 251
0.023 133
210.
0.023 993
254.7
0.024 835
0.025 661
0.026 474
0.027 275
0.028 068
2 r 7.8
232.739
240.101
247.430
43
262,053
269.369
276.69s
284.047
29t.4lS
0.7021
0.7254
0.014 483
0.7 47 6
0.016 368
0.7689
0.7895
0.8094
0.8287
0.8475
0.8659
0.8839
0.9015
0.9187
0.0t7
0.015 463
221
0.018 032
0.018 812
0.019 567
0.020 301
0.021 018
0.02t 721
0.022 4r2
0.023 093
0.01
0.01
160.0
170.9
l80.0
I
I
208
984
0.012 698
0.013 366
0.014 000
216.650
225.r77
233.390
24r.397
0.6959
0.7204
0.7433
20.0
130.0
140.0
150.0
160.0
170.0
r80.0
190.0
200.0
2 r 0.0
220.0
230.0
l
206.661
214.805
222.687
230.398
237.995
245.518
252.993
260.44r
267.875
27 5.307
282.745
290.195
0.6812
0.7060
0.012 579
0.7293
0.013 448
0.7 514
0.014 247
0.7727
0.014 997
0.015 710
0.7931
0.8129
0.8320
0.8507
0.8689
0.8867
0.016
0.017
0.017
0.018
0.9041
0.019 535
393
053
695
321
0.018 934
0.7651
2r3.049
0.6794
222.).98
230.835
0.7057
0.7298
0.7524
255.228
263.094
0.8141
0.0r3 772
270.891
0.8332
0.010 035
0.010 615
0.01 1 159
0.011 676
0.012 172
239. I 55
0.008 704
0.009 406
0.015 195
0.015 765
0.016 320
0.7859
0.8059
0.8253
0.8440
0.8623
0.014 284
278.642
0.85 t 8
0.0r2
0.016 864
0.017 398
287.669
295.290
286.364
294.069
302.9r4
0.8698
0.8874
0.9046
0.013 I t6
0.013 570
0.017 923
0.8801 0.014 784
0.8975 0.0r5 272
0.9145 0.0r5 752
0.014 608
0.006 595
0.007 264
0.007 837
0.008 351
0.008 827
0.009 273
0.009 697
0.0i0
219.562
229.852
239.27 |
248.192
256.794
265. r 80
273.114
104
2B 1.540
0.010 497
289,589
297.583
305.540
313.472
0.010 879
0.01
0.01
l
r
250
614
0.003 736
0.004 325
0.004 781
0.005 172
0.005 522
0.005 845
0.006 147
0.006 434
0.006 708
0.006 972
0.007 228
0.007 477
224.863
238.443
249.703
259.904
269.492
278.684
287.602
296.326
304.906
313.380
321 .77
4
330.108
247.264
30r
.7
67
l/t<g x
40 MPa
21r.457
219.822
227.89r
235.766
243.5r2
25 1.170
258.77 0
266.334
273.877
281 .4
n
288.946
0.6876
0.7
r23
0.7355
0.7575
0.7785
0.7988
0.8183
0.8373
0.8558
0.8738
0.8914
2.00 MP:t
249.264
257.035
264.742
272.406
280.044
0.7739
0.7944
651
0.0r4 013
3.00 MPa
218.859
228.056
36.760
245.r54
253.34r
2
0.6909
0.7166
0.7 402
0.7
624
261.384
269.327
0.7835
0.8037
0.8232
0.8420
285.027
292.822
300.598
0.8781
277.20t
0.8603
0.8955
3.50 MPa
0.6823
0.7103 0.005 231
0.7352 0.005 886
0.7582 0.006 419
0.7798 0.006 887
0.8003 0.007 313
0.8200 0.007 709
0.8390 0.008 083
0.857 4
0.008 439
0.87 52
0.008 782
0.8926 0.009 114
0.9095 0.009 436
4.00 MPa
r
rn'r/kg
0.009 406
0.010 i87
0.010 884
0.011 526
0.012 126
0.012 697
0.013 244
2.50 MPa
90.0
100.0
1 r0.0
120.0
130.0
140.0
150.0
160.0
170.0
180.0
190.0
200.0
K
1.80 MPa
1.60 MPa
70.0
80.0
90.0
100.0
r 10.0
120.0
130.0
140.0
r 50.0
|/kg
i.r
kJ/kg
U
.t
kJ/kg
1.20 MPa
1.00 MPa
50.0
60.0
70.0
80.0
90.0
100.0
I 10.0
120.0
r 30.0
140.0
i50.0
1ii0.0
h
k
0.677 r
0.7i11
0.7386
0.7630
0.7854
0.8063
0.8262
0.8453
0.8636
0.8813
0.8985
0.9152
220.529
232.068
242.208
251.632
260.620
269.3
I
I
277.8r7
286.r71
294.422
302.597
310.718
0.6770
0.7075 0.001324
0.7336 0.004 959
0.7573 0.005 456
0.7793 0.005 884
0.8001 0.006 ?70
0.8200 0.006 626
0.8391 0.006 961
0.8575 0.007 279
0.8753 0.007 584
0.8927 0.007 878
222.t21
234.875
245.66t
255.524
264.846
273.817
282.545
291.100
299.528
3
07.
