Thermodynamics Appendix English Units

  • Upload
    atoro91

  • View
    75

  • Download
    3

Embed Size (px)

DESCRIPTION

English Units(not SI)

Citation preview

cen84959_ap02.qxd 4/27/05 3:02 PM Page 933

Appendix 2PROPERTY TABLES AND CHARTS (ENGLISH UNITS)Table A1E Table A2E Table A3E Table A4E Table A5E Table A6E Table A7E Table A8E Figure A9E Figure A10E Table A11E Table A12E Table A13E Figure A14EMolar mass, gas constant, and critical-point properties Ideal-gas specific heats of various common gases Properties of common liquids, solids, and foods Saturated waterTemperature table Saturated waterPressure table Superheated water Compressed liquid water Saturated icewater vapor T-s diagram for water Mollier diagram for water Saturated refrigerant-134a Temperature table Saturated refrigerant-134aPressure table Superheated refrigerant-134a P-h diagram for refrigerant-134a

Table A16E Properties of the atmosphere at high altitude Table A17E Ideal-gas properties of air Table A18E Ideal-gas properties of nitrogen, N2 Table A19E Ideal-gas properties of oxygen, O2 Table A20E Ideal-gas properties of carbon dioxide, CO2 Table A21E Ideal-gas properties of carbon monoxide, CO Table A22E Ideal-gas properties of hydrogen, H2 Table A23E Ideal-gas properties of water vapor, H2O Table A26E Enthalpy of formation, Gibbs function of formation, and absolute entropy at 77C, 1 atm Table A27E Properties of some common fuels and hydrocarbons Figure A31E Psychrometric chart at 1 atm total pressure

|

933

cen84959_ap02.qxd 4/27/05 3:02 PM Page 934

934

|

Thermodynamics

TABLE A1EMolar mass, gas constant, and critical-point properties Molar mass, M lbm/lbmol 28.97 17.03 39.948 78.115 159.808 58.124 44.01 28.011 153.82 70.906 119.38 120.91 102.92 30.020 46.07 28.054 4.003 86.178 2.016 83.80 16.043 32.042 50.488 20.183 28.013 44.013 31.999 44.097 42.081 64.063 102.03 137.37 18.015 131.30 Gas constant, R Btu/ lbm R* 0.06855 0.1166 0.04971 0.02542 0.01243 0.03417 0.04513 0.07090 0.01291 0.02801 0.01664 0.01643 0.01930 0.06616 0.04311 0.07079 0.4961 0.02305 0.9851 0.02370 0.1238 0.06198 0.03934 0.09840 0.07090 0.04512 0.06206 0.04504 0.04719 0.03100 0.01946 0.01446 0.1102 0.01513 psia ft3/ lbm R* 0.3704 0.6301 0.2686 0.1374 0.06714 0.1846 0.2438 0.3831 0.06976 0.1517 0.08988 0.08874 0.1043 0.3574 0.2329 0.3825 2.6809 0.1245 5.3224 0.1280 0.6688 0.3349 0.2125 0.5316 0.3830 0.2438 0.3353 0.2433 0.2550 1.1675 0.1052 0.07811 0.5956 0.08172 Critical-point properties Temperature, R 238.5 729.8 272 1012 1052 765.2 547.5 240 1001.5 751 965.8 692.4 813.0 549.8 929.0 508.3 9.5 914.2 59.9 376.9 343.9 923.7 749.3 80.1 227.1 557.4 278.6 665.9 656.9 775.2 673.6 848.1 1164.8 521.55 Pressure, psia 547 1636 705 714 1500 551 1071 507 661 1120 794 582 749 708 926 742 33.2 439 188.1 798 673 1154 968 395 492 1054 736 617 670 1143 588.7 635 3200 852 Volume, ft3/lbmol 1.41 1.16 1.20 4.17 2.17 4.08 1.51 1.49 4.42 1.99 3.85 3.49 3.16 2.37 2.68 1.99 0.926 5.89 1.04 1.48 1.59 1.89 2.29 0.668 1.44 1.54 1.25 3.20 2.90 1.95 3.19 3.97 0.90 1.90

Substance Air Ammonia Argon Benzene Bromine n-Butane Carbon dioxide Carbon monoxide Carbon tetrachloride Chlorine Chloroform Dichlorodifluoromethane (R-12) Dichlorofluoromethane (R-21) Ethane Ethyl alcohol Ethylene Helium n-Hexane Hydrogen (normal) Krypton Methane Methyl alcohol Methyl chloride Neon Nitrogen Nitrous oxide Oxygen Propane Propylene Sulfur dioxide Tetrafluoroethane (R-134a) Trichlorofluoromethane (R-11) Water Xenon*Calculated from R Ru /M, where Ru

Formula NH3 Ar C6H6 Br2 C4H10 CO2 CO CCl4 Cl2 CHCl3 CCl2F2 CHCl2F C2H6 C2H5OH C2H4 He C6H14 H2 Kr CH4 CH3OH CH3Cl Ne N2 N2O O2 C3H8 C3H6 SO2 CF3CH2F CCl3F H2O Xe

1.98588 Btu/lbmol R

10.7316 psia ft3/lbmol R and M is the molar mass.

Source: K. A. Kobe and R. E. Lynn, Jr., Chemical Review 52 (1953), pp. 117236, and ASHRAE, Handbook of Fundamentals (Atlanta, GA: American Society of Heating, Refrigerating, and Air-Conditioning Engineers, Inc., 1993), pp. 16.4 and 36.1.

cen84959_ap02.qxd 4/27/05 3:02 PM Page 935

Appendix 2 TABLE A2EIdeal-gas specific heats of various common gases (a) At 80F Gas Air Argon Butane Carbon dioxide Carbon monoxide Ethane Ethylene Helium Hydrogen Methane Neon Nitrogen Octane Oxygen Propane Steam Formula Ar C4H10 CO2 CO C2H6 C2H4 He H2 CH4 Ne N2 C8H18 O2 C3H8 H2O Gas constant, R Btu/lbm R 0.06855 0.04971 0.03424 0.04513 0.07090 0.06616 0.07079 0.4961 0.9851 0.1238 0.09840 0.07090 0.01742 0.06206 0.04504 0.1102 cp Btu/lbm R 0.240 0.1253 0.415 0.203 0.249 0.427 0.411 1.25 3.43 0.532 0.246 0.248 0.409 0.219 0.407 0.445 cv Btu/lbm R 0.171 0.0756 0.381 0.158 0.178 0.361 0.340 0.753 2.44 0.403 0.1477 0.177 0.392 0.157 0.362 0.335

|

935

k 1.400 1.667 1.09 1.285 1.399 1.183 1.208 1.667 1.404 1.32 1.667 1.400 1.044 1.395 1.124 1.329

Source: Gordon J. Van Wylen and Richard E. Sonntag, Fundamentals of Classical Thermodynamics, English/SI Version, 3rd ed. (New York: John Wiley & Sons, 1986), p. 687, Table A8E.

cen84959_ap02.qxd 4/27/05 3:02 PM Page 936

936

|

Thermodynamics

TABLE A2EIdeal-gas specific heats of various common gases (Continued) (b) At various temperatures Temp., F cp Btu/lbm R cv Btu/lbm R Air 40 100 200 300 400 500 600 700 800 900 1000 1500 2000 0.240 0.240 0.241 0.243 0.245 0.248 0.250 0.254 0.257 0.259 0.263 0.276 0.286 0.171 0.172 0.173 0.174 0.176 0.179 0.182 0.185 0.188 0.191 0.195 0.208 0.217 Hydrogen, H2 40 100 200 300 400 500 600 700 800 900 1000 1500 2000 3.397 3.426 3.451 3.461 3.466 3.469 3.473 3.477 3.494 3.502 3.513 3.618 3.758 2.412 2.441 2.466 2.476 2.480 2.484 2.488 2.492 2.509 2.519 2.528 2.633 2.773 1.409 1.404 1.399 1.398 1.397 1.397 1.396 1.395 1.393 1.392 1.390 1.374 1.355 0.248 0.248 0.249 0.250 0.251 0.254 0.256 0.260 0.262 0.265 0.269 0.283 0.293 1.401 1.400 1.397 1.394 1.389 1.383 1.377 1.371 1.365 1.358 1.353 1.330 1.312 0.195 0.205 0.217 0.229 0.239 0.247 0.255 0.262 0.269 0.275 0.280 0.298 0.312 k cp Btu/lbm R cv Btu/lbm R k cp cv Btu/lbm R Btu/lbm R k Carbon monoxide, CO 0.248 0.249 0.249 0.251 0.253 0.256 0.259 0.262 0.266 0.269 0.273 0.287 0.297 0.177 0.178 0.179 0.180 0.182 0.185 0.188 0.191 0.195 0.198 0.202 0.216 0.226 Oxygen, O2 1.400 1.399 1.398 1.396 1.393 1.388 1.383 1.377 1.371 1.364 1.359 1.334 1.319 0.219 0.220 0.223 0.226 0.230 0.235 0.239 0.242 0.246 0.249 0.252 0.263 0.270 0.156 0.158 0.161 0.164 0.168 0.173 0.177 0.181 0.184 0.187 0.190 0.201 0.208 1.397 1.394 1.387 1.378 1.368 1.360 1.352 1.344 1.337 1.331 1.326 1.309 1.298 1.400 1.399 1.397 1.394 1.389 1.384 1.377 1.371 1.364 1.357 1.351 1.328 1.314

Carbon dioxide, C02 0.150 0.160 0.172 0.184 0.193 0.202 0.210 0.217 0.224 0.230 0.235 0.253 0.267 Nitrogen, N2 0.177 0.178 0.178 0.179 0.180 0.183 0.185 0.189 0.191 0.194 0.198 0.212 0.222 1.300 1.283 1.262 1.246 1.233 1.223 1.215 1.208 1.202 1.197 1.192 1.178 1.169

Note: The unit Btu/lbm R is equivalent to Btu/lbm F. Source: Kenneth Wark, Thermodynamics, 4th ed. (New York: McGraw-Hill, 1983), p. 830, Table A4. Originally published in Tables of Properties of Gases, NBS Circular 564, 1955.

cen84959_ap02.qxd 4/27/05 3:02 PM Page 937

Appendix 2 TABLE A2EIdeal-gas specific heats of various common gases (Concluded ) (c) As a function of temperature cp a bT cT 2 dT 3(T in R, cp in Btu/lbmol R)

|

937

Substance Nitrogen Oxygen Air Hydrogen Carbon monoxide Carbon dioxide Water vapor Nitric oxide Nitrous oxide Nitrogen dioxide Ammonia Sulfur Sulfur dioxide Sulfur trioxide Acetylene Benzene Methanol Ethanol Hydrogen chloride Methane Ethane Propane n-Butane i-Butane n-Pentane n-Hexane Ethylene Propylene

Formula N2 O2 H2 CO CO2 H2O NO N2O NO2 NH3 S2 SO2 SO3 C2H2 C6H6 CH4O C2H6O HCl CH4 C2H6 C3H8 C4H10 C4H10 C5H12 C6H14 C2H4 C3H6

a 6.903 6.085 6.713 6.952 6.726 5.316 7.700 7.008 5.758 5.48 6.5846 6.499 6.157 3.918 5.21 8.650 4.55 4.75 7.244 4.750 1.648 0.966 0.945 1.890 1.618 1.657 0.944 0.753

b 0.02085 0.2017 0.02609 0.02542 0.02222 0.79361 0.02552 0.01247 0.7780 0.7583 0.34028 0.2943 0.7689 1.935 1.2227 6.4322 1.214 2.781 0.1011 0.6666 2.291 4.044 4.929 5.520 6.028 7.328 2.075 3.162 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 102 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2

c 0.05957 0.05275 0.03540 0.02952 0.03960 0.2581 0.07781 0.07185 0.2596 0.260 0.073034 0.1200 0.2810 0.8256 0.4812 2.327 0.0898 0.7651 0.09783 0.09352 0.4722 1.159 1.352 1.696 1.656 2.112 0.6151 0.8981 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 105 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5

d 0.1176 0.05372 0.08052 0.03565 0.09100 0.3059 0.1472 0.1715 0.4331 0.322 0.27402 0.1632 0.3527 1.328 0.7457 3.179 0.329 0.821 0.1776 0.4510 0.2984 1.300 1.433 2.044 1.732 2.363 0.7326 1.008 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 109 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9

% error Temperature range, R Max. Avg. 491-3240 491-3240 491-3240 491-3240 491-3240 491-3240 491-3240 491-2700 491-2700 491-2700 491-2700 491-3240 491-3240 491-2340 491-2700 491-2700 491-1800 491-2700 491-2740 491-2740 491-2740 491-2740 491-2740 491-2740 491-2740 491-2740 491-2740 491-2740 0.59 1.19 0.72 1.02 0.89 0.67 0.53 0.97 0.59 0.46 0.91 0.99 0.45 0.29 1.46 0.34 0.18 0.40 0.22 1.33 0.83 0.40 0.54 0.25 0.56 0.72 0.54 0.73 0.34 0.28 0.33 0.26 0.37 0.22 0.24 0.36 0.26 0.18 0.36 0.38 0.24 0.13 0.59 0.20 0.08 0.22 0.08 0.57 0.28 0.12 0.24 0.13 0.21 0.20 0.13 0.17

Source: Chemical and Process Thermodynamics 3/E by Kyle, B. G., 2000. Adapted by permission of Pearson Education, Inc., Upper Saddle River, NJ.

cen84959_ap02.qxd 4/27/05 3:02 PM Page 938

938

|

Thermodynamics

TABLE A3EProperties of common liquids, solids, and foods (a) Liquids Boiling data at 1 atm Normal boiling point, F 27.9 Latent heat of vaporization, hfg Btu/lbm 24.54 Freezing data Freezing point, F 107.9 Latent heat of fusion, hif Btu/lbm 138.6 Liquid properties Temperature, F 27.9 0 40 80 302.6 68 Density, r lbm/ft3 42.6 41.3 39.5 37.5 87.0 54.9 Specific heat, cp Btu/lbm R 1.06 1.083 1.103 1.135 0.272 0.411

Substance Ammonia

Argon Benzene Brine (20% sodium chloride by mass) n-Butane Carbon dioxide Ethanol Ethyl alcohol Ethylene glycol Glycerine Helium Hydrogen Isobutane Kerosene Mercury Methane Methanol Nitrogen Octane Oil (light) Oxygen Petroleum Propane

302.6 176.4

69.5 169.4

308.7 41.9

12.0 54.2

219.0 31.1 109.2* 172.8 173.5 388.6 355.8 452.1 423.0 10.9 399559 674.1 258.7 148.1 320.4 256.6 297.3 43.7

165.6 99.6 (at 32F) 360.5 368 344.0 419 9.80 191.7 157.8 108 126.7 219.6 473 85.4 131.7 91.5 99165 184.0

0.7 217.3 69.8 173.6 248.8 12.6 66.0 434.5 255.5 12.8 38.0 296.0 143.9 346.0 71.5 361.8 305.8

