waste1

G.E. TABLE 3A 9C PARKER BOILER CO. TABLE 3A THERMODYNAMIC PROPERTIES OF SATURATED STEAM BASED ON TEMPERATURES ABSOLUTE PRESSURE SPECIFIC VOLUME CU FT/LB ENTHALPY BTU/LB TEMP. ºF + PSI IN HG SAT. LIQUID v f SAT. VAPOR v g SAT. LIQUID h f EVAP. h fg SAT. VAPOR h g 32.0 .08854 .1803 .01602 3306.0 0.00 1075.8 1075.8 35.0 .09995 .2035 .01602 2947.0 3.02 1074.1 1077.1 40.0 .12170 .2478 .01602 2444.0 8.05 1071.3 1079.3 45.0 .14752 .3004 .01602 2036.4 13.06 10 68.4 1081.5 50.0 .17811 .3626 .01603 1703.2 18.07 10 65.6 1083.7 55.0 .2141 .4359 .01603 1430.7 23.07 1062.7 1085.8 60.0 .2563 .5218 .01604 1206.7 28.06 1059.9 1088.0 65.0 .3056 .6222 .01605 1021.4 33.05 1057.1 1090.2 70.0 .3631 .7392 .01606 867.9 38.04 1054.3 1092.3 75.0 .4298 .8750 .01607 740.0 43.03 1051.5 1094.5 80.0 .5069 1.0321 .01608 633.1 48.02 1048.6 1096.6 85.0 .5959 1.2133 .01609 543.5 53.00 1045.8 1098.8 90.0 .6982 1.4515 .01610 468.0 57.99 1042.9 1100.9 95.0 .8153 1.6600 .01612 404.3 62.98 1040.1 1103.1 100.0 .9492 1.9325 .01613 350.4 67.97 1037.2 1105.2 105.0 1.1016 2.2429 .01615 304.5 72.95 10 34.3 1107.3 110.0 1.2748 2.5955 .01617 265.4 77.94 10 31.6 1109.5 115.0 1.4709 2.9948 .01618 231.9 82.93 10 28.7 1111.6 120.0 1.6924 3.4458 .01620 203.3 87.92 10 25.8 1113.7 125.0 1.9420 3.9539 .01622 178.6 92.91 10 22.9 1115.8 130.0 2.2225 4.5251 .01625 157.34 97.90 1020.0 1117.9 135.0 2.5370 5.1653 .01627 138.95 102.90 1017.0 1119.9 140.0 2.8886 5.8812 .01629 123.01 107.89 1014.1 1122.0 145.0 3.281 6.680 .01632 109.15 112.89 1011.2 1124.1 150.0 3.718 7.569 .01634 97.07 117.89 1008.2 1126.1 160.0 4.741 9.652 .01639 77.29 127.89 1002.3 1130.2 170.0 5.992 12.199 .01645 62.06 137.90 996.3 1134.2 180.0 7.510 15.291 .01651 50.23 147.92 990.2 1138.1 190.0 9.339 19.014 .01657 40.96 157.95 984.1 1142.0 200.0 11.526 23.467 .01663 33.64 167.99 977.9 1145.9 210.0 14.123 28.755 .01670 27.82 178.05 971.6 1149.7 220.0 17.186 34.992 .01677 23.15 188.13 965.2 1153.4 230.0 20.780 42.308 .01684 19.38 198.23 958.8 1157.0 240.0 24.969 50.837 .01692 16.32 208.34 952.2 1160.5 250.0 29.825 60.725 .01700 13.82 218.48 945.5 1164.0

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G.E. TABLE 3A 9C

PARKER BOILER CO. TABLE 3A

THERMODYNAMIC PROPERTIES OF SATURATED STEAM BASED ON TEMPERATURES

ABSOLUTE PRESSURE

SPECIFIC VOLUME CU FT/LB

ENTHALPY BTU/LB TEMP. F

+ PSI IN HG SAT. LIQUID vf SAT. VAPOR

vg SAT. LIQUID

hf EVAP.

hfg SAT. VAPOR

hg 32.0 .08854 .1803 .01602 3306.0 0.00 1075.8 1075.8 35.0 .09995 .2035 .01602 2947.0 3.02 1074.1 1077.1 40.0 .12170 .2478 .01602 2444.0 8.05 1071.3 1079.3 45.0 .14752 .3004 .01602 2036.4 13.06 1068.4 1081.5 50.0 .17811 .3626 .01603 1703.2 18.07 1065.6 1083.7

55.0 .2141 .4359 .01603 1430.7 23.07 1062.7 1085.8 60.0 .2563 .5218 .01604 1206.7 28.06 1059.9 1088.0 65.0 .3056 .6222 .01605 1021.4 33.05 1057.1 1090.2 70.0 .3631 .7392 .01606 867.9 38.04 1054.3 1092.3 75.0 .4298 .8750 .01607 740.0 43.03 1051.5 1094.5

80.0 .5069 1.0321 .01608 633.1 48.02 1048.6 1096.6 85.0 .5959 1.2133 .01609 543.5 53.00 1045.8 1098.8 90.0 .6982 1.4515 .01610 468.0 57.99 1042.9 1100.9 95.0 .8153 1.6600 .01612 404.3 62.98 1040.1 1103.1

100.0 .9492 1.9325 .01613 350.4 67.97 1037.2 1105.2

105.0 1.1016 2.2429 .01615 304.5 72.95 1034.3 1107.3 110.0 1.2748 2.5955 .01617 265.4 77.94 1031.6 1109.5 115.0 1.4709 2.9948 .01618 231.9 82.93 1028.7 1111.6 120.0 1.6924 3.4458 .01620 203.3 87.92 1025.8 1113.7 125.0 1.9420 3.9539 .01622 178.6 92.91 1022.9 1115.8

130.0 2.2225 4.5251 .01625 157.34 97.90 1020.0 1117.9 135.0 2.5370 5.1653 .01627 138.95 102.90 1017.0 1119.9 140.0 2.8886 5.8812 .01629 123.01 107.89 1014.1 1122.0 145.0 3.281 6.680 .01632 109.15 112.89 1011.2 1124.1 150.0 3.718 7.569 .01634 97.07 117.89 1008.2 1126.1

160.0 4.741 9.652 .01639 77.29 127.89 1002.3 1130.2 170.0 5.992 12.199 .01645 62.06 137.90 996.3 1134.2 180.0 7.510 15.291 .01651 50.23 147.92 990.2 1138.1 190.0 9.339 19.014 .01657 40.96 157.95 984.1 1142.0 200.0 11.526 23.467 .01663 33.64 167.99 977.9 1145.9

210.0 14.123 28.755 .01670 27.82 178.05 971.6 1149.7 220.0 17.186 34.992 .01677 23.15 188.13 965.2 1153.4 230.0 20.780 42.308 .01684 19.38 198.23 958.8 1157.0 240.0 24.969 50.837 .01692 16.32 208.34 952.2 1160.5 250.0 29.825 60.725 .01700 13.82 218.48 945.5 1164.0

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