il64
0.6750
0.7078
0.7349
0.7591
0.7814
0.8023
0.8222
0.8413
0.8597
0.877 5

16. Table A.4
Thermodynamic Properties of Oxygen'
Table A.4.1
Saturated Oxygen
Enropy
k|/kg K
Enthalpy
kJ/kg
Speci{ic Volume
ms/kg
Press.
Sat.
Sat.
Sat.
Temp
MPa
Liquid
Evap,
Vapor
Liquid
Evap
K
P
a1
uts
us
hl
hts
0.00015
0.00073
0.00623
0.03006
0.09943
0.000 765
0.000 780
0.000 808
0.000 840
0.000 876
0.000 917
0.000 966
0.001 027
0.001 i 08
Sat.
Vapor
54.3507
60
70
80
90
100
110
120
130
140
150
154.57 6
0.25425
0.54339
I .0215
r.7478
2.7866
4.2190
5.0427
0.00
i
92.9658
92.9666
2r.3461
2r.3469
2.9085
2.9093
0.681 04
0.68I
0.226 49
0.227 36
0.095 562
0.046 821
0.025 363
0.014 596
0.008 569
0.004 660
0.002 293
230
0.001 480
0.002 293
0.094 645
0.045 855
0.024 336
0.013 488
0.007 339
0.003 180
0.000 000
88
-193.432
-
184.029
-167.372
-
150.646
133.758
r 1o.55 /
-98.829
-80.219
-60.093
-37.045
-7.038
32.257
h,,
Vapor
se
2.0938 4.4514
2.2585 3.9686
2.5r51 3.2936
2.7
382
2.7
7
79
2.9364 2.3663
3.ll6r 2.0222
3.2823 1.7 210
3.440t 1.4445
3.5948 1.1766
3.7567 0.8935
3.9498 0.5301
4.1977 0.0000
79.3r2
202.291 85.734
189.320 90.491
173.310 93.091
152.887 92.794
125.051 88.006
79.459 72.421
0.000
Evap.
.l.rs
J1
242.553 49.l2 I
238.265 54.236
230.527 63. I 55
222.289 7 r.643
2t3A70
Sat'
Sat.
Liquid
32.257
6.5452
6.227
5.5 l6 I
5.3027
5.1383
5.0033
4.8846
4.7714
4.6502
4.4799
4.1977
,'Adapted frorn L. A. Weber,rlc,zrnaL of Research oJ the National Bureau of Standard's,74Az 93 (1970).
Table A.4.2
Superheated Oxygen
Temp.
K
I
h
J
a
h
J
m'/kg
u
kJ/kg
kJ/kg K
m3/kg
kJ/kg
kJ/kg K
m'/kg
0.10 MPa
100
r25
150
r t5
200
225
250
275
300
0.253 503
0.320 717
0.386 914
0.452 645
0.518 127
0.583 465
0.648 7l I
0.713 895
0.779 036
88.828
r12.2r4
135.301
158.255
181.r45
204.007
226.869
249.769
272.720
0.20 MPa
5.4016
5.6107
5.7787
5.9202
6.0427
6.1502
6.2468
6.3369
6.4140
86.864
5.2083
l 10.988
5.424r
0.060 674
r92 016
134.440
0.225 276
0.258 282
0.291 140
0.323 906
0.356 610
0.389 271
157.609
180.638
5.5V+ I
5. t 5lo
0.075 039
0.088 842
0.