34.5 46.9 46.4 77.9 86.3 25.6 45.5 4.90 25.1 42.7 10.9 77.9 5.9 34.4

Refrigerant-134a

15.0

93.3

141.9

Water

212

970.1

32

143.5

68 31.1 32 77 68 68 68 452.1 423.0 10.9 68 77 258.7 160 77 320.4 260 68 77 297.3 68 43.7 32 100 40 15 32 90 32 90 150 212

71.8 37.5 57.8 48.9 49.3 69.2 78.7 9.13 4.41 37.1 51.2 847 26.4 20.0 49.1 50.5 38.2 43.9 56.8 71.2 40.0 36.3 33.0 29.4 88.5 86.0 80.9 73.6 62.4 62.1 61.2 59.8

0.743 0.552 0.583 0.588 0.678 0.678 0.554 5.45 2.39 0.545 0.478 0.033 0.834 1.074 0.609 0.492 0.643 0.502 0.430 0.408 0.478 0.538 0.604 0.673 0.283 0.294 0.318 0.348 1.01 1.00 1.00 1.01

*Sublimation temperature. (At pressures below the triple-point pressure of 75.1 psia, carbon dioxide exists as a solid or gas. Also, the freezing-point temperature of carbon dioxide is the triple-point temperature of 69.8F.)

cen84959_ap02.qxd 4/27/05 3:02 PM Page 939

Appendix 2 TABLE A3EProperties of common liquids, solids, and foods (Continued) (b) Solids (values are for room temperature unless indicated otherwise) Density, r lbm/ft3 Specific heat, cp Btu/lbm R Density, r lbm/ft3

|

939

Substance MetalsAluminum 100F 32F 100F 200F 300F 400F 500F Bronze (76% Cu, 2% Zn, 2% Al) Brass, yellow (65% Cu, 35% Zn) Copper 60F 0F 100F 200F 390F Iron Lead Magnesium Nickel Silver Steel, mild Tungsten

Substance Nonmetals

Specific heat, cp Btu/lbm R

170

517 519

0.192 0.212 0.218 0.224 0.229 0.235 0.240 0.0955 0.0955

555

490 705 108 555 655 489 1211

0.0862 0.0893 0.0925 0.0938 0.0963 0.107 0.030 0.239 0.105 0.056 0.119 0.031

Asphalt Brick, common Brick, fireclay (500C) Concrete Clay Diamond Glass, window Glass, pyrex Graphite Granite Gypsum or plaster board Ice 50F 0F 20F 32F Limestone Marble Plywood (Douglas fir) Rubber (soft) Rubber (hard) Sand Stone Woods, hard (maple, oak, etc.) Woods, soft (fir, pine, etc.)

132 120 144 144 62.4 151 169 139 156 169 50

0.220 0.189 0.229 0.156 0.220 0.147 0.191 0.200 0.170 0.243 0.260 0.424 0.471 0.491 0.502 0.217 0.210

57.5 103 162 34.0 68.7 71.8 94.9 93.6 45.0 32.0

(c) FoodsSpecific heat, Btu/lbm R Above freezing 0.873 0.801 0.737 0.921 0.513 0.841 0.793 0.793 0.793 0.705 Below freezing 0.453 0.426 0.402 0.471 0.249 0.318 0.441 0.423 0.423 0.423 0.390 Latent heat of fusion, Btu/lbm 121 108 96 129 23 56 115 106 106 106 90 Water content, % (mass) 95 88 87 78 64 83 93 90 94 64 93 Specific heat, Btu/lbm R Freezing point, Above Below F freezing freezing 32 31 31 31 28 28 31 31 31 31 0.961 0.905 0.897 0.825 0.713 0.865 0.945 0.921 0.953 0.713 0.945 0.487 0.465 0.462 0.435 0.393 0.450 0.481 0.471 0.484 0.393 0.481 Latent heat of fusion, Btu/lbm 136 126 125 112 92 119 134 129 135 92 134

Food Apples Bananas Beef round Broccoli Butter Cheese, Swiss Cherries Chicken Corn, sweet Eggs, whole Ice cream

Water content, % (mass) 84 75 67 90 16 39 80 74 74 74 63

Freezing point, F 30 31 31 14 29 27 31 31 22

Food Lettuce Milk, whole Oranges Potatoes Salmon fish Shrimp Spinach Strawberries Tomatoes, ripe Turkey Watermelon

Source: Values are obtained from various handbooks and other sources or are calculated. Water content and freezing-point data of foods are from ASHRAE, Handbook of Fundamentals, I-P version (Atlanta, GA: American Society of Heating, Refrigerating, and Air-Conditioning Engineers, Inc., 1993), Chap. 30, Table 1. Freezing point is the temperature at which freezing starts for fruits and vegetables, and the average freezing temperature for other foods.

cen84959_ap02.qxd 4/27/05 3:02 PM Page 940

940

|

Thermodynamics

TABLE A4ESaturated waterTemperature tableSpecific volume, ft3/lbm Sat. press., Psat psia 0.08871 0.09998 0.12173 0.14756 0.17812 0.21413 0.25638 0.30578 0.36334 0.43016 0.50745 0.59659 0.69904 0.81643 0.95052 1.2767 1.6951 2.2260 2.8931 3.7234 4.7474 5.9999 7.5197 9.3497 11.538 14.136 14.709 17.201 20.795 24.985 29.844 35.447 41.877 49.222 57.573 67.028 77.691 89.667 103.07 118.02 134.63 153.03 173.36 195.74 220.33 Sat. liquid, vf 0.01602 0.01602 0.01602 0.01602 0.01602 Sat. vapor, vg 3299.9 2945.7 2443.6 2035.8 1703.1 Sat. liquid, uf 0.000 3.004 8.032 13.05 18.07 23.07 28.08 33.08 38.08 43.07 48.06 53.06 58.05 63.04 68.03 78.01 88.00 97.99 107.98 117.98 127.98 138.00 148.02 158.05 168.10 178.15 180.16 188.22 198.31 208.41 218.54 228.68 238.85 249.04 259.26 269.51 279.79 290.11 300.46 310.85 321.29 331.76 342.29 352.87 363.50 Internal energy, Btu/lbm Sat. vapor, ug 1021.0 1022.0 1023.7 1025.3 1026.9 1028.6 1030.2 1031.8 1033.5 1035.1 1036.7 1038.3 1040.0 1041.6 1043.2 1046.4 1049.6 1052.7 1055.9 1059.0 1062.0 1065.1 1068.1 1071.0 1074.0 1076.8 1077.4 1079.6 1082.4 1085.1 1087.7 1090.3 1092.8 1095.2 1097.5 1099.8 1101.9 1104.0 1105.9 1107.7 1109.4 1111.0 1112.5 1113.9 1115.1 Sat. liquid, hf 0.000 3.004 8.032 13.05 18.07 23.07 28.08 33.08 38.08 43.07 48.07 53.06 58.05 63.04 68.03 78.02 88.00 97.99 107.99 117.99 128.00 138.02 148.04 158.08 168.13 178.20 180.21 188.28 198.37 208.49 218.63 228.79 238.98 249.20 259.45 269.73 280.05 290.40 300.80 311.24 321.73 332.28 342.88 353.53 364.25 Enthalpy, Btu/lbm Sat. vapor, hg 1075.2 1076.5 1078.7 1080.9 1083.1 1085.3 1087.4 1089.6 1091.8 1093.9 1096.1 1098.3 1100.4 1102.6 1104.7 1109.0 1113.2 1117.4 1121.6 1125.7 1129.8 1133.9 1137.9 1141.8 1145.7 1149.5 1150.3 1153.3 1157.0 1160.5 1164.0 1167.4 1170.7 1173.9 1177.0 1180.0 1182.8 1185.5 1188.1 1190.5 1192.7 1194.8 1196.7 1198.5 1200.1 Sat. liquid, sf 0.00000 0.00609 0.01620 0.02620 0.03609 0.04586 0.05554 0.06511 0.07459 0.08398 0.09328 0.10248 0.11161 0.12065 0.12961 0.14728 0.16466 0.18174 0.19855 0.21508 0.23136 0.24739 0.26318 0.27874 0.29409 0.30922 0.31222 0.32414 0.33887 0.35342 0.36779 0.38198 0.39601 0.40989 0.42361 0.43720 0.45065 0.46396 0.47716 0.49024 0.50321 0.51607 0.52884 0.54152 0.55411 Entropy, Btu/lbm R Sat. vapor, sg 2.1867 2.1762 2.1589 2.1421 2.1256 2.1096 2.0940 2.0788 2.0639 2.0494 2.0352 2.0214 2.0079 1.9947 1.9819 1.9570 1.9332 1.9105 1.8888 1.8680 1.8481 1.8289 1.8106 1.7930 1.7760 1.7597 1.7565 1.7439 1.7288 1.7141 1.6999 1.6862 1.6730 1.6601 1.6475 1.6354 1.6235 1.6120 1.6007 1.5897 1.5789 1.5683 1.5580 1.5478 1.5378

Temp., T F 32.018 35 40 45 50 55 60 65 70 75 80 85 90 95 100 110 120 130 140 150 160 170 180 190 200 210 212 220 230 240 250 260 270 280 290 300 310 320 330 340 350 360 370 380 390

Evap., ufg 1021.0 1019.0 1015.6 1012.2 1008.9 1005.5 1002.1 998.76 995.39 992.02 988.65 985.28 981.90 978.52 975.14 968.36 961.56 954.73 947.87 940.98 934.05 927.08 920.06 912.99 905.87 898.68 897.24 891.43 884.10 876.70 869.21 861.62 853.94 846.16 838.27 830.25 822.11 813.84 805.43 796.87 788.16 779.28 770.23 761.00 751.58

Evap., hfg 1075.2 1073.5 1070.7 1067.8 1065.0 1062.2 1059.4 1056.5 1053.7 1050.9 1048.0 1045.2 1042.4 1039.5 1036.7 1031.0 1025.2 1019.4 1013.6 1007.8 1001.8 995.88 989.85 983.76 977.60 971.35 970.09 965.02 958.59 952.06 945.41 938.65 931.76 924.74 917.57 910.24 902.75 895.09 887.25 879.22 870.98 862.53 853.86 844.96 835.81

Evap., sfg 2.18672 2.17011 2.14271 2.11587 2.08956 2.06377 2.03847 2.01366 1.98931 1.96541 1.94196 1.91892 1.89630 1.87408 1.85225 1.80970 1.76856 1.72877 1.69024 1.65291 1.61670 1.58155 1.54741 1.51421 1.48191 1.45046 1.44427 1.41980 1.38989 1.36069 1.33216 1.30425 1.27694 1.25018 1.22393 1.19818 1.17289 1.14802 1.12355 1.09945 1.07570 1.05227 1.02914 1.00628 0.98366

0.01603 1430.4 0.01604 1206.1 0.01604 1020.8 0.01605 867.18 0.01606 739.27 0.01607 0.01609 0.01610 0.01612 0.01613 0.01617 0.01620 0.01625 0.01629 0.01634 0.01639 0.01645 0.01651 0.01657 0.01663 0.01670 0.01671 0.01677 0.01684 0.01692 0.01700 0.01708 0.01717 0.01726 0.01735 0.01745 0.01755 0.01765 0.01776 0.01787 0.01799 0.01811 0.01823 0.01836 0.01850 632.41 542.80 467.40 403.74 349.83 264.96 202.94 157.09 122.81 96.929 77.185 61.982 50.172 40.920 33.613 27.798 26.782 23.136 19.374 16.316 13.816 11.760 10.059 8.6439 7.4607 6.4663 5.6266 4.9144 4.3076 3.7885 3.3425 2.9580 2.6252 2.3361 2.0842

cen84959_ap02.qxd 4/27/05 3:02 PM Page 941

Appendix 2 TABLE A4ESaturated waterTemperature table (Concluded)Specific volume, ft3/lbm Sat. press., Psat psia 247.26 276.69 308.76 343.64 381.49 422.47 466.75 514.52 565.96 621.24 680.56 744.11 812.11 884.74 962.24 1044.8 1132.7 1226.2 1325.5 1430.8 1542.5 1660.9 1786.2 1918.9 2059.3 2207.8 2364.9 2531.2 2707.3 2894.1 3093.0 3200.1 Sat. liquid, vf 0.01864 0.01878 0.01894 0.01910 0.01926 0.01944 0.01962 0.01981 0.02001 0.02022 0.02044 0.02067 0.02092 0.02118 0.02146 0.02176 0.02207 0.02242 0.02279 0.02319 0.02362 0.02411 0.02464 0.02524 0.02593 0.02673 0.02767 0.02884 0.03035 0.03255 0.03670 0.04975 Sat. vapor, vg 1.8639 1.6706 1.5006 1.3505 1.2178 1.0999 0.99510 0.90158 0.81794 0.74296 0.67558 0.61489 0.56009 0.51051 0.46553 0.42465 0.38740 0.35339 0.32225 0.29367 0.26737 0.24309 0.22061 0.19972 0.18019 0.16184 0.14444 0.12774 0.11134 0.09451 Sat. liquid, uf 374.19 384.94 395.76 406.65 417.61 428.66 439.79 451.01 462.34 473.77 485.32 496.99 508.80 520.76 532.88 545.18 557.68 570.40 583.37 596.61 610.18 624.11 638.47 653.35 668.86 685.16 702.48 721.23 742.11 766.81 Internal energy, Btu/lbm Sat. vapor, ug 1116.2 1117.1 1117.8 1118.4 1118.9 1119.1 1119.2 1119.0 1118.7 1118.1 1117.3 1116.2 1114.8 1113.1 1111.1 1108.8 1106.0 1102.8 1099.2 1095.0 1090.3 1084.8 1078.6 1071.5 1063.2 1053.6 1042.2 1028.5 1011.1 987.6 948.3 866.6 Sat. liquid, hf 375.04 385.90 396.84 407.86 418.97 430.18 441.48 452.90 464.43 476.09 487.89 499.84 511.94 524.23 536.70 549.39 562.31 575.49 588.95 602.75 616.92 631.52 646.62 662.32 678.74 696.08 714.59 734.74 757.32 784.24 822.76 896.07 Enthalpy, Btu/lbm Sat. vapor, hg 1201.4 1202.6 1203.6 1204.3 1204.8 1205.1 1205.1 1204.9 1204.3 1203.5 1202.3 1200.8 1199.0 1196.7 1194.0 1190.9 1187.2 1183.0 1178.2 1172.8 1166.6 1159.5 1151.5 1142.4 1131.9 1119.7 1105.4 1088.3 1066.9 1038.2 991.1 896.1 Sat. liquid, sf 0.56663 0.57907 0.59145 0.60377 0.61603 0.62826 0.64044 0.65260 0.66474 0.67686 0.68899 0.70112 0.71327 0.72546 0.73770 0.75000 0.76238 0.77486 0.78748 0.80026 0.81323 0.82645 0.83998 0.85389 0.86828 0.88332 0.89922 0.91636 0.93541 0.95797 0.99023 1.05257 Entropy, Btu/lbm R

|

941

Temp., T F 400 410 420 430 440 450 460 470 480 490 500 510 520 530 540 550 560 570 580 590 600 610 620 630 640 650 660 670 680 690 700 705.10

