Page 265 - Standard Handbook Of Petroleum & Natural Gas Engineering

236 General Engineering and Science

Table 2-22
Steam Table for Use in Condenser Calculations
Specific
Abs pressure "OllUlle Entl V
Psi In. Hg Sat Sat sat
vapor, liquid, liquid,
P vg f?? !f
50 0. I781 1 0.3626 1703.2 18.07 1065.6 1083.7 0.0361 2.1264
52 0.19182 0.3906 1587.6 20.07 1064.4 1084.5 0.0400 2.1199
54 0.20642 0.1203 1481.0 22.07 1063.3 1085.4 0.0439 2.1136
56 0.2220 0.4520 13132.4 24.06 1062.2 1086.3 0.0478 2.1072
58 0.2386 0.4858 1291.1 26.06 1061.0 1087.1 0.0517 2.1010
60 0.2563 0.5218 1206.7 28.06 10.59.9 1088.0 0.0555 2.0948
62 0.2751 0.5601 1128.4 30.05 1058.8 1088.9 0.0993 2.0886
64 0.2951 0.6009 1055.7 3'2.05 1057.6 I 089. 7 0.0632 2.0826
66 0.3164 0.6442 988.4 34.05 1056.5 1090.6 0.0670 2.0766
68 0.3390 0.6903 925.9 36.04 1055.5 1091.5 0.0708 2.0706
70 0.3631 0.7992 867.9 38.04 1054.3 1092.5 0.0748 9.0647
72 0.3886 0.7912 813.9 40.04 1053.2 1093.2 0.0783 2.0588
74 0.4156 0.8462 763.8 42.03 1058.1 1094.1 0.0820 2.0530
76 0.4443 0.9046 717.1 44.03 1050.9 1094.9 0.0858 9.0473
78 0 4747 0.9666 673.1; 46.02 1049.8 1095.8 0.0895 2.0416
80 0.5069 1.0321 633.1 48.02 1048.6 1096.6 0.0932 2.0360
82 0.5410 1.1016 595.3 50.01 1047.5 1097.5 0.0969 2.0304
84 0.5771 I 1750 560.2 52.01 1046.4 1098.4 0.1005 2.0249
86 0.6154 1.2.527 527.3 .54.00 1045.2 1099.2 0.1042 2.0195
88 0.65.56 1.3547 496.7 .m.on 1044.1 1100.1 0.1079 2.0141
90 0.6982 14215 468.0 57.99 1042.9 1100.9 0.1115 2.0087
92 0.7432 15131 441.3 59.99 104i.x 1101.8 O.ll.51 2.0034
94 0.7906 1.6097 416.2 61.98 1040.7 1102.6 0.1187 I 9981
96 0.8407 1.7117 392.8 63 98 1039.5 110s.i 0.1223 1.9929
98 0.8935 1.819'2 370.9 65.97 1038.4 1104.4 0.1259 1.9877
100 0.9492 1.9325 350 4 67 97 1037.2 1105.2 0.1295 1.9826
102 1.0078 2.0519 331.1 69.96 1036.1 1106.1 0.1330 1.9775
104 1.0695 2. I775 313.1 71.96 1034.9 1106.9 0.1366 1.9725
106 1.1345 2.3099 296.2 73.95 1033.8 I 107.8 0.1401 1.9675
108 1.2029 2.4491 280.3 75.95 1032.7 1108.6 0.1436 1.9626
110 1.2748 2.5955 265.4 77.94 1031.6 llO9.5 0.1471 1.9577
112 1.3504 2.7494 251.4 79.94 1030.4 I1 10.3 0.1506 1.9529
114 1.4298 2.91 11 238.2 81.93 1OpY.2 1111.1 0.1541 1.9481
1 I6 1.5130 3.0806 225.8 83.93 1028.1 11 12.0 0.1576 1.9433
I18 1.6006 9.2589 214.2 85.92 1026.9 1112.8 n.1610 1.9386
120 1.6924 9.4458 203.27 87.92 1025.8 1113.7 0.1645 1.9339
122 1.7888 3.64'20 192.95 89.92 1024.6 1114.5 0.1679 1.9293
124 1.8897 3.8475 183.25 91.91 1023.4 1115.3 0.1714 1.9247
126 1.9955 4.0629 174.10 93.91 1022.5 11 16.2 0.174R 1.9202
128 2.1064 4.2887 165.47 95.91 1021.1 1117.0 0. I782 1.9156
130 2.2225 4.5251 157 14 97 YO 1020.0 1117.9 0.1816 1.9112
132 2.3440 4.7725 149.66 99.90 1018 8 1 118.7 0.1S49 1.9067
134 2.4712 5.0314 14'2.42 101.90 1017.6 11 19.5 0.1883 1.9023
136 2.6042 5.3022 135.58 103.90 1016.4 1120.3 0.1917 1.8980
I38 2.7432 5.5852 129.12 105.89 1015.3 1121.2 0. I950 1 ,8937
I40 2.8886 5.8812 123.01 107.89 1014.1 1122.0 0.1984 1.8894
142 3.0440 6.1903 11 7.23 109.89 1012.9 1122.8 0.2016 1.8851
144 3.1990 6.5132 111.77 I I I .n9 1011.7 1123.6 0.2049 1.8809
146 3.365 6.850 106.60 113.89 10106 1 124.5 0.2083 1.8768
148 3.537 7.202 101.71 115.89 1009.4 1125.3 0.2116 1.8726
-
1008.2
11 7.89
150 3.718 7.569 97.07 - 1126.1 0.2149 1.8685
SOURCE: Baurneister T., and Marks, L. S., e&.. Standard HmdDookJor M~rhanml EngiiiePrs, Seventh edition, MrGldw-
Hill Book Co., New York, 1967.