Document 4JMo99ErZ0zv1RMBBRKm7nrga

Table 3. Thermodynamic Properties of Water at Saturation (Continued) Fahr. Temp. tm Absolute Pressure P* Lb/Sq In. In. Hg Specific Volume, cu ft per lb Enthalpy. Btu per lb Entropy. Btu per (Lb) (F) Sat. Solid H Evap. Sat. Vapor Sat. Solid tig x 10-* t8 x 10- hi Evap. hi8 Sat. Vapor Sat. Solid hg si Evap. rig Sat. Vapor s* 0 1 2. 3 4 5 6 7 8 0 10 11 . 12 13 14 15 16 17 18 19 20 21 . 22 23 24 25 26 27 28 . 29 30 31 32 0.01849 0.01948 0.02052 0.02161 0.Q2276 0.02396 0.02521 0.02653 6.02791 0.02936 0.03087 0.03246 0 03412 0.03585 0.03767 0.03957 0.04156 0.043630 04581 0.04808 0:05045 0.05293 0.05552 0 05823 0.06105 0.06400 0.00708 0.07030 0.07365 0.07715 0.08080 0.08461 0.08858 0.03764 0.03966 0.04178 ' 0.04400 0.04633 0.04878 0.05134 0.05402 0.05683 0.05977 0.06286 0.06608 0.06946 0.07300 0.07669 0.08056 0.08461 0.08884 0.09326 0.09789 0.1027 0.1078 0.1130 0.1186 0.1243 0.1303 0.1366 0.1431 - 0.1500 0.1671 0.1645 0.1723 0.1803 0.01742 0.01742 0.01742 0.01743 0.01743 0 01743 0.01743 0.01743 0.01743 0.01744 0.01744 0.01744 0.01744' 0.01744 0.01744 0.01744 0.01745 0.01745 0.01745 0.01745 0.01745 0.01745 0.01746 0.01746 0.01748 0.01746 0.01748 0.01748 0.01746 0.01747 0.01747 0 01747 0,01747 14.81 14.08 1340 12.75 12.14 11.55 11.00 10.48 9.979 9.507 9.060 8 636 8.234 7.851 7.489 7.144 6.817 6.505 6.210 5.929 5.662 6.408 5.166 4.936 4.717 4.509 4.311 4.122 3.943 3.771 3.608 3.453 3.305 . 14.81 14.08 13 40 12.75 12.14 11.55 11.00 10.48 9.979 9.507 9 060 8.636 8.234 7.851 7.489 7.144 6.817 6.505 6.210 5.929 5.662 5.408 5.166 4.936 4.717 4.509 4.311 4.122 3.943 3.771 3.608 3.453 3.305 -168.98 - 158.51 -158.04 -157.50 -157.09 -156.61 -156.14 -155.66 -155.18 -154.70 -154.22 -153.74 -153.26 -152.77 -152.29 -151.80 -151.32 -150.83 -150.34 -149.85 -149.36 -148.87 -148.38 -147.88 -147.39 -146.89 -146.40 -145.90 -145.40 -14490 -144.40 -143.90 -143.40 1220.07 1220.04 1220.01 1219.97 1219.94 1219.90 1219.88 1219.84 1219.80 1219.76 1219.72 1219.68 1219.64 1219.59 1219.55 1219.50 1219.46 1219.41 1219.36 1219.31 1219.26 1219.21 1219.16 1219.10 1219,05 1218.98 1218.93 1218.87 1218.81 1218.75 ' 1218.69 1218.63 1218.56 1061.09 10G1.53 1061.97 1062.41 1062.85 1063.29 1003.74 1064.18 1064.62 1005 06 1005.50 1005.94 1060.38 1066.82 1067.26 1067.70 , 1068.14 1068.58 1009.02 1069.46 1009.90 1070.34 1070.78 1071.22 1071.66 1072.09 1072.53 1072.97 1073.41 1073.85 1074.29 1074.73 1075.16 -0.3244 -0.3234 -0.3224 -0.3213 -0.3203 -0.3193 -0.3182 -0.3172 -0.3162 -0.3152 -0.3142 -0.3131 -0.3121 -0.3111 -0.3101 -0.3090 -0.3080 -0.3070 -0.3060 -0.3049 -0.3039 -0.3029 -0.3019 -0.3008 -0.2998 -0.2988 -0.2078 -0.2068 -0.2957 -0.2947 -0.2937 -0.2927 -0.2916 2.6541 2.6483 2.0425 2.6367 2.6309 2.6252 2.6194 2.6138 2.6081 2.6026. 2.5969 2.5912 2.5857 2:5801 2.5746 2.5690 2.5635 2.5581 2.5526 2.5471 2:5417 2.6364 2.5310 2.5256 2.5203 2.5150 2.5097 2.5045 2.4991 2.4939 2.4887 2.4835 2.4783 2.3297 2.3249 2.3201 2.3154 2.3106 2.3059 2.3012 2.2966 2.2919 2.2873 2.2827 2.2781 2.2736 2.2690 2.2646 2.2600 2.2555 2.2511 2.2466 2.2422 2.2378 2.2335 2.2291 2.2248 2.2205 2.2162 2.2119 2.2077 2.2034 2.1992 2.1950 2.1008 2.1867 Compiled by John A. Goff and S. Gmtch. Fahr. Temp. 1(F) 0 1 2 3 4 5 6 7 8 9 10 11 12 13 . 