Evap., ufg 741.97 732.14 722.08 711.80 701.26 690.47 679.39 668.02 656.34 644.32 631.94 619.17 605.99 592.35 578.23 563.58 548.33 532.45 515.84 498.43 480.10 460.73 440.14 418.12 394.36 368.44 339.74 307.22 269.00 220.77 146.50 0

Evap., hfg 826.39 816.71 806.74 796.46 785.87 774.94 763.65 751.98 739.91 727.40 714.44 700.99 687.01 672.47 657.31 641.47 624.91 607.55 589.29 570.04 549.67 528.03 504.92 480.07 453.14 423.65 390.84 353.54 309.57 253.96 168.32 0

Evap., sfg 0.96127 0.93908 0.91707 0.89522 0.87349 0.85187 0.83033 0.80885 0.78739 0.76594 0.74445 0.72290 0.70126 0.67947 0.65751 0.63532 0.61284 0.59003 0.56679 0.54306 0.51871 0.49363 0.46765 0.44056 0.41206 0.38177 0.34906 0.31296 0.27163 0.22089

Sat. vapor, sg 1.5279 1.5182 1.5085 1.4990 1.4895 1.4801 1.4708 1.4615 1.4521 1.4428 1.4334 1.4240 1.4145 1.4049 1.3952 1.3853 1.3752 1.3649 1.3543 1.3433 1.3319 1.3201 1.3076 1.2944 1.2803 1.2651 1.2483 1.2293 1.2070 1.1789

0.07482 801.75 0.04975 866.61

0.14514 1.1354 0 1.0526

Source: Tables A4E through A8E are generated using the Engineering Equation Solver (EES) software developed by S. A. Klein and F. L. Alvarado. The routine used in calculations is the highly accurate Steam_IAPWS, which incorporates the 1995 Formulation for the Thermodynamic Properties of Ordinary Water Substance for General and Scientific Use, issued by The International Association for the Properties of Water and Steam (IAPWS). This formulation replaces the 1984 formulation of Haar, Gallagher, and Kell (NBS/NRC Steam Tables, Hemisphere Publishing Co., 1984), which is also available in EES as the routine STEAM. The new formulation is based on the correlations of Saul and Wagner (J. Phys. Chem. Ref. Data, 16, 893, 1987) with modifications to adjust to the International Temperature Scale of 1990. The modifications are described by Wagner and Pruss (J. Phys. Chem. Ref. Data, 22, 783, 1993). The properties of ice are based on Hyland and Wexler, Formulations for the Thermodynamic Properties of the Saturated Phases of H2O from 173.15 K to 473.15 K, ASHRAE Trans., Part 2A, Paper 2793, 1983.

cen84959_ap02.qxd 4/27/05 3:02 PM Page 942

942

|

Thermodynamics

TABLE A5ESaturated waterPressure tableSpecific volume, ft3/lbm Sat. temp., Tsat F 101.69 126.02 141.41 152.91 162.18 170.00 182.81 193.16 211.95 212.99 227.92 240.03 250.30 259.25 267.22 274.41 280.99 287.05 292.69 297.95 302.91 307.59 312.02 316.24 320.26 324.11 327.81 334.77 341.25 347.32 353.03 358.42 363.54 368.41 373.07 377.52 381.80 400.97 417.35 431.74 444.62 456.31 467.04 476.97 486.24 Sat. liquid, vf 0.01614 0.01623 0.01630 0.01636 0.01641 0.01645 0.01652 0.01659 0.01671 0.01672 0.01683 0.01692 0.01700 0.01708 0.01715 0.01721 0.01727 0.01732 0.01738 0.01743 0.01748 0.01752 0.01757 0.01761 0.01765 0.01770 0.01774 0.01781 0.01789 0.01796 0.01802 0.01809 0.01815 0.01821 0.01827 0.01833 0.01839 0.01865 0.01890 0.01912 0.01934 0.01955 0.01975 0.01995 0.02014 Sat. vapor, vg 333.49 173.71 118.70 90.629 73.525 61.982 47.347 38.425 26.805 26.297 20.093 16.307 13.749 11.901 10.501 9.4028 8.5175 7.7882 7.1766 6.6560 6.2075 5.8167 5.4733 5.1689 4.8972 4.6532 4.4327 4.0410 3.7289 3.4557 3.2202 3.0150 2.8347 2.6749 2.5322 2.4040 2.2882 1.8440 1.5435 1.3263 1.1617 1.0324 0.92819 0.84228 0.77020 Sat. liquid, uf 69.72 94.02 109.39 120.89 130.17 138.00 150.83 161.22 180.12 181.16 196.21 208.45 218.84 227.92 236.02 243.34 250.05 256.25 262.01 267.41 272.50 277.31 281.87 286.22 290.38 294.36 298.19 305.41 312.16 318.48 324.45 330.11 335.49 340.62 345.53 350.24 354.78 375.23 392.89 408.55 422.70 435.67 447.68 458.90 469.46 Internal energy, Btu/lbm Sat. vapor, ug 1043.7 1051.5 1056.3 1059.9 1062.7 1065.1 1068.9 1072.0 1077.4 1077.7 1081.8 1085.1 1087.8 1090.1 1092.1 1093.9 1095.4 1096.9 1098.1 1099.3 1100.4 1101.4 1102.3 1103.2 1104.0 1104.8 1105.5 1106.8 1107.9 1109.0 1109.9 1110.8 1111.6 1112.3 1113.0 1113.6 1114.1 1116.3 1117.7 1118.5 1119.0 1119.2 1119.1 1118.8 1118.3 Sat. liquid, hf 69.72 94.02 109.40 120.90 130.18 138.02 150.86 161.25 180.16 181.21 196.27 208.52 218.93 228.03 236.14 243.49 250.21 256.42 262.20 267.62 272.72 277.55 282.13 286.50 290.67 294.67 298.51 305.78 312.55 318.92 324.92 330.61 336.02 341.19 346.14 350.89 355.46 376.09 393.94 409.79 424.13 437.30 449.51 460.93 471.70 Enthalpy, Btu/lbm Sat. vapor, hg 1105.4 1115.8 1122.2 1126.9 1130.7 1133.9 1139.0 1143.1 1150.3 1150.7 1156.2 1160.6 1164.1 1167.2 1169.8 1172.2 1174.2 1176.1 1177.8 1179.4 1180.8 1182.1 1183.4 1184.5 1185.6 1186.6 1187.5 1189.2 1190.8 1192.1 1193.4 1194.5 1195.5 1196.4 1197.3 1198.1 1198.8 1201.6 1203.3 1204.4 1205.0 1205.2 1205.0 1204.5 1203.9 Sat. liquid, sf 0.13262 0.17499 0.20090 0.21985 0.23488 0.24739 0.26757 0.28362 0.31215 0.31370 0.33582 0.35347 0.36821 0.38093 0.39213 0.40216 0.41125 0.41958 0.42728 0.43443 0.44112 0.44741 0.45335 0.45897 0.46431 0.46941 0.47427 0.48341 0.49187 0.49974 0.50711 0.51405 0.52061 0.52682 0.53274 0.53839 0.54379 0.56784 0.58818 0.60590 0.62168 0.63595 0.64900 0.66107 0.67231 Entropy, Btu/lbm R Sat. vapor, sg 1.9776 1.9194 1.8858 1.8621 1.8438 1.8289 1.8056 1.7875 1.7566 1.7549 1.7319 1.7141 1.6995 1.6872 1.6766 1.6672 1.6588 1.6512 1.6442 1.6378 1.6319 1.6264 1.6212 1.6163 1.6117 1.6073 1.6032 1.5954 1.5883 1.5818 1.5757 1.5700 1.5647 1.5596 1.5548 1.5503 1.5460 1.5270 1.5111 1.4973 1.4852 1.4742 1.4642 1.4550 1.4463

Press., P psia 1 2 3 4 5 6 8 10 14.696 15 20 25 30 35 40 45 50 55 60 65 70 75 80 85 90 95 100 110 120 130 140 150 160 170 180 190 200 250 300 350 400 450 500 550 600

Evap., ufg 973.99 957.45 946.90 938.97 932.53 927.08 918.08 910.75 897.27 896.52 885.63 876.67 868.98 862.19 856.09 850.52 845.39 840.61 836.13 831.90 827.90 824.09 820.45 816.97 813.62 810.40 807.29 801.37 795.79 790.51 785.49 780.69 776.10 771.68 767.42 763.31 759.32 741.02 724.77 709.98 696.31 683.52 671.42 659.91 648.88

Evap., hfg 1035.7 1021.7 1012.8 1006.0 1000.5 995.88 988.15 981.82 970.12 969.47 959.93 952.03 945.21 939.16 933.69 928.68 924.03 919.70 915.61 911.75 908.08 904.58 901.22 898.00 894.89 891.89 888.99 883.44 878.20 873.21 868.45 863.88 859.49 855.25 851.16 847.19 843.33 825.47 809.41 794.65 780.87 767.86 755.48 743.60 732.15

Evap., sfg 1.84495 1.74444 1.68489 1.64225 1.60894 1.58155 1.53800 1.50391 1.44441 1.44441 1.39606 1.36060 1.33132 1.30632 1.28448 1.26506 1.24756 1.23162 1.21697 1.20341 1.19078 1.17895 1.16783 1.15732 1.14737 1.13791 1.12888 1.11201 1.09646 1.08204 1.06858 1.05595 1.04405 1.03279 1.02210 1.01191 1.00219 0.95912 0.92289 0.89143 0.86350 0.83828 0.81521 0.79388 0.77400

cen84959_ap02.qxd 4/27/05 3:02 PM Page 943

Appendix 2 TABLE A5ESaturated waterPressure table (Concluded)Specific volume, ft3/lbm Sat. temp., Tsat F 503.13 518.27 532.02 544.65 567.26 587.14 604.93 621.07 635.85 668.17 695.41 705.10 Sat. liquid, vf 0.02051 0.02087 0.02124 0.02159 0.02232 0.02307 0.02386 0.02470 0.02563 0.02860 0.03433 0.04975 Sat. vapor, vg 0.65589 0.56920 0.50107 0.44604 0.36241 0.30161 0.25516 0.21831 0.18815 0.13076 0.08460 0.04975 Sat. liquid, uf 488.96 506.74 523.19 538.58 566.89 592.79 616.99 640.03 662.33 717.67 783.39 866.61 Internal energy, Btu/lbm Sat. vapor, ug 1116.9 1115.0 1112.7 1110.1 1103.8 1096.3 1087.7 1077.9 1066.8 1031.2 969.8 866.6 Sat. liquid, hf 491.62 509.83 526.73 542.57 571.85 598.76 624.06 648.26 671.82 730.90 802.45 896.07 Enthalpy, Btu/lbm Sat. vapor, hg 1201.9 1199.3 1196.2 1192.6 1184.2 1174.4 1163.2 1150.6 1136.4 1091.7 Sat. liquid, sf 0.69279 0.71117 0.72793 0.74341 0.77143 0.79658 0.81972 0.84144 0.86224 0.91311 0.97321 1.05257 Entropy, Btu/lbm R

|

943

Press., P psia 700 800 900 1000 1200 1400 1600 1800 2000 2500 3000 3200.1

Evap., ufg 627.98 608.30 589.54 571.49 536.87 503.50 470.69 437.86 404.46 313.53 186.41 0

Evap., hfg 710.29 689.48 669.46 650.03 612.39 575.66 539.18 502.35 464.60 360.79

Evap., sfg 0.73771 0.70502 0.67505 0.64722 0.59632 0.54991 0.50645 0.46482 0.42409 0.31988

Sat. vapor, sg 1.4305 1.4162 1.4030 1.3906 1.3677 1.3465 1.3262 1.3063 1.2863 1.2330

214.32 1016.8 0 896.1

0.18554 1.1587 0 1.0526

cen84959_ap02.qxd 4/27/05 3:02 PM Page 944

944

|

Thermodynamics

TABLE A6ESuperheated waterT F v ft3/lbm P 333.49 200 392.53 240 416.44 280 440.33 320 464.20 360 488.07 400 511.92 440 535.77 500 571.54 600 631.14 700 690.73 800 750.31 1000 869.47 1200 988.62 1400 1107.8 P Sat. 240 280 320 360 400 440 500 600 700 800 1000 1200 1400 1600 26.297 27.429 29.085 30.722 32.348 33.965 35.576 37.986 41.988 45.981 49.967 57.930 65.885 73.836 81.784 P Sat. 320 360 400 440 500 600 700 800 1000 1200 1400 1600 1800 2000 7.1766 7.4863 7.9259 8.3548 8.7766 9.4005 10.4256 11.4401 12.4484 14.4543 16.4525 18.4464 20.438 22.428 24.417 Sat. u Btu/lbm h Btu/lbm s Btu/ lbm R v ft3/lbm P 73.525 78.153 83.009 87.838 92.650 97.452 102.25 107.03 114.21 126.15 138.09 150.02 173.86 197.70 221.54 P 1.7549 1.7742 1.8010 1.8260 1.8496 1.8721 1.8936 1.9243 1.9718 2.0156 2.0565 2.1312 2.1986 2.2604 2.3178 20.093 20.478 21.739 22.980 24.209 25.429 26.644 28.458 31.467 34.467 37.461 43.438 49.407 55.373 61.335 P 1.6442 1.6636 1.6897 1.7138 1.7364 1.7682 1.8168 1.8613 1.9026 1.9777 2.0454 2.1073 2.1648 2.2187 2.2694 5.4733 5.5440 5.8876 6.2187 6.5420 7.0177 7.7951 8.5616 9.3218 10.8313 12.3331 13.8306 15.3257 16.8192 18.3117 u Btu/lbm h Btu/lbm s Btu/ lbm R v ft3/lbm P 38.425 38.849 41.326 43.774 46.205 48.624 51.035 53.441 57.041 63.029 69.007 74.980 86.913 98.840 110.762 P 10.501 10.713 11.363 11.999 12.625 13.244 14.165 15.686 17.197 18.702 21.700 24.691 27.678 30.662 P u Btu/lbm s h Btu/ Btu/lbm lbm R

1.0 psia (101.69F)* 1043.7 1077.5 1091.2 1105.0 1118.9 1132.9 1147.1 1161.3 1182.8 1219.4 1256.8 1295.1 1374.2 1457.1 1543.7 1105.4 1150.1 1168.3 1186.5 1204.8 1223.3 1241.8 1260.4 1288.6 1336.2 1384.6 1433.9 1535.1 1640.0 1748.7 1.9776 2.0509 2.0777 2.1030 2.1271 2.1502 2.1722 2.1934 2.2237 2.2709 2.3146 2.3553 2.4299 2.4972 2.5590