r25
I t5
200
225
250
275
300
0.027 869
0.035 976
0.043 341
0.050 394
0.057 282
0.064 068
0.070 790
200.280
223.795
247.185
0.077 467
270.516
99.653
r27.t12
r52.269
176.508
203.596
226.529
249.483
272.475
5.8609
5.9688
6.0657
6. l 560
6.2332
0.102 371
l5
746
0.129 025
0.1
0.142 242
0.155 415
2.00 MPa
I
07.093
116.476
145.
l
l2
171.150
196.052
220.348
244.309
268.076
5. 1650
131.788
155.643
5.4919
l 79. I
5.6 175
05
202.359
225.506
248.62t
27 r..740
5.3448
5.7268
5.8246
5.9 r 56
5.9932
4.00 MPa
4.9431
5.t433 0.016 270
5.2986 0.020 544
5.4283 0.024 395
5.540 r
0.02& 051
5.6394 0.031 597
5.7314 0.035 073
5.8098 0.038 502
kJ/kg K
0.50 MPa
0.123 394
0.158 268
1.00 MPa
150
hs
kJ/kg
4.9130
5.0899
0.005 526
81.48
0.009 029
128.61
5.2293
5.3464
0.01
l
376
5.449r
0.013 444
0.015 378
5.5433
5.6263
0.0
0.0
r
7 233
l9
039
r
8
159.715
187.333
213.37
4
238.560
263.234
4.5475
4.8414
5.0080
5.
|
5.8087
r380
5.2480
5.3469
5.4300

17. Table A.4.2 (Continued)
Superheated Oxygen
'fernp,
u
h
J
'(.)
h
J
rn3/kg
kJ/kg
kJ/ks K
m'/kB
kJ/kg
kJ/kg K
hs
kJ/ks
u
K
mir/kg
I t5
225
250
0.007 027
0.008 589
0.009 991
zl5
0.01
300
0.012 570
I
4,643r
107.496
147.232
0.005 051
200
178.304
4.8565
5.0029
206.340
5.1214
232.848
258.464
306
10.00 MPa
8.00 MPa
6.00 MPa
5.2253
5.3 I l6
0.003 002
0.004 864
0.006 l8l
0.007 316
0.008 360
0.009 351
r
kJikg K
79.5r3
33.760
169.069
199.317
227.2r9
253.797
5.0251
0.002 020
0.003 603
0.004 757
0.005 730
5.1344
5.2240
0.006 606
0.007 432
4.4384
4.7308
4.8973
r
67
52.66
119 .7
159.686
192.401
221.685
249.262
4.2573
4.6 189
4.8072
4.9455
5.0572
5. I 533
20.00 MPa
24.551
75.318
122.595
163.109
198.021
229.655
r 343
r75
0.00
200
225
0.00r 727
250
z/5
300
0.002 236
0.002 755
0.003 241
0.003 700
4.0086
4.2798
4.5024
4.6739
4.8069
4.917 4
Table A.5
Thermodynamic Properties of
Table A.5.1
Saturated Nitrogen
N
itrogen.
Specific Volume
Enthalpy
kJ/kg
m'/kg
'femp
Press.
Sat.
Sat.
MPa
Liquid
Sat.
Evap.
Vapor
Liquid
Evap.
U1
Ufu
us
hr
hto
0.001 152
0.001 162
r.480 060
1.093 r 73
0.525 785
r.481 212
Entropy
kJ/kg K
K
D
r43 0.01253
65 0.01742
70 0.03858
5 0.0761 2
77 .347 0. 101325
B0 0.1 370
85 0.2291
90 0.3608
95 0.541 l
100 0.7 790
r 05
1.0843
l l0
1.4673
I 15
1.9395
120 2.5135
r 25
3.2079
I 26. 1
3.4000
63.
7
0.001 l 89
0.00
r ?21
0.001 237
0.001 256
0.00
0.00
i 296
i 340
0.001 392
0.001 452
0.001 524
0.001 613
0.001 797
0.001 904
0.002 323
0.003 184
0.280 970
0.215 504
0.162 794
0.100 434
0.064 950
0.043 504
0.029 861
0.020 745
0.014 402
0.009 696
0.006 130
0.002 568
0.000 000
1.094 335
0.526 974
0.282 l9l
0.216 74r
0.r64 050
0.10r 730
0.066 290
0.044 896
0.031 313
0.022 269
0.0
r
6 015
0.011 493
0.008 034
0.004 891
0.003 I 84
-
150.348
r 46.691
136.569
-126.287
- t21.433
- r 15.926
- r05.461
-94.817
-83.895
-7 2.571
-60.691
*48.027
-34.t57
-
18.017
+6.202
+30.791
215.188
2t3.29t
207 .727
20 l .662
Sat.