14 15 16 17 18 19 20 21 22 23 24 26 26 27 28 29 30 31 32 00 Table 3. Thermodynamic Properties of Water at Saturation (Continued) Fahr. Temp. F) Absolute Pressure P% Lb/Sq In. In. Hg Specific Volume, cu ft per lb Sat. Liquid *f Evap. vtg Sat. Vapor H Enthalpy, Btu per lb Sat. Liquid ht Evap. ht* Sat. Vapor h* Entropy, Btu per (lb) (F) Sat. Liquid st Evap. sf* | 1 Sat, Vapor s* Fahr. Temp. 1(F) *32 0.088580 33 0.092227 34 0.095999 35 0.099908 36 0.10396 .37 0.10815 38 0.11249 39 0.11699 40 0.12164 41 0.12640 42 0.13145 43 0.13660 44 0.14194 45 0.14746 46 0.15317 47 48 49 . 60 51 0.15907 0.16517 0.17148 0.17799' 0.18473 52 . 0.16169 63 0.19888 54 0.20630 55 0.21397 56 0.22188 57 0.23006 58 0.23849 69 0.24720 60 0.25618 61 0.26545 0.18036 0.18778 0.19546 0.20342 0.21166 0.22020 0.22904 0.23819 0.24767 0.25748 0.26763 0.27813 0.28899 0.30023 0.31185 0.32387 0.33629 0.34913 0.36240 0.37611 0.30028 0.40402 0.42003 0.43564 0.45176 0.46840 0.48558 0.50330 0.62160 0.54047 0.01602 0.01602 0.01602 0.01602 0.01602 0.01602 0.01602 0.01602 0.01602 0.01602 0.01602 0.01602 0.01602 0.01602 0.01602 0.01602 0.01602 0.01602 0.01602 0.01602 0.01602 0.01603 0.01603 0.01603 0.01603 0.01603 0.01603 0.01603 0.01603 0.01604 3304.6 3180.5 3061.7 2947.8 2838.7 2734.1 2633.8 2537.6 2445.4 2356.9 2272.0 2190.5 2112.3 . 2037.3 1965.2 1896.0 1829.5. 1765.7 1704.3 1645.4 1588.7 1534.3 1481.9 1431.5 1383.1 1336.5 1291.7 1248.6 1207.1 1167.2 3304.6 3180.5. 3061.7 2947.8 2838.7 2734.1 2633.8 2537.6 2445.4 2356.9 2272.0 2190.5 2112.3 2037.3 1965.2 .1896.0 1829.5 1765.7 1704.3 1645.4 1588.7 .1534.3 1481.9 1431.5 1383.1 1336.5 1291.7 1248.6 1207.1 1167.2 Compiled by John A. Goff and S. Gratch. Extrapolated to represent metastable equilibrium with undercooled liquid. 0.00 1.01 2.01 3.02 4.02 5.03 6.03 7.04 8.04 9.05 10.05 11.05 12.06 13.06 14.06 15.06 16.07. 17.07' 18.67 19.07 20.07 21.07 22.08 23.08 24.08 25.08 26.08 27.08 28.08 29.08 1075.16 1074:59 1074.03 1073.46 1072.90 1072.33 1071.77 1071.20 1070.64 1070.06 1069.50 1068.94 1068.37 1067.81 1067.24 1066.68 1066. U 1065.55 1064.99 1064.42 1063.86 1063.30 1062.72 1062.16 .1061.60 1061.04 1060.47 1059.91 1059.34 1058.78 1075.16 1075.60 1076.04 1076.48 1076.92 1077.36 1077.80 1078.24 1078.68 1079.11 1079.55 1079.99 1080.43 1080.87 1081.30 1081.74 1082.18 1082.62 1083.06 1083.49 1083.93 1084.37 1084.80 1085.24 1085.68 1086.12 1086.55 1086.99 1087.42 1087.86 0.00000 0.00205 0.00409 0.00612 0:00815 0.01018 0.01220 0.01422 0.01623 0.01824 0.02024 0.02224 0.02423 0.02622 0.02820 0.03018 0.03216 0.03413 0.03610 0.03806 0.04002 0.04197 0.04392 0.04587 0.04781 0.04975 . 0.05168 0.05361 0.05553 0.05746 2.1867 2.1811 2.1755 2.1700 2.1644 2.1589 2.1535 2.1480 2.1426 2.1372 2.1318 2.1265 2.1211 2.1158 .2.1105 2.1052 2.0999 2.0947 2.0895 2.0842 2.0791 2.0739 2.0688 2.0637 2.0586 2.0535 2.0485 2.0434 2.0385 2.0334 2.1867 2.1831 2.1796 2.1761 2.1726 2.1691 2.1657 2.1622 2.1588 2.1554 2.1520 2.1487 2.1453 2.1420 2.1387 2.1354 2.1321 2.1288 2.1256 2.1223 2.1191 2.1159 2.1127 2.1096 2.1064 2.1033 2.1002 2.0970 2.0940 2.0909 32* 33 34 35 36 37 38 39 40 41* 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 \ CO 1