5.0 psia (162.18F) 1062.7 1076.2 1090.3 1104.3 1118.4 1132.5 1146.7 1160.9 1182.6 1219.2 1256.7 1294.9 1374.2 1457.0 1543.7 1130.7 1148.5 1167.1 1185.6 1204.1 1222.6 1241.3 1260.0 1288.2 1335.9 1384.4 1433.7 1535.0 1640.0 1748.7 1.8438 1.8716 1.8989 1.9246 1.9490 1.9722 1.9944 2.0156 2.0461 2.0933 2.1371 2.1778 2.2524 2.3198 2.3816

10 psia (193.16F) 1072.0 1074.5 1089.1 1103.4 1117.6 1131.9 1146.2 1160.5 1182.2 1219.0 1256.5 1294.8 1374.1 1457.0 1543.6 1143.1 1146.4 1165.5 1184.4 1203.1 1221.8 1240.6 1259.4 1287.8 1335.6 1384.2 1433.5 1534.9 1639.9 1748.6 1.7875 1.7926 1.8207 1.8469 1.8716 1.8950 1.9174 1.9388 1.9693 2.0167 2.0605 2.1013 2.1760 2.2433 2.3052

15 psia (212.99F) 1077.7 1087.8 1102.4 1116.9 1131.3 1145.7 1160.1 1181.9 1218.7 1256.3 1294.6 1374.0 1456.9 1543.6 1634.0 1150.7 1163.9 1183.2 1202.2 1221.1 1239.9 1258.8 1287.3 1335.3 1383.9 1433.3 1534.8 1639.8 1748.5 1861.0

20 psia (227.92F) 1081.8 1086.5 1101.4 1116.1 1130.7 1145.1 1159.7 1181.6 1218.5 1256.1 1294.5 1373.8 1456.8 1543.5 1633.9 1156.2 1162.3 1181.9 1201.2 1220.2 1239.3 1258.3 1286.9 1334.9 1383.7 1433.1 1534.6 1639.7 1748.4 1860.9 1.7319 1.7406 1.7679 1.7933 1.8171 1.8398 1.8614 1.8922 1.9398 1.9837 2.0247 2.0994 2.1668 2.2287 2.2861

40 psia (267.22F) 1092.1 1097.3 1112.9 1128.1 1143.1 1157.9 1180.2 1217.5 1255.3 1293.9 1373.4 1456.5 1543.3 1633.7 1169.8 1176.6 1197.1 1216.9 1236.5 1256.0 1285.0 1333.6 1382.6 1432.3 1534.1 1639.3 1748.1 1860.7 1.6766 1.6858 1.7128 1.7376 1.7610 1.7831 1.8143 1.8625 1.9067 1.9478 2.0227 2.0902 2.1522 2.2096

60 psia (292.69F) 1098.1 1109.6 1125.5 1140.9 1156.1 1178.8 1216.5 1254.5 1293.3 1373.0 1456.2 1543.0 1633.5 1727.6 1825.2 1177.8 1192.7 1213.5 1233.7 1253.6 1283.1 1332.2 1381.6 1431.5 1533.5 1638.9 1747.8 1860.5 1976.6 2096.3

80 psia (312.02F) 1102.3 1105.9 1122.7 1138.7 1154.3 1177.3 1215.4 1253.8 1292.6 1372.6 1455.9 1542.8 1633.3 1727.5 1825.0 1183.4 1187.9 1209.9 1230.8 1251.2 1281.2 1330.8 1380.5 1430.6 1532.9 1638.5 1747.5 1860.2 1976.5 2096.1 1.6212 1.6271 1.6545 1.6794 1.7026 1.7350 1.7841 1.8289 1.8704 1.9457 2.0135 2.0755 2.1330 2.1869 2.2376

100 psia (327.81F) 1187.5 1206.1 1227.8 1248.7 1279.3 1329.4 1379.5 1429.8 1532.4 1638.1 1747.2 1860.0 1976.3 2096.0 1.6032 1.6263 1.6521 1.6759 1.7088 1.7586 1.8037 1.8453 1.9208 1.9887 2.0508 2.1083 2.1622 2.2130

4.4327 1105.5 4.6628 4.9359 5.2006 5.5876 6.2167 6.8344 7.4457 8.6575 9.8615 11.0612 12.2584 13.4541 14.6487 1119.8 1136.4 1152.4 1175.9 1214.4 1253.0 1292.0 1372.2 1455.6 1542.6 1633.2 1727.3 1824.9

*The temperature in parentheses is the saturation temperature at the specified pressure.

Properties of saturated vapor at the specified pressure.

cen84959_ap02.qxd 4/27/05 3:02 PM Page 945

Appendix 2 TABLE A6ESuperheated water (Continued )T F v ft3/lbm P Sat. 360 400 450 500 550 600 700 800 1000 1200 1400 1600 1800 2000 3.7289 3.8446 4.0799 4.3613 4.6340 4.9010 5.1642 5.6829 6.1950 7.2083 8.2137 9.2149 10.2135 11.2106 12.2067 P Sat. 400 450 500 550 600 700 800 900 1000 1200 1400 1600 1800 2000 2.5322 2.6490 2.8514 3.0433 3.2286 3.4097 3.7635 4.1104 4.4531 4.7929 5.4674 6.1377 6.8054 7.4716 8.1367 P Sat. 450 500 550 600 650 700 800 900 1000 1200 1400 1600 1800 2000 1.8440 2.0027 2.1506 2.2910 2.4264 2.5586 2.6883 2.9429 3.1930 3.4403 3.9295 4.4144 4.8969 5.3777 5.8575 u Btu/lbm h Btu/lbm s Btu/ lbm R v ft3/lbm P 3.2202 3.2584 3.4676 3.7147 3.9525 4.1845 4.4124 4.8604 5.3017 6.1732 7.0367 7.8961 8.7529 9.6082 10.4624 P 2.2882 2.3615 2.5488 2.7247 2.8939 3.0586 3.3796 3.6934 4.0031 4.3099 4.9182 5.5222 6.1238 6.7238 7.3227 P 1.6806 1.8034 1.9415 2.0715 2.1964 2.3179 2.4369 2.6699 2.8984 3.1241 3.5700 4.0116 4.4507 4.8882 5.3247 s u h Btu/ Btu/lbm Btu/lbm lbm R 140 psia (353.03F) 1109.9 1113.4 1131.5 1152.6 1172.9 1192.7 1212.3 1251.4 1290.8 1371.3 1455.0 1542.1 1632.8 1727.0 1824.6 1193.4 1197.8 1221.4 1248.9 1275.3 1301.1 1326.6 1377.3 1428.1 1531.3 1637.3 1746.6 1859.5 1975.9 2095.7 1.5757 1.5811 1.6092 1.6403 1.6686 1.6948 1.7195 1.7652 1.8072 1.8832 1.9512 2.0134 2.0711 2.1250 2.1758 v ft3/lbm P 2.8347 3.0076 3.2293 3.4412 3.6469 3.8484 4.2434 4.6316 5.3968 6.1540 6.9070 7.6574 8.4063 9.1542 P 2.0423 2.0728 2.2457 2.4059 2.5590 2.7075 2.9956 3.2765 3.5530 3.8268 4.3689 4.9068 5.4422 5.9760 6.5087 P 1.5435 1.6369 1.7670 1.8885 2.0046 2.1172 2.2273 2.4424 2.6529 2.8605 3.2704 3.6759 4.0789 4.4803 4.8807 u Btu/lbm

|

945

s h Btu/ Btu/lbm lbm R

120 psia (341.25F) 1107.9 1116.7 1134.0 1154.5 1174.4 1193.9 1213.4 1252.2 1291.4 1371.7 1455.3 1542.3 1633.0 1727.2 1824.8 1190.8 1202.1 1224.6 1251.4 1277.3 1302.8 1328.0 1378.4 1429.0 1531.8 1637.7 1746.9 1859.8 1976.1 2095.8 1.5883 1.6023 1.6292 1.6594 1.6872 1.7131 1.7375 1.7829 1.8247 1.9005 1.9684 2.0305 2.0881 2.1420 2.1928

160 psia (363.54F) 1111.6 1129.0 1150.7 1171.4 1191.4 1211.3 1250.6 1290.2 1370.9 1454.7 1541.8 1632.6 1726.9 1824.5 1195.5 1218.0 1246.3 1273.2 1299.4 1325.2 1376.3 1427.3 1530.7 1636.9 1746.3 1859.3 1975.7 2095.5 1.5647 1.5914 1.6234 1.6522 1.6788 1.7037 1.7498 1.7920 1.8682 1.9363 1.9986 2.0563 2.1102 2.1610

180 psia (373.07F) 1113.0 1126.3 1148.7 1169.8 1190.2 1210.2 1249.8 1289.5 1329.7 1370.5 1454.3 1541.6 1632.4 1726.7 1824.4 1197.3 1214.5 1243.7 1271.2 1297.7 1323.8 1375.2 1426.5 1478.0 1530.1 1636.5 1746.0 1859.1 1975.6 2095.4 1.5548 1.5752 1.6082 1.6376 1.6646 1.6897 1.7361 1.7785 1.8179 1.8549 1.9231 1.9855 2.0432 2.0971 2.1479

200 psia (381.80F) 1114.1 1123.5 1146.7 1168.2 1188.9 1209.1 1249.0 1288.9 1329.2 1370.1 1454.0 1541.4 1632.2 1726.5 1824.3 1198.8 1210.9 1241.0 1269.0 1296.0 1322.3 1374.1 1425.6 1477.3 1529.6 1636.1 1745.7 1858.8 1975.4 2095.3 1.5460 1.5602 1.5943 1.6243 1.6516 1.6771 1.7238 1.7664 1.8059 1.8430 1.9113 1.9737 2.0315 2.0855 2.1363

225 psia (391.80F) 1115.3 1119.7 1144.1 1166.2 1187.2 1207.7 1248.0 1288.1 1328.5 1369.5 1453.6 1541.1 1632.0 1726.4 1824.1 1200.3 1206.0 1237.6 1266.3 1293.8 1320.5 1372.7 1424.5 1476.5 1528.9 1635.6 1745.4 1858.6 1975.2 2095.1 1.5360 1.5427 1.5783 1.6091 1.6370 1.6628 1.7099 1.7528 1.7925 1.8296 1.8981 1.9606 2.0184 2.0724 2.1232

250 psia (400.97F) 1116.3 1141.3 1164.1 1185.6 1206.3 1226.8 1247.0 1287.3 1327.9 1369.0 1453.3 1540.8 1631.7 1726.2 1823.9 1201.6 1234.0 1263.6 1291.5 1318.6 1345.1 1371.4 1423.5 1475.6 1528.2 1635.0 1745.0 1858.3 1974.9 2094.9 1.5270 1.5636 1.5953 1.6237 1.6499 1.6743 1.6974 1.7406 1.7804 1.8177 1.8863 1.9488 2.0066 2.0607 2.1116

275 psia (409.45F) 1117.0 1138.5 1162.0 1183.9 1204.9 1225.6 1246.0 1286.5 1327.3 1368.5 1452.9 1540.5 1631.5 1726.0 1823.8 1202.6 1230.3 1260.8 1289.3 1316.7 1343.5 1370.0 1422.4 1474.8 1527.4 1634.5 1744.6 1858.0 1974.7 2094.7 1.5187 1.5499 1.5825 1.6115 1.6380 1.6627 1.6860 1.7294 1.7694 1.8068 1.8755 1.9381 1.9960 2.0501 2.1010

300 psia (417.35F) 1117.7 1135.6 1159.8 1182.1 1203.5 1224.4 1244.9 1285.7 1326.6 1367.9 1452.5 1540.2 1631.3 1725.8 1823.6 1203.3 1226.4 1257.9 1287.0 1314.8 1341.9 1368.6 1421.3 1473.9 1526.7 1634.0 1744.2 1857.7 1974.5 2094.6 1.5111 1.5369 1.5706 1.6001 1.6270 1.6520 1.6755 1.7192 1.7593 1.7968 1.8657 1.9284 1.9863 2.0404 2.0913

cen84959_ap02.qxd 4/27/05 3:02 PM Page 946

946

|

Thermodynamics

TABLE A6ESuperheated water (Continued )T F v ft3/lbm P Sat. 450 500 550 600 650 700 800 900 1000 1200 1400 1600 1800 2000 1.3263 1.3739 1.4921 1.6004 1.7030 1.8018 1.8979 2.0848 2.2671 2.4464 2.7996 3.1484 3.4947 3.8394 4.1830 P Sat. 500 550 600 650 700 800 900 1000 1100 1200 1400 1600 1800 2000 0.92815 0.99304 1.07974 1.15876 1.23312 1.30440 1.44097 1.57252 1.70094 1.82726 1.95211 2.1988 2.4430 2.6856 2.9271 P Sat. 550 600 650 700 750 800 900 1000 1100 1200 1400 1600 1800 2000 0.56920 0.61586 0.67799 0.73279 0.78330 0.83102 0.87678 0.96434 1.04841 1.13024 1.21051 1.36797 1.52283 1.67606 1.82823 s u h Btu/ Btu/lbm Btu/lbm lbm R 350 psia (431.74F) 1118.5 1129.3 1155.2 1178.6 1200.6 1221.9 1242.8 1284.1 1325.3 1366.9 1451.7 1539.6 1630.8 1725.4 1823.3 1204.4 1218.3 1251.9 1282.2 1310.9 1338.6 1365.8 1419.1 1472.2 1525.3 1633.0 1743.5 1857.1 1974.0 2094.2 1.4973 1.5128 1.5487 1.5795 1.6073 1.6328 1.6567 1.7009 1.7414 1.7791 1.8483 1.9111 1.9691 2.0233 2.0742 v ft3/lbm P 1.1617 1.1747 1.2851 1.3840 1.4765 1.5650 1.6507 1.8166 1.9777 2.1358 2.4465 2.7527 3.0565 3.3586 3.6597 P 0.77020 0.79526 0.87542 0.94605 1.01133 1.07316 1.19038 1.30230 1.41097 1.51749 1.62252 1.82957 2.0340 2.2369 2.4387 P 0.44604 0.45375 0.51431 0.56411 0.60844 0.64944 0.68821 0.76136 0.83078 0.89783 0.96327 1.09101 1.21610 1.33956 1.46194 u h Btu/lbm Btu/lbm s Btu/ lbm R v ft3/lbm P 1.0324 1.1233 1.2152 1.3001 1.3807 1.4584 1.6080 1.7526 1.8942 2.1718 2.4450 2.7157 2.9847 3.2527 P 0.65589 0.72799 0.79332 0.85242 0.90769 1.01125 1.10921 1.20381 1.29621 1.38709 1.56580 1.74192 1.91643 2.08987 P 0.34549 0.37894 0.42703 0.46735 0.50344 0.53687 0.59876 0.65656 0.71184 0.76545 0.86944 0.97072 1.07036 1.16892 s u h Btu/ Btu/lbm Btu/lbm lbm R 450 psia (456.31F) 1119.2 1145.4 1171.1 1194.6 1216.9 1238.5 1280.8 1322.7 1364.7 1450.1 1538.4 1629.8 1724.6 1822.6 1205.2 1238.9 1272.3 1302.8 1331.9 1360.0 1414.7 1468.6 1522.4 1631.0 1742.0 1856.0 1973.2 2093.5 1.4742 1.5103 1.5441 1.5737 1.6005 1.6253 1.6706 1.7117 1.7499 1.8196 1.8827 1.9409 1.9952 2.0462