Sat.
Vapor Liquid
ho
64.840
66.600
7l . l58
7
5.37 5
ii
2.4310
2.4845
2.6345
2.7755
2.8390
2.9083
3.0339
Sat.
Evap.
Vapor
.16
3.4076
3.2849
2.9703
5.8386
2.69
5.4670
t5
5.7694
5.6048
r98.645 77.2r2
2.5706 5.4096
195.089 79. t63
2.4409 5.3492
r 87.892 82.43 r
2.2122 5.246r
r79.894 85.077 3. r535 2.0001 5.1536
r70.877 86.982 3.2688 1.7995 5.0683
160.562 87.991 3.38 l6 I .6060 4.9876
r48.573 87.882 3.4930 I .4150 4.9080
134.319 86.292 3.6054 r.2209 4.8263
l16.701 82.544 3.7214 l.0145 4.7359
93.092 75.075 3.8450 0.7803 4.6253
50. r 14 56.3 t 6
4.0356 0.3989 4.4345
0.000 30.791 4.2269 0.0000 4.2269
"Adapted from "Thermodynamic Properties of Nitrogen Including Liquid and Vapor Phases liom 63 l( to 2000 I( with pressures to
'f.
Jacobsen and R. R. Stewart, Jour. oJ Phys. and Chem. Ref. Data,21 757-922 (1973).
10,000 Bar'," R.

18. Table A.5.2
Superheated Nitrogen
7)
I-ernp
h
.t
u
h
.t
u
rn3/kg
kJ/kg
kJ/ks K
m3/kg
kJ/kg
kJ/kg K
mt'/kg
K
100
i25
i50
0.290 978
0.367 217
r 01 .965
128.505
0.442 6 l9
ts4.7 7I
180.935
207.029
233.085
259.122
285.144
311.158
| /5
0.5 r 7 576
200
0.592 288
0.666 552
225
250
275
300
0.2 MPa
0. 1 MPa
0.741375
0.815 563
0.890 205
5.6944 0.142 475
5.93 13 0.181 71
6.1228 0.220 014
6.2841 0.257 890
6.4234 0.295 531
6.5460 0.332 841
6.6561 0.370 418
6.7550 , 0.407 619 )
6.8457 0.445 047
1
r25
225
0.033
0.041
0.050
0.058
0.065
250
0.073 634
275
0.08I
150
ll3
200
300
065
117.422
884
141
i 25
096
875
I I 5.155
260
0.088 899
256.220
282.720
5.1872
5.4042
5.5779
5.1237
5.8502
5.9632
6.0639
309. i 73
6. I 563
.176
202.596
229.526
0.014 02r
0.019 546
0.024 155
0.028 436
0.035 697
0.036 557
0.040 485
0.044 398
rt5
200
225
250
275
300
0.004
0.006
0.008
0.010
413
913
772
396
0.01 1 934
0.013 383
0.014 800
87.090
140.183
4.5667
4.8966
177
5.0961
.447
139
210.
240.806
270.222
298.907
5.2410
5.3796
5.4917
5.5916
0.002
0.004
0.006
0.007
0.008
0.010
0.0r I
9r7
863
390
200
225
250
275
300
0.001 956
0.002 603
0.003 369
0.004 106
0.004 808
0.005 461
0.006 091
36.922
92.284
140.886
182.034
218.710
252.465
284.523
206.537
232.690
6.2160
6.3388
258.796
6.449r
-)
.284.876
310.937
6.5485
6.6393
137.9
l6
168.709
197.609
0.055 520
0.073 422
0.090 150
0.106 394
0.122 394
0.138 173
0.154 006
0.169 642
0.185 346
4.8878
5.1547
5.3449
0.008 234
5.4992
0.013 648
5.6309
0.0 r 5 894
0.018 060
0.020 133
0.022 r 78
225.578
253.032
5.7469
280. r 32
5.850 r
307.014
5.9436
6 r.903
r25.536
4.35 r 8
4.7470
4.9726
5. I 384
034
133
295.2r9
5.4942
5.2750
5.3910
20.0 MPa
4.0798
4.4213
4.6813
4.8752
5.0303
5.1845
5.2707
0.001
0.002
0.002
0.003
0.003
0.004
0.004
781
r 86
685
208
728
223
704
94.345
I23.824
151 .470
t78.434
205.063
23r.459
257 .828
284.076
3 r 0.273
5. 1706
5.4343
5.6361
5.8025
5.9447
6.0690
6. I
B0l
6.2800
6.37 15
0.01
l
186
l t 5.7 l6
4.8384
154.85
5.0804
5.2553
5.3976
r
187.52t
2r7.757
246.793
275.056
302.848
5.5202
5.6277
5.7248
10.0 MPa
167.680
903
K
4.0 MPa
202.867
235.141
265.676
69 r
15.0 MPa
150
ttD
5.47 67
| 5.7 194
153.962 5.9 r 32
r80.314 6.0760
t27 .37
8,0 MPA
6.0 MPa
150
100.209
101.489
kf/kg
0.5 MPa
2.0 MPa
1.0 MPa
hs
kf/ks
33.637
3.9956
83.453
4.3029
130.291
172.307
2 10.456
+.55.1C
245.640
278.942
b.0467
+-/5lL
4.9r27
5. l 629
0.002
0.003
0.005
0.006
0.007
0.008
0.008
388
750
016
r04
r 12
046
950
48.687
112.489
158.578
196.079
229.861
4.2287
4.6239
4.8709
5.0474
5.1900
26 I
5.3 103
.450
291.800
5.4163

19. F
;
G'
g
Table A.6
;
:l
i
Thermodynamic Properties of Saturated Mercurv"
Enthalpy, kJ/kg
Press., Temp.,
Sat.
oC Liquid
MPa
0.000 06
0.000 07
0.000 08
0.000 09
0.000 l0
109.2
0.0002
0.0004
0.0006
0.0008
0.0010
0.002
0.004
0.006
0.008
0.010
0.02
0.04
0.06
0.08
t34.9
329.0
343.9
0.1
J5r).
0.2
0.3
423.8
15.13
r2.3 15.55
15.0 15.93
r I .3 16.27
19.7
151.5
161.8
169.4
rI
t.5
195.6
2r7.7
23r.6
242.0
250.3
278.1
309.1
I
397.r
i6.58
t8.67
Evap.
3r2.33
297.r4
312.69
313.02
257.09
297.04
297.00
296.71
20.93 296.40
22.33 296.2r
23.37 296.06
24.21 295.95
26.94 295.5?
29.92 295.r5
31.81 294.89
33.21 294.70
34.33 294.54
38.05 294.02
42.21 293.43
44.85 293.06
46.84 292.78
48.45 292.55
53.87 29r.77
57.38 291.27
60.03 290.89
62.20 290.58
64.06 290.3r
65.66 290.08
0.4
444.1
460.7
474.9
0.8
67.rr
289.87
0.9
498.4
508.5
1.0
Jr /.d
69.6r
289.50
t.2
534.4
1.4
1.6
1.8
549.0
562.0
574.0
584.9
2.0
2.2
2.4
2.6
2.8
3.0
595.1
J.5
604.6
613.5
622.0
630.0
648.5
4.0
665.
r
68.42 289.68
71.7 5 289. l9
73.63 288.92
75.37 288.67
76.83 288.45
78.23 288.24
79.54 288.05
80.7
5
8r.89
82.96
83.97
86.33
88.43
Sat. Sat.
Vapor Liquid Evap.
297.20
0.5
0.6
0.7
487.3
Entropy, kJ/kg K
313.31
313.58
315.38
317.33
318.54
3r9.43
320.
l6
322.5r
325.07
326.70
327.9r
328.87
332.07
JJ3.04
337.9r
339.62
341.00
345.64
348.65
350.92
352.78
354.37
355.74
356.98
358. I 0
359. I I
Specific
Table A.6 (Continued)
Thermodynamic Properties of Saturated Mercurv"
Volume
Sat.