400 psia (444.62F) 1119.0 1122.5 1150.4 1174.9 1197.6 1219.4 1240.7 1282.5 1324.0 1365.8 1450.9 1539.0 1630.3 1725.0 1823.0 1205.0 1209.4 1245.6 1277.3 1306.9 1335.3 1362.9 1417.0 1470.4 1523.9 1632.0 1742.7 1856.5 1973.6 2093.9 1.4852 1.4901 1.5288 1.5610 1.5897 1.6158 1.6401 1.6849 1.7257 1.7636 1.8331 1.8960 1.9541 2.0084 2.0594

500 psia (467.04F) 1119.1 1140.1 1167.1 1191.4 1214.3 1236.4 1279.2 1321.4 1363.6 1406.2 1449.4 1537.8 1629.4 1724.2 1822.3 1205.0 1231.9 1267.0 1298.6 1328.4 1357.0 1412.5 1466.9 1521.0 1575.3 1630.0 1741.2 1855.4 1972.7 2093.1 1.4642 1.4928 1.5284 1.5590 1.5865 1.6117 1.6576 1.6992 1.7376 1.7735 1.8075 1.8708 1.9291 1.9834 2.0345

600 psia (486.24F) 1118.3 1128.2 1158.7 1184.9 1209.0 1231.9 1275.8 1318.7 1361.4 1404.4 1447.8 1536.6 1628.4 1723.4 1821.7 1203.9 1216.5 1255.9 1289.9 1321.3 1351.0 1408.0 1463.3 1518.1 1572.9 1627.9 1739.7 1854.2 1971.8 2092.4 1.4463 1.4596 1.4996 1.5325 1.5614 1.5877 1.6348 1.6771 1.7160 1.7522 1.7865 1.8501 1.9085 1.9630 2.0141

700 psia (503.13F) 1116.9 1149.5 1177.9 1203.4 1227.2 1272.4 1316.0 1359.2 1402.5 1446.2 1535.4 1627.5 1722.7 1821.0 1201.9 1243.8 1280.7 1313.8 1344.8 1403.4 1459.7 1515.2 1570.4 1625.9 1738.2 1853.1 1970.9 2091.7 1.4305 1.4730 1.5087 1.5393 1.5666 1.6150 1.6581 1.6974 1.7341 1.7685 1.8324 1.8911 1.9457 1.9969

800 psia (518.27F) 1115.0 1139.4 1170.5 1197.6 1222.4 1246.0 1268.9 1313.3 1357.0 1400.7 1444.6 1534.2 1626.5 1721.9 1820.4 1199.3 1230.5 1270.9 1306.0 1338.4 1369.1 1398.7 1456.0 1512.2 1568.0 1623.8 1736.7 1851.9 1970.0 2091.0 1.4162 1.4476 1.4866 1.5191 1.5476 1.5735 1.5975 1.6413 1.6812 1.7181 1.7528 1.8170 1.8759 1.9306 1.9819

1000 psia (544.65F) 1110.1 1115.2 1154.1 1185.1 1212.4 1237.6 1261.7 1307.7 1352.5 1396.9 1441.4 1531.8 1624.6 1720.3 1819.1 1192.6 1199.2 1249.3 1289.5 1325.0 1357.8 1389.0 1448.6 1506.2 1563.1 1619.7 1733.7 1849.6 1968.2 2089.6 1.3906 1.3972 1.4457 1.4827 1.5140 1.5418 1.5670 1.6126 1.6535 1.6911 1.7263 1.7911 1.8504 1.9053 1.9568

1250 psia (572.45F) 1102.0 1129.5 1167.5 1198.7 1226.4 1252.2 1300.5 1346.7 1392.2 1437.4 1528.7 1622.2 1718.4 1817.5 1181.9 1217.2 1266.3 1306.8 1342.9 1376.4 1439.0 1498.6 1556.8 1614.5 1729.8 1846.7 1966.0 2087.9 1.3623 1.3961 1.4414 1.4771 1.5076 1.5347 1.5826 1.6249 1.6635 1.6993 1.7649 1.8246 1.8799 1.9315

cen84959_ap02.qxd 4/27/05 3:02 PM Page 947

Appendix 2 TABLE A6ESuperheated water (Concluded)T F v ft3/lbm P Sat. 600 650 700 750 800 850 900 1000 1100 1200 1400 1600 1800 2000 0.27695 0.28189 0.33310 0.37198 0.40535 0.43550 0.46356 0.49015 0.54031 0.58781 0.63355 0.72172 0.80714 0.89090 0.97358 P Sat. 650 700 750 800 850 900 950 1000 1100 1200 1400 1600 1800 2000 0.13076 0.16849 0.20327 0.22949 0.25174 0.27165 0.29001 0.30726 0.33949 0.36966 0.42631 0.48004 0.53205 0.58295 u Btu/lbm s h Btu/ Btu/lbm lbm R v ft3/lbm P 0.22681 0.26292 0.30252 0.33455 0.36266 0.38835 0.41238 0.45719 0.49917 0.53932 0.61621 0.69031 0.76273 0.83406 P 0.08460 0.09838 0.14840 0.17601 0.19771 0.21640 0.23321 0.24876 0.27732 0.30367 0.35249 0.39830 0.44237 0.48532 u h Btu/lbm Btu/lbm s Btu/ lbm R v ft3/lbm P 0.18815 0.20586 0.24894 0.28074 0.30763 0.33169 0.35390 0.39479 0.43266 0.46864 0.53708 0.60269 0.66660 0.72942

|

947

s u h Btu/ Btu/lbm Btu/lbm lbm R 2000 psia (635.85F) 1066.8 1091.4 1147.6 1187.4 1220.5 1250.0 1277.5 1328.7 1377.5 1425.1 1519.5 1615.0 1712.5 1812.6 P 1136.4 1167.6 1239.8 1291.3 1334.3 1372.8 1408.5 1474.9 1537.6 1598.5 1718.3 1838.0 1959.2 2082.6 1.2863 1.3146 1.3783 1.4218 1.4567 1.4867 1.5134 1.5606 1.6021 1.6400 1.7081 1.7693 1.8255 1.8778

1500 psia (596.26F) 1092.1 1097.2 1147.2 1183.6 1214.4 1242.2 1268.2 1293.1 1340.9 1387.3 1433.3 1525.7 1619.8 1716.4 1815.9 1169.0 1175.4 1239.7 1286.9 1326.9 1363.1 1396.9 1429.2 1490.8 1550.5 1609.2 1726.0 1843.8 1963.7 2086.1 1.3362 1.3423 1.4016 1.4433 1.4771 1.5064 1.5328 1.5569 1.6007 1.6402 1.6767 1.7432 1.8033 1.8589 1.9108

1750 psia (617.17F) 1080.5 1122.8 1166.8 1201.5 1231.7 1259.3 1285.4 1334.9 1382.4 1429.2 1522.6 1617.4 1714.5 1814.2 1153.9 1207.9 1264.7 1309.8 1349.1 1385.1 1419.0 1482.9 1544.1 1603.9 1722.1 1840.9 1961.5 2084.3 1.3112 1.3607 1.4108 1.4489 1.4807 1.5088 1.5341 1.5796 1.6201 1.6572 1.7245 1.7852 1.8410 1.8931

2500 psia (668.17F) 1031.2 1098.4 1154.9 1195.9 1230.1 1260.7 1289.1 1316.1 1367.3 1416.6 1513.3 1610.1 1708.6 1809.4 P 1091.7 1176.3 1249.0 1302.0 1346.6 1386.4 1423.3 1458.2 1524.4 1587.6 1710.5 1832.2 1954.8 2079.1 1.2330 1.3072 1.3686 1.4116 1.4463 1.4761 1.5028 1.5271 1.5710 1.6103 1.6802 1.7424 1.7991 1.8518

3000 psia (695.41F) 969.8 1005.3 1114.1 1167.5 1208.2 1242.8 1273.9 1302.8 1356.8 1408.0 1507.0 1605.3 1704.7 1806.1 P 1016.8 1059.9 1196.5 1265.3 1317.9 1362.9 1403.3 1440.9 1510.8 1576.6 1702.7 1826.4 1950.3 2075.6 1.1587 1.1960 1.3118 1.3676 1.4086 1.4423 1.4716 1.4978 1.5441 1.5850 1.6567 1.7199 1.7773 1.8304 0.02492 0.03065 0.10460 0.13639 0.15847 0.17659 0.19245 0.20687 0.23289 0.25654 0.29978 0.33994 0.37833 0.41561

3500 psia 679.9 779.9 1125.4 1222.6 1286.5 1337.8 1382.4 1423.0 1496.9 1565.4 1694.8 1820.5 1945.8 2072.1 0.8632 0.9511 1.2434 1.3224 1.3721 1.4106 1.4428 1.4711 1.5201 1.5627 1.6364 1.7006 1.7586 1.8121

663.7 760.0 1057.6 1134.3 1183.8 1223.4 1257.8 1289.0 1346.1 1399.3 1500.7 1600.4 1700.8 1802.9 P

4000 psia 676.1 763.6 1009.2 1172.1 1251.8 1310.9 1360.5 1404.4 1482.8 1554.1 1621.6 1687.0 1814.7 1941.4 2068.6 0.8577 0.9347 1.1410 1.2734 1.3355 1.3799 1.4157 1.4463 1.4983 1.5426 1.5821 1.6182 1.6835 1.7422 1.7961 0.02379 0.02678 0.03373 0.05937 0.08551 0.10390 0.11863 0.13128 0.15298 0.17185 0.18902 0.20508 0.23505 0.26320 0.29023

5000 psia 670.3 746.6 853.0 1041.8 1171.5 1252.1 1313.6 1365.5 1453.8 1531.1 1602.7 1671.1 1803.1 1932.5 2061.7 0.8485 0.9156 1.0054 1.1581 1.2593 1.3198 1.3643 1.4004 1.4590 1.5070 1.5490 1.5868 1.6542 1.7142 1.7689 0.02325 0.02564 0.02981 0.03949 0.05815 0.07584 0.09010 0.10208 0.12211 0.13911 0.15434 0.16841 0.19438 0.21853 0.24155

6000 psia 666.1 736.5 821.8 941.0 1083.1 1187.7 1263.7 1324.7 1424.0 1507.8 1583.8 1655.4 1791.5 1923.7 2054.9 0.8408 0.9028 0.9747 1.0711 1.1819 1.2603 1.3153 1.3578 1.4237 1.4758 1.5203 1.5598 1.6294 1.6907 1.7463

650 700 750 800 850 900 950 1000 1100 1200 1300 1400 1600 1800 2000

0.02448 0.02871 0.06370 0.10520 0.12848 0.14647 0.16176 0.17538 0.19957 0.22121 0.24128 0.26028 0.29620 0.33033 0.36335

657.9 742.3 962.1 1094.2 1156.7 1202.5 1240.7 1274.6 1335.1 1390.3 1443.0 1494.3 1595.5 1696.8 1799.7

648.3 721.8 821.8 986.9 1092.4 1155.9 1203.9 1244.0 1312.2 1372.1 1427.8 1481.4 1585.6 1689.0 1793.2

640.3 708.1 788.7 897.1 1018.6 1103.5 1163.7 1211.4 1288.4 1353.4 1412.5 1468.4 1575.7 1681.1 1786.7

cen84959_ap02.qxd 4/27/05 3:02 PM Page 948

948

|

Thermodynamics

TABLE A7ECompressed liquid waterT F v ft3/lbm P Sat. 32 50 100 150 200 250 300 350 400 450 500 550 0.019750 0.015994 0.015998 0.016107 0.016317 0.016607 0.016972 0.017417 0.017954 0.018609 0.019425 u h Btu/lbm Btu/lbm s v Btu/lbm R ft3/lbm P 0.021595 0.015966 0.015972 0.016083 0.016292 0.016580 0.016941 0.017380 0.017910 0.018552 0.019347 0.020368 P 0.034335 0.015859 0.015870 0.015988 0.016475 0.017242 0.018338 0.019062 0.019960 0.021405 0.022759 0.024765 0.028821 u h s v Btu/lbm Btu/lbm Btu/lbm R ft3/lbm 1000 psia (544.65F) 538.58 0.03 17.99 67.69 117.42 167.31 217.51 268.24 319.77 372.48 426.93 484.03 542.57 2.99 20.95 70.67 120.43 170.38 220.65 271.46 323.08 375.91 430.51 487.80 0.74341 0.00005 0.03593 0.12899 0.21416 0.29289 0.36634 0.43551 0.50132 0.56463 0.62635 0.68764 P 0.023456 0.015939 0.015946 0.016059 0.016267 0.016553 0.016911 0.017345 0.017866 0.018496 0.019271 0.020258 0.021595 u h s Btu/lbm Btu/lbm Btu/lbm R 1500 psia (596.26F) 605.07 0.05 17.95 67.53 117.14 166.92 217.00 267.57 318.91 371.37 425.47 482.01 542.50 P 0.015756 0.015773 0.015897 0.016375 0.017112 0.018145 0.018812 0.019620 0.020862 0.021943 0.023358 0.025366 0.026777 611.58 4.48 22.38 71.98 121.66 171.52 221.69 272.39 323.87 376.51 430.82 487.63 548.50 0.80836 0.00008 0.03584 0.12869 0.21369 0.29229 0.36560 0.43463 0.50025 0.56333 0.62472 0.68550 0.74731

500 psia (467.04F) 447.68 0.01 18.03 67.86 117.70 167.70 218.04 268.92 320.64 373.61 428.44 449.51 1.49 19.51 69.35 119.21 169.24 219.61 270.53 322.30 375.33 430.24 0.64900 0.00001 0.03601 0.12930 0.21462 0.29349 0.36708 0.43641 0.50240 0.56595 0.62802

P Sat. 32 50 100 200 300 400 450 500 560 600 640 680 700 0.025634 0.015912 0.015921 0.016035 0.016527 0.017310 0.018442 0.019199 0.020154 0.021739 0.023317

2000 psia (635.85F) 662.33 0.07 17.91 67.36 166.54 266.92 370.30 424.06 480.08 552.21 605.77 671.82 5.96 23.80 73.30 172.66 273.33 377.12 431.16 487.54 560.26 614.40 0.86224 0.00010 0.03574 0.12838 0.29170 0.43376 0.56205 0.62314 0.68346 0.75692 0.80898

3000 psia (695.41F) 783.39 0.10 17.83 67.04 165.79 265.65 368.22 421.36 476.45 546.59 597.42 654.52 728.63 802.45 8.90 26.64 75.91 174.94 275.22 378.41 431.94 487.53 558.47 610.06 668.27 744.64 0.97321 0.00011 0.03554 0.12776 0.29053 0.43204 0.55959 0.62010 0.67958 0.75126 0.80086 0.85476 0.92288

5000 psia 14.71 32.25 81.12 179.51 279.07 381.14 433.80 488.10 556.38 604.72 656.56 714.14 746.56 0.00002 0.03505 0.12652 0.28824 0.42874 0.55492 0.61445 0.67254 0.74154 0.78803 0.83603 0.88745 0.91564

0.13 17.65 66.41 164.36 263.24 364.35 416.40 469.94 537.08 584.42 634.95 690.67 721.78

cen84959_ap02.qxd 4/27/05 3:02 PM Page 949

Appendix 2 TABLE A8ESaturated icewater vaporSpecific volume, ft3/lbm Sat. ice, vi Sat. vapor, vg Sat. ice, ui143.34 143.35 144.35 146.85 149.32 151.76 154.18 156.57 158.94 161.28 163.60 165.90 168.16 170.41 172.63 174.83 177.00

|

949

Temp., T F32.018 32 30 25 20 15 10 5 0 5 10 15 20 25 30 35 40

Sat. press., Psat psia0.08871 0.08864 0.08086 0.06405 0.05049 0.03960 0.03089 0.02397 0.01850 0.01420 0.01083 0.00821 0.00619 0.00463 0.00344 0.00254 0.00186

Internal energy, Btu/lbm Subl., uig1164.2 1164.2 1164.6 1165.4 1166.2 1167.0 1167.8 1168.5 1169.2 1169.9 1170.6 1171.2 1171.8 1172.4 1173.0 1173.5 1174.0

Enthalpy, Btu/lbm Sat. ice, hi143.34 143.35 144.35 146.85 149.32 151.76 154.18 156.57 158.94 161.28 163.60 165.90 168.16 170.41 172.63 174.83 177.00

Entropy, Btu/Ibm R Sat. vapor, hg1075.0 1075.0 1074.2 1072.0 1069.8 1067.6 1065.4 1063.1 1060.9 1058.7 1056.5 1054.3 1052.1 1049.9 1047.7 1045.5 1043.3

Sat. vapor, ug1020.9 1020.9 1020.2 1018.6 1016.9 1015.2 1013.6 1011.9 1010.3 1008.6 1007.0 1005.3 1003.6 1002.0 1000.3 998.7 997.0

Subl., hig1218.3 1218.4 1218.5 1218.8 1219.1 1219.3 1219.5 1219.7 1219.9 1220.0 1220.1 1220.2 1220.3 1220.3 1220.3 1220.3 1220.3

Sat. ice, si0.29146 0.29148 0.29353 0.29865 0.30377 0.30889 0.31401 0.31913 0.32426 0.32938 0.33451 0.33964 0.34478 0.34991 0.35505 0.36019 0.36534

Subl., sig2.4779 2.4779 2.4883 2.5146 2.5414 2.5687 2.5965 2.6248 2.6537 2.6832 2.7133 2.7440 2.7754 2.8074 2.8401 2.8735 2.9076

Sat. vapor, sg2.1864 2.1865 2.1948 2.2160 2.2376 2.2598 2.2825 2.3057 2.3295 2.3538 2.3788 2.4044 2.4306 2.4575 2.4850 2.5133 2.5423

0.01747 3299.6 0.01747 3302.6 0.01747 3605.8 0.01746 4505.8 0.01746 5657.6 0.01745 7138.9 0.01744 9054.0 0.01743 11,543 0.01743 14,797 0.01742 19,075 0.01741 24,731 0.01740 32,257 0.01740 42,335 0.01739 55,917 0.01738 74,345 0.01738 99,526 0.01737 134,182

cen84959_ap02.qxd 4/27/05 3:02 PM Page 950

950

|

Thermodynamics1800

Constant n Pressure lbf/in 2

13

1780

00

1500

17601740

12

50

15001500 0

1211

00

1400

1720

10000 8000 5000 6000 3 204 4000 2 5 00 3000

1700

50

1400

16801 000

1110

130000

1660400 300 200

1640

50

100

0.1 1

130

600

0

162060 0

10

120000

30

0.05053

0.2

120 0

1600

14.696

95

0

10

15800.41560

110090

0

62

0.6

110 0

1540

8580750

0

4

1520

10000

15001480

100 0150 00 100 80 00 00

1

900706500

1460

900 800 700

32

400

04

0

5

14201400

6055

0

bm

00

20

0.0 0.03 5 60 53

me ft 3/l

1360

20

25

00

3

00

1380

0

700

505010045

00

0

10

1320

Con stan t Qu ality , Pe rcen t

1000

0 .4

400

1 280

2000

500

600

0.2

1300

0 Constant Enthalpy Btu/lbm 35 030

C o n sta

500

40

200

1 0.

n t V olu

600

1340

15

00

0

600

500

300

0.6

1 2601 240

0

400

200

1

2520

0

400

100

12201 20

2

0

1220

60

0

1530

0

12003001180

1 4 .6

C o ns

ta nt V

ol

3 /l b m u m e ft

96

5

1020

1050

01160

10

504 4 4 450

0 .5

2007 70

1

100

85

0

90

0

2

95

0

10

10 5 00 085

11

00

4

1140

200

6

95

1120

35

45

30

40

25

15

20

10

10002000

0 .1

500

0 .2

1100

100 60 32 2.4

0.0

5

0.5

1.0 Entropy, Btu/lbmR

1.5

2.0

FIGURE A9E T-s diagram for water.Source: Joseph H. Keenan, Frederick G. Keyes, Philip G. Hill, and Joan G. Moore, Steam Tables (New York: John Wiley & Sons, 1969).

Temperature, F

00 60 00 50

2

1440

800

10

0

F h t rhea S Supe t stant Cons

0 800 b lbm B / y Btu th p nthal stant E Consta 70 700

0 1 115 0 1 110

0 0 100

900

600

5 500

4 40070

0 400

7 75

0 65

5 500

3 3 3 350

5 5 50 55

00 60

0

0

300

50 50 50 250

200

90

8 80

75

150

5 65

100

6 60

5 55

5 50

50 50 50 50

cen84959_ap02.qxd 4/27/05 3:02 PM Page 951

Appendix 2Entropy, Btu/lbm R 1.510,00 0 psi a 5000

|

951

1.6

1.7

1.8

1.9 F 1100F

2.0

2.1

2.2

1600

15503204 200 0

1000

100 0

500

1500900

300 200

1450 Enthalpy, Btu / lbm800

100

psia

F 700F

50

1400

600

20

135010

13008 5 6 2p 3 4 sia

500

1250

400

300 satu line ration x= 0.9 8 0.9 6 0.9 4 0.9 2 0.9 0 0.8 8 0. 8684 0.2 2 2 0...8 0 . 0 . 0 0.8

12001.0

0. 5

200F 200 200F

11500. 2

100

2.2

1100 2.1 1050 2.0 1000 1.9 950

FIGURE A10E Mollier diagram for water.Source: Joseph H. Keenan, Frederick G. Keyes, Philip G. Hill, and Joan G. Moore, Steam Tables (New York: John Wiley & Sons, 1969).

1.3

1.4

1.5

1.6

1.7 1.8 Entropy, Btu/lbm R

cen84959_ap02.qxd 4/27/05 3:02 PM Page 952

952

|

Thermodynamics

TABLE A11ESaturated refrigerant-134aTemperature tableSpecific volume, ft3/lbm Sat. Temp., press., T F Psat psia 40 35 30 25 20 15 10 5 0 5 10 15 20 25 30 35 40 45 50 55 60 65 70 75 80 85 90 95 100 105 110 115 120 130 140 150 160 170 180 190 200 210 7.432 8.581 9.869 11.306 12.906 14.680 16.642 18.806 21.185 23.793 26.646 29.759 33.147 36.826 40.813 45.124 49.776 54.787 60.175 65.957 72.152 78.780 85.858 93.408 101.45 110.00 119.08 128.72 138.93 149.73 161.16 173.23 185.96 213.53 244.06 277.79 314.94 355.80 400.66 449.90 504.00 563.76 Sat. liquid, vf 0.01130 0.01136 0.01143 0.01150 0.01156 0.01163 0.01171 0.01178 0.01185 0.01193 0.01201 0.01209 0.01217 0.01225 0.01234 0.01242 0.01251 0.01261 0.01270 0.01280 0.01290 0.01301 0.01312 0.01323 0.01334 0.01347 0.01359 0.01372 0.01386 0.01400 0.01415 0.01430 0.01446 0.01482 0.01521 0.01567 0.01619 0.01681 0.01759 0.01860 0.02009 0.02309 Sat. vapor, vg 5.7796 5.0509 4.4300 3.8988 3.4426 3.0494 2.7091 2.4137 2.1564 1.9316 1.7345 1.5612 1.4084 1.2732 1.1534 1.0470 0.95205 0.86727 0.79136 0.72323 0.66195 0.60671 0.55681 0.51165 0.47069 0.43348 0.39959 0.36869 0.34045 0.31460 0.29090 0.26913 0.24909 0.21356 0.18315 0.15692 0.13410 0.11405 0.09618 0.07990 0.06441 0.04722 Internal energy, Btu/lbm Sat. liquid, uf 0.016 1.484 2.990 4.502 6.019 7.543 9.073 10.609 12.152 13.702 15.259 16.823 18.394 19.973 21.560 23.154 24.757 26.369 27.990 29.619 31.258 32.908 34.567 36.237 37.919 39.612 41.317 43.036 44.768 46.514 48.276 50.054 51.849 55.495 59.226 63.059 67.014 71.126 75.448 80.082 85.267 91.986 Evap., ufg 89.167 88.352 87.532 86.706 85.874 85.036 84.191 83.339 82.479 81.610 80.733 79.846 78.950 78.043 77.124 76.195 75.253 74.298 73.329 72.346 71.347 70.333 69.301 68.251 67.181 66.091 64.979 63.844 62.683 61.496 60.279 59.031 57.749 55.071 52.216 49.144 45.799 42.097 37.899 32.950 26.651 16.498 Sat. vapor, ug 89.15 89.84 90.52 91.21 91.89 92.58 93.26 93.95 94.63 95.31 95.99 96.67 97.34 98.02 98.68 99.35 100.01 100.67 101.32 101.97 102.61 103.24 103.87 104.49 105.10 105.70 106.30 106.88 107.45 108.01 108.56 109.08 109.60 110.57 111.44 112.20 112.81 113.22 113.35 113.03 111.92 108.48 Enthalpy, Btu/lbm Sat. liquid, hf 0.000 1.502 3.011 4.526 6.047 7.574 9.109 10.650 12.199 13.755 15.318 16.889 18.469 20.056 21.653 23.258 24.873 26.497 28.131 29.775 31.431 33.097 34.776 36.466 38.169 39.886 41.617 43.363 45.124 46.902 48.698 50.512 52.346 56.080 59.913 63.864 67.958 72.233 76.752 81.631 87.140 94.395 Evap., hfg Sat. vapor, hg Sat. liquid, sf 0.00000 0.00355 0.00708 0.01058 0.01405 0.01749 0.02092 0.02431 0.02769 0.03104 0.03438 0.03769 0.04098 0.04426 0.04752 0.05076 0.05398 0.05720 0.06039 0.06358 0.06675 0.06991 0.07306 0.07620 0.07934 0.08246 0.08559 0.08870 0.09182 0.09493 0.09804 0.10116 0.10428 0.11054 0.11684 0.12321 0.12970 0.13634 0.14323 0.15055 0.15867 0.16922 Entropy, Btu/lbm R Evap., sfg 0.23135 0.22687 0.22248 0.21817 0.21394 0.20978 0.20569 0.20166 0.19770 0.19380 0.18996 0.18617 0.18243 0.17874 0.17509 0.17148 0.16791 0.16437 0.16087 0.15740 0.15396 0.15053 0.14713 0.14375 0.14038 0.13703 0.13368 0.13033 0.12699 0.12365 0.12029 0.11693 0.11354 0.10670 0.09971 0.09251 0.08499 0.07701 0.06835 0.05857 0.04666 0.02839 Sat. vapor, sg 0.23135 0.23043 0.22956 0.22875 0.22798 0.22727 0.22660 0.22598 0.22539 0.22485 0.22434 0.22386 0.22341 0.22300 0.22260 0.22224 0.22189 0.22157 0.22127 0.22098 0.22070 0.22044 0.22019 0.21995 0.21972 0.21949 0.21926 0.21904 0.21881 0.21858 0.21834 0.21809 0.21782 0.21724 0.21655 0.21572 0.21469 0.21335 0.21158 0.20911 0.20533 0.19761

97.100 97.10 96.354 97.86 95.601 98.61 94.839 99.36 94.068 100.12 93.288 100.86 92.498 101.61 91.698 90.886 90.062 89.226 88.377 87.514 86.636 85.742 84.833 83.907 82.963 82.000 81.017 80.013 78.988 77.939 76.866 75.767 74.641 73.485 72.299 71.080 69.825 68.533 67.200 65.823 62.924 59.801 56.405 52.671 48.499 43.726 38.053 30.785 19.015 102.35 103.08 103.82 104.54 105.27 105.98 106.69 107.40 108.09 108.78 109.46 110.13 110.79 111.44 112.09 112.71 113.33 113.94 114.53 115.10 115.66 116.20 116.73 117.23 117.71 118.17 119.00 119.71 120.27 120.63 120.73 120.48 119.68 117.93 113.41

Source: Tables A11E through A13E are generated using the Engineering Equation Solver (EES) software developed by S. A. Klein and F. L. Alvarado. The routine used in calculations is the R134a, which is based on the fundamental equation of state developed by R. Tillner-Roth and H.D. Baehr, An International Standard Formulation for the Thermodynamic Properties of 1,1,1,2-Tetrafluoroethane (HFC-134a) for Temperatures from 170 K to 455 K and Pressures up to 70 MPa, J. Phys. Chem, Ref. Data, Vol. 23, No. 5, 1994. The enthalpy and entropy values of saturated liquid are set to zero at 40C (and 40F).