Vapor
m3/kg
Enthalpy, kJikg
Sat. Vapor,
0.0466 0.7774 0.8240 259.6
p.0477 0.7709 0.8186 994 c,
0.0487 0.7654 0.814t r97.7
0.0496 0.7604 0.8r00 176.8
0.0503 0.7560 0.8063 160. l
0.0556 0.727r 0.7827 83.18
0.06r0 0.6981 0.7591 43.29
0.0643 0.681 I 0.7454 29.57
0.0666 0.6690 0.7356 22.57
0.0685 0.6596 0.7281
18.31
0.0744 0.6305 0.7049
9.57 0
0.0806 0.6013 0.6819
5.013
0.0843 0.5842 0.6685
3.438
0.0870 0.5721 0.6591
2.632
0.0892 0.5627 0.6519
2.r40
0.0961 0.5334 0.6295
l. 128
0.1034 0.5039 0.6073
0.5942
0.1078 0.4869 0.5947
0.41 13
0.1I l0 0.4745 0.5855
0.3163
0. l l 36 0.4649 0.5 785
0.258I
0.i2t8 0.4353 0.5571 0.r377
0.1?68 0.4t79 0.5447
0.095 5 t
0.1305 0.4056 0.5361
0.073 78
0.1334 0.3960 0.5294
0.060 ,14
0.1359 0.3881 0.5240
0.051 37
0.1380 0.3815 0.5195
0.044 79
0. t398 o.3757 0.5155
0.039 78
0.1415 0.3706 0.512t
0.035 84
0.1429 0.3660 0.5089
0.032 66
0.1455 0.3581 0.5036
0.027 B I
0.r478 0.3514 0.4992
0.024 29
0.1498 0.3456 0.4954
0.021 6 r
0.1515 0.3405 0.4920
0.019 49
0. r 53 l 0.3359 0.4890
0.0r7 78
0. r 546 0.331B 0.4864
0.016 37
0. r 559 0.3280 0.4839
0.015 l8
0.t571 0.3245 0.4816
0.0r4 l6
0. r 583 0.32 t2 0.4795
0.0i3 29
0. t594 0.3182 0.4776
0.012 52
360.94
362.55
364.04
365.28
366.47
367.59
287 .87 368.62
287.70 369.59
287.54 370.50
287.39 37 r.36
287.04 J l a..t / 0.I6 t9 0.:J 1 i5 0.4734
286.73 J/5.tt) 0.1641 0.3056 0.1657
0.010 96
0.009 78
Press.,
MPa
4.5
5.0
5.5
6.0
o.5
7.0
t.3
Temp.,
Sat.
"C Liquid
680.3
694.4
707.4
719.7
Evap.
Entropy, kJikg K
Sat.
Sat.
Vapor Liquid Evap
90.35
286.44
92.r
286.18 378.29 0.1678
285.93 379.69 0.1694
285.70 38r.00 0.1709
285.48 382.23 0.1723
285.28 383.40 0.I736
285.08 384.50 0.1748
I
93.76
95.30
73r.3 96.75
742.3 98.12
752.7 99.42
Specific
Sat.
Volume
Sat. Vapor,
Vapor
m3/kg
376.79 0.1660 0.3004 0.4664
0.2958 0.4636
0.29r6
0.4610
0.2878
0.2842
0.2809
0.2779
0.4587
0.4565
0.4545
0.4527
0.008 85
0.008 09
0.007 46
0.006 93
0.006 48
0.006 09
0.005 75
fromThermodlmttnric properties of Mercury Vapor,by
Lucian A. Sheldon. ASME,
.^'.O1ip::9
49A,30 (l949).

20. Table A.8
Table A.7
Critical Constantsu
Properties of Various ldeal Gasesu
Molecular Temp
Substance
F-ormula Weight
Ammonia
Argon
NH,
Ar
Br,
co,
co
cl,
D2
He
He
H2
Kr
Ne
N2
NrO
02
so,.
HrO
Xe
cuHu
crHro
ccl4
cHCl3
CC|1F2 J
cHCtrF
crHu
crH5oH
crHn
cuH,n
cHn
cH3oH
cHscl
crH,
c.Hu
c.H,
cclsF
Bromine
Carbon Dioxide
Carbon Monoxide
Chlorine
Deuterium (Normal)
Helium
Helium3
Hydrogen (Normal)
Krypton
Neon
Nitrogen
Nitrous Oxide
Oxygen
Sulfur Dioxide
Water
Xenon
Benzene
n-Butane
Carbon Tetrachloride
Chloroform
,/ Dichlorodifl uoromethane
D ich lo
rofl
uo
ro metha ne
Ethane
Ethyl Alcohol
Ethylene
n-Hexane
Methane
Methyl Alcohol
Methyl Chloride
Propane
Propene
Propyne
Trichlorofl uoromethane
"K. A. Kobe and R. E. Lynn,Jr.,
Chem.