cen84959_ap02.qxd 4/27/05 3:02 PM Page 953

Appendix 2 TABLE A12ESaturated refrigerant-134aPressure tableSpecific volume, ft3/lbm Sat. temp., T F 53.09 29.52 14.15 2.43 7.17 15.37 22.57 29.01 34.86 40.23 45.20 49.84 54.20 58.30 62.19 65.89 69.41 72.78 76.02 79.12 85.00 90.49 95.64 100.51 105.12 109.50 113.69 117.69 121.53 125.22 132.21 138.73 144.85 150.62 156.09 168.64 179.86 190.02 199.29 Sat. liquid, vf 0.01113 0.01144 0.01165 0.01182 0.01196 0.01209 0.01221 0.01232 0.01242 0.01252 0.01261 0.01270 0.01279 0.01287 0.01295 0.01303 0.01310 0.01318 0.01325 0.01332 0.01347 0.01360 0.01374 0.01387 0.01400 0.01413 0.01426 0.01439 0.01452 0.01464 0.01490 0.01516 0.01543 0.01570 0.01598 0.01672 0.01757 0.01860 0.01995 Sat. vapor, vg 8.3785 4.3753 2.9880 2.2772 1.8429 1.5492 1.3369 1.1760 1.0497 0.94791 0.86400 0.79361 0.73370 0.68205 0.63706 0.59750 0.56244 0.53113 0.50301 0.47760 0.43347 0.39644 0.36491 0.33771 0.31401 0.29316 0.27466 0.25813 0.24327 0.22983 0.20645 0.18677 0.16996 0.15541 0.14266 0.11664 0.09642 0.07987 0.06551 Sat. liquid, uf 3.918 3.135 7.803 11.401 14.377 16.939 19.205 21.246 23.110 24.832 26.435 27.939 29.357 30.700 31.979 33.201 34.371 35.495 36.578 37.623 39.612 41.485 43.258 44.945 46.556 48.101 49.586 51.018 52.402 53.743 56.310 58.746 61.071 63.301 65.452 70.554 75.385 80.092 84.871 Internal energy, Btu/lbm Sat. vapor, ug 87.36 90.59 92.70 94.30 95.61 96.72 97.69 98.55 99.33 100.04 100.69 101.30 101.86 102.39 102.88 103.35 103.79 104.21 104.61 104.99 105.70 106.35 106.95 107.51 108.02 108.50 108.95 109.36 109.75 110.11 110.77 111.34 111.83 112.25 112.60 113.18 113.35 113.03 112.04 Sat. liquid, hf 3.907 3.156 7.835 11.445 14.432 17.006 19.284 21.337 23.214 24.948 26.564 28.080 29.510 30.867 32.159 33.394 34.577 35.715 36.811 37.869 39.886 41.787 43.589 45.304 46.945 48.519 50.035 51.497 52.912 54.285 56.917 59.419 61.813 64.115 66.339 71.638 76.686 81.641 86.718 Enthalpy, Btu/lbm Sat. vapor, hg 95.11 98.68 100.99 102.73 104.13 105.32 106.35 107.26 108.07 108.81 109.49 110.11 110.69 111.22 111.73 112.20 112.64 113.06 113.46 113.83 114.53 115.16 115.73 116.26 116.74 117.18 117.59 117.96 118.30 118.62 119.17 119.63 120.00 120.30 120.52 120.74 120.48 119.68 118.10 Sat. liquid, sf 0.00945 0.00742 0.01808 0.02605 0.03249 0.03793 0.04267 0.04688 0.05067 0.05413 0.05733 0.06029 0.06307 0.06567 0.06813 0.07047 0.07269 0.07481 0.07684 0.07879 0.08246 0.08589 0.08911 0.09214 0.09501 0.09774 0.10034 0.10284 0.10524 0.10754 0.11192 0.11603 0.11992 0.12362 0.12715 0.13542 0.14314 0.15056 0.15805 Entropy, Btu/lbm R

|

953

Press., P psia 5 10 15 20 25 30 35 40 45 50 55 60 65 70 75 80 85 90 95 100 110 120 130 140 150 160 170 180 190 200 220 240 260 280 300 350 400 450 500

Evap., ufg 91.280 87.453 84.893 82.898 81.231 79.780 78.485 77.307 76.221 75.209 74.258 73.360 72.505 71.688 70.905 70.151 69.424 68.719 68.035 67.371 66.091 64.869 63.696 62.564 61.467 60.401 59.362 58.345 57.349 56.371 54.458 52.591 50.757 48.945 47.143 42.627 37.963 32.939 27.168

Evap., hfg 99.022 95.528 93.155 91.282 89.701 88.313 87.064 85.920 84.858 83.863 82.924 82.030 81.176 80.357 79.567 78.804 78.064 77.345 76.645 75.962 74.641 73.371 72.144 70.954 69.795 68.662 67.553 66.464 65.392 64.335 62.256 60.213 58.192 56.184 54.176 49.099 43.798 38.041 31.382

Evap., sfg 0.24353 0.22206 0.20908 0.19962 0.19213 0.18589 0.18053 0.17580 0.17158 0.16774 0.16423 0.16098 0.15796 0.15512 0.15245 0.14993 0.14753 0.14525 0.14307 0.14097 0.13703 0.13335 0.12990 0.12665 0.12357 0.12062 0.11781 0.11511 0.11250 0.10998 0.10517 0.10061 0.09625 0.09205 0.08797 0.07814 0.06848 0.05854 0.04762

Sat. vapor, sg 0.23408 0.22948 0.22715 0.22567 0.22462 0.22383 0.22319 0.22268 0.22225 0.22188 0.22156 0.22127 0.22102 0.22080 0.22059 0.22040 0.22022 0.22006 0.21991 0.21976 0.21949 0.21924 0.21901 0.21879 0.21857 0.21836 0.21815 0.21795 0.21774 0.21753 0.21710 0.21665 0.21617 0.21567 0.21512 0.21356 0.21161 0.20911 0.20566

cen84959_ap02.qxd 4/27/05 3:02 PM Page 954

954

|

Thermodynamics

TABLE A13ESuperheated refrigerant-134aT F v ft3/lbm P Sat. 20 0 20 40 60 80 100 120 140 160 180 200 220 4.3753 4.4856 4.7135 4.9380 5.1600 5.3802 5.5989 5.8165 6.0331 6.2490 6.4642 6.6789 6.8930 7.1068 P Sat. 20 40 60 80 100 120 140 160 180 200 220 240 260 280 1.5492 1.5691 1.6528 1.7338 1.8130 1.8908 1.9675 2.0434 2.1185 2.1931 2.2671 2.3408 2.4141 2.4871 2.5598 P Sat. 60 80 100 120 140 160 180 200 220 240 260 280 300 320 0.7936 0.8179 0.8636 0.9072 0.9495 0.9908 1.0312 1.0709 1.1101 1.1489 1.1872 1.2252 1.2629 1.3004 1.3377 s u h Btu/ Btu/lbm Btu/lbm lbm R 10 psia (Tsat 90.59 92.13 95.41 98.77 102.20 105.72 109.32 113.01 116.79 120.66 124.61 128.65 132.77 136.98 29.52F) 0.22948 0.23350 0.24174 0.24976 0.25761 0.26531 0.27288 0.28033 0.28767 0.29490 0.30203 0.30908 0.31604 0.32292 v ft3/lbm P 2.9880 3.1001 3.2551 3.4074 3.5577 3.7064 3.8540 4.0006 4.1464 4.2915 4.4361 4.5802 4.7239 P 1.1760 1.2126 1.2768 1.3389 1.3995 1.4588 1.5173 1.5750 1.6321 1.6887 1.7449 1.8007 1.8562 1.9114 P 0.6821 0.6857 0.7271 0.7662 0.8037 0.8401 0.8756 0.9105 0.9447 0.9785 1.0118 1.0449 1.0776 1.1101 1.1424 u Btu/lbm s h Btu/ Btu/lbm lbm R 14.15F) 0.22715 0.23310 0.24127 0.24922 0.25700 0.26463 0.27212 0.27950 0.28677 0.29393 0.30100 0.30798 0.31487 v ft3/lbm P 2.2772 2.2922 2.4130 2.5306 2.6461 2.7600 2.8726 2.9842 3.0950 3.2051 3.3146 3.4237 3.5324 P 0.9479 s u h Btu/ Btu/lbm Btu/lbm lbm R 20 psia (Tsat 94.30 94.72 98.19 101.70 105.28 108.93 112.66 116.47 120.37 124.35 128.41 132.55 136.78 2.43F) 0.22567 0.22671 0.23504 0.24311 0.25097 0.25866 0.26621 0.27363 0.28093 0.28812 0.29521 0.30221 0.30912

15 psia (Tsat 92.70 95.08 98.48 101.95 105.50 109.13 112.84 116.63 120.51 124.48 128.53 132.66 136.88

98.68 100.43 104.14 107.91 111.75 115.67 119.68 123.78 127.96 132.22 136.57 141.01 145.53 150.13

100.99 103.68 107.52 111.41 115.38 119.42 123.54 127.74 132.02 136.39 140.84 145.37 149.99

102.73 103.20 107.12 111.07 115.07 119.15 123.29 127.52 131.82 136.21 140.67 145.22 149.85

30 psia (Tsat 96.72 97.56 101.17 104.82 108.53 112.30 116.15 120.08 124.08 128.16 132.32 136.57 140.89 145.30 149.78

15.37F) 0.22383 0.22581 0.23414 0.24219 0.25002 0.25767 0.26517 0.27254 0.27979 0.28693 0.29398 0.30092 0.30778 0.31456 0.32126

40 psia (Tsat 98.55 100.61 104.34 108.11 111.93 115.82 119.78 123.81 127.91 132.10 136.36 140.70 145.12 149.61

29.01F) 0.22268 0.22738 0.23565 0.24363 0.25140 0.25900 0.26644 0.27375 0.28095 0.28803 0.29501 0.30190 0.30871 0.31543

50 psia (Tsat 100.04

40.23F) 0.22188

105.32 106.27 110.35 114.45 118.59 122.80 127.07 131.42 135.84 140.34 144.91 149.56 154.29 159.10 163.99

107.26 109.58 113.79 118.02 122.29 126.62 131.01 135.47 140.00 144.60 149.27 154.03 158.86 163.76

108.81

1.0019 1.0540 1.1043 1.1534 1.2015 1.2488 1.2955 1.3416 1.3873 1.4326 1.4776 1.5223 P 0.59750 0.62430 0.66009 0.69415 0.72698 0.75888 0.79003 0.82059 0.85065 0.88030 0.90961 0.93861 0.96737 0.99590

103.84 107.68 111.55 115.48 119.47 123.53 127.66 131.87 136.15 140.50 144.93 149.44

113.11 117.43 121.77 126.16 130.59 135.09 139.65 144.28 148.98 153.76 158.60 163.53

0.23031 0.23847 0.24637 0.25406 0.26159 0.26896 0.27621 0.28333 0.29036 0.29728 0.30411 0.31086

60 psia (Tsat 101.30 103.31 107.23 111.16 115.14 119.16 123.25 127.41 131.63 135.93 140.30 144.75 149.27 153.87 158.54

49.84F) 0.22127 0.22570 0.23407 0.24211 0.24991 0.25751 0.26496 0.27226 0.27943 0.28649 0.29344 0.30030 0.30707 0.31376 0.32037

70 psia (Tsat 102.39 102.73 106.76 110.76 114.78 118.85 122.97 127.15 131.40 135.71 140.10 144.56 149.10 153.71 158.39

58.30F) 0.22080 0.22155 0.23016 0.23836 0.24628 0.25398 0.26149 0.26885 0.27607 0.28317 0.29015 0.29704 0.30384 0.31055 0.31718

80 psia (Tsat 103.35 106.26 110.34 114.42 118.52 122.68 126.89 131.16 135.49 139.90 144.37 148.92 153.54 158.24

65.89F) 0.22040 0.22661 0.23499 0.24304 0.25083 0.25841 0.26583 0.27310 0.28024 0.28726 0.29418 0.30100 0.30773 0.31438

110.11 112.39 116.82 121.24 125.68 130.16 134.70 139.30 143.96 148.69 153.48 158.35 163.29 168.31 173.39

111.22 111.62 116.18 120.68 125.19 129.73 134.31 138.94 143.63 148.39 153.21 158.10 163.06 168.09 173.19

112.20 115.51 120.11 124.69 129.29 133.91 138.58 143.31 148.09 152.93 157.84 162.82 167.86 172.98

cen84959_ap02.qxd 4/27/05 3:02 PM Page 955

Appendix 2 TABLE A13ESuperheated refrigerant-134a (Concluded )T F v ft3/lbm P Sat. 80 100 120 140 160 180 200 220 240 260 280 300 320 0.53113 0.54388 0.57729 0.60874 0.63885 0.66796 0.69629 0.72399 0.75119 0.77796 0.80437 0.83048 0.85633 0.88195 P Sat. 120 140 160 180 200 220 240 260 280 300 320 340 360 0.33771 0.36243 0.38551 0.40711 0.42766 0.44743 0.46657 0.48522 0.50345 0.52134 0.53895 0.55630 0.57345 0.59041 P Sat. 140 160 180 200 220 240 260 280 300 320 340 360 0.22983 0.24541 0.26412 0.28115 0.29704 0.31212 0.32658 0.34054 0.35410 0.36733 0.38029 0.39300 0.40552 u Btu/lbm h Btu/lbm s Btu/ lbm R v ft3/lbm P 0.47760 0.47906 0.51076 0.54022 0.56821 0.59513 0.62122 0.64667 0.67158 0.69605 0.72016 0.74396 0.76749 0.79079 P u Btu/lbm h Btu/lbm s Btu/ lbm R v ft3/lbm P u h Btu/lbm Btu/lbm 120 psia (Tsat

|

955

s Btu/ lbm R

90 psia (Tsat 104.21 105.74 109.91 114.04 118.19 122.38 126.62 130.92 135.27 139.69 144.19 148.75 153.38 158.08

72.78F) 0.22006 0.22330 0.23189 0.24008 0.24797 0.25563 0.26311 0.27043 0.27762 0.28468 0.29162 0.29847 0.30522 0.31189

100 psia (Tsat 104.99 105.18 109.45 113.66 117.86 122.08 126.35 130.67 135.05 139.49 143.99 148.57 153.21 157.93

79.12F) 0.21976 0.22016 0.22900 0.23733 0.24534 0.25309 0.26063 0.26801 0.27523 0.28233 0.28931 0.29618 0.30296 0.30964

90.49F)

113.06 114.80 119.52 124.18 128.83 133.51 138.22 142.97 147.78 152.65 157.58 162.58 167.64 172.77

113.83 114.05 118.90 123.65 128.37 133.09 137.85 142.64 147.47 152.37 157.32 162.34 167.42 172.56

0.39644 106.35 0.41013 0.43692 0.46190 0.48563 0.50844 0.53054 0.55206 0.57312 0.59379 0.61413 0.63420 0.65402 P 108.48 112.84 117.15 121.46 125.79 130.17 134.59 139.07 143.61 148.21 152.88 157.62

115.16 0.21924 117.59 122.54 127.41 132.25 137.09 141.95 146.85 151.80 156.79 161.85 166.96 172.14 0.22362 0.23232 0.24058 0.24851 0.25619 0.26368 0.27100 0.27817 0.28521 0.29214 0.29896 0.30569

140 psia (Tsat 107.51 111.96 116.41 120.81 125.22 129.65 134.12 138.64 143.21 147.85 152.54 157.30 162.13 167.02