t7.03
39.948
159.808
44.01
K
405.5
i5l
584
304.2
28.01l
IJJ
70.906
4.00
4r7
38.4
4..003
3.00
2.016
83.80
20.183
28.013
5.J
J..l
J J..f
209.4
44.5
126.2
44.013
309.7
31.999
64.063
43Q.7
18.015
131.30
79. I t5
59.124
r54.8
647.3
289.8
562
425.2
153.82
556.4
I19.38
536.6
384.7
120.91
102.92
45t.7
30.070
305.5
46.07
5r6
28.054
282,4
g6.l7g
507.9
191.1
32.042
50.488
44.097
513.2
416.3
370
365
40.065
401
137.37
/nt
MPa
m3/kmol
1.28 .0724
4.86 .a749
10.34 .1355
7.39 .0943
3.50 .0930
7 .7 |
.t242
1.66
0.23 .0578
0. l2
1.30 -0649
5.50 .0924
2.73 .0417
3.39 .0899
7.27 .0961
5.08 .0780
7.88 .1217
22.09 .0568
5.88 .1 186
4.92 .2603
3.80 .2547
4.56 .2759
5.47 .2403
4.01 .2179
5.r7 .r97 3
4.88 .1480
6.38 1673
5.r2 .1242
3.03 .3677
4.64 .0993
7 .95
.1 180
6.68 .1430
4.26 .1998
4.62 .1810
5.J5
4.38 .2478
r
Molecular
Formula Weight
Gas
Air
q
Rex.,52: il7-236 (t953)
R
kl
a
Ar
28.97
39.948
Butane
Carbon
Dioxide
Carbon
Monoxide
Ethane
Ethylene
CrHro
58.r24
44.01
0.188 92
CO
28.01
CrHo
30.07
CrH.
28.054
165 I .400
0.3122 1.667
r.7164
1.5734 1.091
0.8418
0.6529 r.289
1.0413 0.7445 1.400
r.7662 1.4897 1.186
r.5482 r.2518 1.237
r .667
5.1 926
3. r r 56
14.2091 10.0849 1.409
2.2537 r.7354 r.299
1.0299 0.6 r79 l.667
1.0416 0.7448 1.400
1.7113 1.6385 1.044
0.92r6 0.6618 1.393
1.6794 1.4909 1.126
1.8723 1.4108 1.327
0.287 00
0.208 13
0.143 04
CO,
0.296 83
0.276 50
0.296 37
Helium
He
Hydrogen
Methane
H2
4.003
2.016
1.0035
2.077 03
CHn
16.04
Ne
20.1 83
0.41
N2
28.013
31.999
44.097
0.296
0.072
0.259
0.188
l5
0.46
Octane
CrHrt
Oxygen
o2
Propane
CrHt
HrO
Steam
r14.27
1
8.0
I
0.7
0.5203
4.124 t8
0.518 35
Neon.
Nitrogen
KI
('-uo kg K
KT
"oo kg K
kg K
Argon
95
80
79
83
55
52
^(Cro, C,o, and A are at 300 K).
Table A.9
Constant-Pressure Soecific Heats of Various ldeal Gases'
.
16.043
42.091
Chemical
Pressure Volume
Co,: kJ/kmol
0:
K
T(Kelvin)/100
Range Max.
K
Error
Gas
Vo
N2
02
H2
co
oH
NO
HrO
CO,
2,,
e
:
- bt2.7g0-1s + 1e72.7 0*2 - 820.400-3
+0.02010201'5 - 178.570-1 5 +236.88d-2
o":37.432
39.060
o":56.505 -702.740-o?5 + 1165.00-r 560.70d-''5
-oo:69. t45 -0.7046300'75 -200.77 0-o 5 + 176.760-0 75
e
e,": 143.05 -
e o":81.546
e o.:59.283
59.350f
2s
1.7096fl's
+
-
17
.32900
75
-
4.2660e
70.613 0-0 s + 74.8890-'
l8g.54f'2s +82.751005 -3.69899
eo":-3.7357 +30.529f's - 4.10340+0.024198P
5
300-3500
300-3500
300-3500
300-3500
300-3500
300-3500
300-3500
300-3500
0.43
0.30
0.60
0.42
0.43
0.34
0.43
0.19