100.50F) 0.21879 0.22773 0.23628 0.24443 0.25227 0.25988 0.26730 0.27455 0.28166 0.28864 0.29551 0.30228 0.30896 0.31555

160 psia (Tsat 108.50 111.01 115.62 120.13 124.62 129.12 133.64 138.20 142.81 147.48 152.20 156.98 161.83 166.74

109.50F) 0.21836 0.22337 0.23230 0.24069 0.24871 0.25645 0.26397 0.27131 0.27849 0.28554 0.29246 0.29927 0.30598 0.31260

180 psia (Tsat 109.36 109.94 114.77 119.42 124.00 128.57 133.15 137.76 142.40 147.10 151.85 156.66 161.53 166.46

117.69F) 0.21795 0.21910 0.22850 0.23718 0.24540 0.25330 0.26094 0.26837 0.27562 0.28273 0.28970 0.29656 0.30331 0.30996

116.26 121.35 126.40 131.36 136.30 141.24 146.21 151.21 156.26 161.35 166.50 171.71 176.98 182.32

0.29316 0.30578 0.32774 0.34790 0.36686 0.38494 0.40234 0.41921 0.43564 0.45171 0.46748 0.48299 0.49828 0.51338 P

117.18 120.06 125.32 130.43 135.49 140.52 145.55 150.62 155.71 160.85 166.04 171.28 176.58 181.94

0.25813 0.26083 0.28231 0.30154 0.31936 0.33619 0.35228 0.36779 0.38284 0.39751 0.41186 0.42594 0.43980 0.45347 P

117.96 118.63 124.17 129.46 134.64 139.77 144.88 150.01 155.16 160.34 165.57 170.85 176.18 181.56

200 psia (Tsat 110.11 113.85 118.66 123.35 128.00 132.64 137.30 141.99 146.72 151.50 156.33 161.22 166.17

125.22F) 0.21753 0.22481 0.23384 0.24229 0.25035 0.25812 0.26565 0.27298 0.28015 0.28718 0.29408 0.30087 0.30756

300 psia (Tsat 112.60 113.82 119.52 124.78 129.85 134.83 139.77 144.70 149.65 154.63 159.64 164.70

156.09F)

400 psia (Tsat

179.86F)

118.62 122.93 128.44 133.76 138.99 144.19 149.38 154.59 159.82 165.09 170.40 175.77 181.18

0.14266 0.14656 0.16355 0.17776 0.19044 0.20211 0.21306 0.22347 0.23346 0.24310 0.25246 0.26159

120.52 121.95 128.60 134.65 140.42 146.05 151.59 157.11 162.61 168.12 173.66 179.22

0.21512 0.09642 113.35 0.21745 0.22802 0.23733 0.24594 0.25410 0.26192 0.26947 0.27681 0.28398 0.29098 0.29786

120.48 0.21161

0.09658 0.11440 0.12746 0.13853 0.14844 0.15756 0.16611 0.17423 0.18201 0.18951

113.41 120.52 126.44 131.95 137.26 142.48 147.65 152.80 157.97 163.15

120.56 128.99 135.88 142.20 148.25 154.14 159.94 165.70 171.44 177.18

0.21173 0.22471 0.23500 0.24418 0.25270 0.26077 0.26851 0.27599 0.28326 0.29035

cen84959_ap02.qxd 4/27/05 3:02 PM Page 956

956

|20 3000 2000

Thermodynamics20bm/ 3 ft3

6065

100

14050454035

18030

2203 /ft3 = 1 8 lb m 12 9.6 7.2

260 3000 2000 1000

80

85

95

90

55

70

60

24

1000 R-134a

75 l

D e n sit y

2 2 22

0

180140 140 140

400 200

4.8 3.6 2.4 1.8 1.2 0.96 0.72

T = 100F

400 200 100

60

100 Pressure, psia20 20 20

40-20

0.48 0.36 0.24 0.180.20 0.22 0.240.3 0B tu/l bm R 0.3 2

40 20 10620

-0.04 -0.02

0. 0.00 0.02

20 10

0.14 0.16 0.18

0.04 0.06 0.08

0.10 0.12

0.26

0.3 4

0.3 6

0.12 0.0960.3 80 500 .42

0.28

id

0.4 0

-60T = -1 0 0 F

te d va p o ur - 60 -20 20

T = 3 0 0 F

ate d

220

s atur

60 100 1 40

0.8

0.3

0.6

0.7

0.9

1 80

260

340

380

4 2

4 20

4 60

s=

5 40 580

li q u

0.072 0.048 0.036 0.024 0.018 0.012

4 2 1 260

0.2

0.1

0.4

s atu ra

0.4 20.4 4

0.5

s=

1 20

20

60

100

140

180

220

Enthalpy, Btu/lbm

FIGURE A14E P-h diagram for refrigerant-134a.Reprinted by permission of American Society of Heating, Refrigerating, and Air-Conditioning Engineers, Inc., Atlanta, GA.

0.4 6

cen84959_ap02.qxd 4/27/05 3:02 PM Page 957

Appendix 2 TABLE A16EProperties of the atmosphere at high altitude Altitude, ft 0 500 1000 1500 2000 2500 3000 3500 4000 4500 5000 5500 6000 6500 7000 7500 8000 8500 9000 9500 10,000 11,000 12,000 13,000 14,000 15,000 16,000 17,000 18,000 19,000 20,000 22,000 24,000 26,000 28,000 30,000 32,000 34,000 36,000 38,000 40,000 45,000 50,000 55,000 60,000 Temperature, F 59.00 57.22 55.43 53.65 51.87 50.09 48.30 46.52 44.74 42.96 41.17 39.39 37.61 35.83 34.05 32.26 30.48 28.70 26.92 25.14 23.36 19.79 16.23 12.67 9.12 5.55 1.99 1.58 5.14 8.70 12.2 19.4 26.5 33.6 40.7 47.8 54.9 62.0 69.2 69.7 69.7 69.7 69.7 69.7 69.7 Pressure, psia 14.7 14.4 14.2 13.9 13.7 13.4 13.2 12.9 12.7 12.5 12.2 12.0 11.8 11.6 11.3 11.1 10.9 10.7 10.5 10.3 10.1 9.72 9.34 8.99 8.63 8.29 7.97 7.65 7.34 7.05 6.76 6.21 5.70 5.22 4.78 4.37 3.99 3.63 3.30 3.05 2.73 2.148 1.691 1.332 1.048 Gravity, g, ft/s2 32.174 32.173 32.171 32.169 32.168 32.166 32.165 32.163 32.162 32.160 32.159 32.157 32.156 32.154 32.152 32.151 32.149 32.148 32.146 32.145 32.145 32.140 32.137 32.134 32.131 32.128 32.125 32.122 32.119 32.115 32.112 32.106 32.100 32.094 32.088 32.082 32.08 32.07 32.06 32.06 32.05 32.04 32.02 32.00 31.99 Speed of sound, ft/s 1116 1115 1113 1111 1109 1107 1105 1103 1101 1099 1097 1095 1093 1091 1089 1087 1085 1083 1081 1079 1077 1073 1069 1065 1061 1057 1053 1049 1045 1041 1037 1029 1020 1012 1003 995 987 978 969 968 968 968 968 968 968 Density, lbm/ft3 0.07647 0.07536 0.07426 0.07317 0.07210 0.07104 0.06998 0.06985 0.06792 0.06690 0.06590 0.06491 0.06393 0.06296 0.06200 0.06105 0.06012 0.05919 0.05828 0.05738 0.05648 0.05473 0.05302 0.05135 0.04973 0.04814 0.04659 0.04508 0.04361 0.04217 0.04077 0.03808 0.03553 0.03311 0.03082 0.02866 0.02661 0.02468 0.02285 0.02079 0.01890 0.01487 0.01171 0.00922 0.00726 Viscosity m, lbm/ft s 1.202 1.199 1.196 1.193 1.190 1.186 1.183 1.180 1.177 1.173 1.170 1.167 1.164 1.160 1.157 1.154 1.150 1.147 1.144 1.140 1.137 1.130 1.124 1.117 1.110 1.104 1.097 1.090 1.083 1.076 1.070 1.056 1.042 1.028 1.014 1.000 0.986 0.971 0.956 0.955 0.955 0.955 0.955 0.955 0.955 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 10 105 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5

|

957

Thermal conductivity, Btu/h ft R 0.0146 0.0146 0.0146 0.0145 0.0145 0.0144 0.0144 0.0143 0.0143 0.0142 0.0142 0.0141 0.0141 0.0141 0.0140 0.0140 0.0139 0.0139 0.0138 0.0138 0.0137 0.0136 0.0136 0.0135 0.0134 0.0133 0.0132 0.0132 0.0130 0.0129 0.0128 0.0126 0.0124 0.0122 0.0121 0.0119 0.0117 0.0115 0.0113 0.0113 0.0113 0.0113 0.0113 0.0113 0.0113

Source: U.S. Standard Atmosphere Supplements, U.S. Government Printing Office, 1966. Based on year-round mean conditions at 45 latitude and varies with the time of the year and the weather patterns. The conditions at sea level (z 0) are taken to be P 14.696 psia, T 59F, 32.1741 ft2/s. r 0.076474 lbm/ft3, g

cen84959_ap02.qxd 4/27/05 3:02 PM Page 958

958

|

Thermodynamics

TABLE A17EIdeal-gas properties of air T R 360 380 400 420 440 460 480 500 520 537 540 560 580 600 620 640 660 680 700 720 740 760 780 800 820 840 860 880 900 920 940 960 980 1000 1040 1080 1120 1160 1200 1240 1280 1320 1360 1400 1440 1480 1520 1560 h Btu/lbm 85.97 90.75 95.53 100.32 105.11 109.90 114.69 119.48 124.27 128.10 129.06 133.86 138.66 143.47 148.28 153.09 157.92 162.73 167.56 172.39 177.23 182.08 186.94 191.81 196.69 201.56 206.46 211.35 216.26 221.18 226.11 231.06 236.02 240.98 250.95 260.97 271.03 281.14 291.30 301.52 311.79 322.11 332.48 342.90 353.37 363.89 374.47 385.08 Pr 0.3363 0.4061 0.4858 0.5760 0.6776 0.7913 0.9182 1.0590 1.2147 1.3593 1.3860 1.5742 1.7800 2.005 2.249 2.514 2.801 3.111 3.446 3.806 4.193 4.607 5.051 5.526 6.033 6.573 7.149 7.761 8.411 9.102 9.834 10.61 11.43 12.30 14.18 16.28 18.60 21.18 24.01 27.13 30.55 34.31 38.41 42.88 47.75 53.04 58.78 65.00 u Btu/lbm 61.29 64.70 68.11 71.52 74.93 78.36 81.77 85.20 88.62 91.53 92.04 95.47 98.90 102.34 105.78 109.21 112.67 116.12 119.58 123.04 126.51 129.99 133.47 136.97 140.47 143.98 147.50 151.02 154.57 158.12 161.68 165.26 168.83 172.43 179.66 186.93 194.25 201.63 209.05 216.53 224.05 231.63 239.25 246.93 254.66 262.44 270.26 278.13 vr 396.6 346.6 305.0 270.1 240.6 215.33 193.65 174.90 158.58 146.34 144.32 131.78 120.70 110.88 102.12 94.30 87.27 80.96 75.25 70.07 65.38 61.10 57.20 53.63 50.35 47.34 44.57 42.01 39.64 37.44 35.41 33.52 31.76 30.12 27.17 24.58 22.30 20.29 18.51 16.93 15.52 14.25 13.12 12.10 11.17 10.34 9.578 8.890 s T Btu/lbm R R 0.50369 0.51663 0.52890 0.54058 0.55172 0.56235 0.57255 0.58233 0.59173 0.59945 0.60078 0.60950 0.61793 0.62607 0.63395 0.64159 0.64902 0.65621 0.66321 0.67002 0.67665 0.68312 0.68942 0.69558 0.70160 0.70747 0.71323 0.71886 0.72438 0.72979 0.73509 0.74030 0.74540 0.75042 0.76019 0.76964 0.77880 0.78767 0.79628 0.80466 0.81280 0.82075 0.82848 0.83604 0.84341 0.85062 0.85767 0.86456 1600 1650 1700 1750 1800 1850 1900 1950 2000 2050 2100 2150 2200 2250 2300 2350 2400 2450 2500 2550 2600 2650 2700 2750 2800 2850 2900 2950 3000 3050 3100 3150 3200 3250 3300 3350 3400 3450 3500 3550 3600 3650 3700 3750 3800 3850 3900 3950 h Btu/lbm 395.74 409.13 422.59 436.12 449.71 463.37 477.09 490.88 504.71 518.71 532.55 546.54 560.59 574.69 588.82 603.00 617.22 631.48 645.78 660.12 674.49 688.90 703.35 717.83 732.33 746.88 761.45 776.05 790.68 805.34 820.03 834.75 849.48 864.24 879.02 893.83 908.66 923.52 938.40 953.30 968.21 983.15 998.11 1013.1 1028.1 1043.1 1058.1 1073.2 Pr 71.13 80.89 90.95 101.98 114.0 127.2 141.5 157.1 174.0 192.3 212.1 223.5 256.6 281.4 308.1 336.8 367.6 400.5 435.7 473.3 513.5 556.3 601.9 650.4 702.0 756.7 814.8 876.4 941.4 1011 1083 1161 1242 1328 1418 1513 1613 1719 1829 1946 2068 2196 2330 2471 2618 2773 2934 3103 u Btu/lbm 286.06 296.03 306.06 316.16 326.32 336.55 346.85 357.20 367.61 378.08 388.60 399.17 409.78 420.46 431.16 441.91 452.70 463.54 474.40 485.31 496.26 507.25 518.26 529.31 540.40 551.52 562.66 573.84 585.04 596.28 607.53 618.82 630.12 641.46 652.81 664.20 675.60 687.04 698.48 709.95 721.44 732.95 744.48 756.04 767.60 779.19 790.80 802.43 vr s Btu/lbm R 0.87130 0.87954 0.88758 0.89542 0.90308 0.91056 0.91788 0.92504 0.93205 0.93891 0.94564 0.95222 0.95919 0.96501 0.97123 0.97732 0.98331 0.98919 0.99497 1.00064 1.00623 1.01172 1.01712 1.02244 1.02767 1.03282 1.03788 1.04288 1.04779 1.05264 1.05741 1.06212 1.06676 1.07134 1.07585 1.08031 1.08470 1.08904 1.09332 1.09755 1.10172 1.10584 1.10991 1.11393 1.11791 1.12183 1.12571 1.12955

8.263 7.556 6.924 6.357 5.847 5.388 4.974 4.598 4.258 3.949 3.667 3.410 3.176 2.961 2.765 2.585 2.419 2.266 2.125 1.996 1.876 1.765 1.662 1.566 1.478 1.395 1.318 1.247 1.180 1.118 1.060 1.006 0.955 0.907 0.8621 0.8202 0.7807 0.7436 0.7087 0.6759 0.6449 0.6157 0.5882 0.5621 0.5376 0.5143 0.4923 0.4715

cen84959_ap02.qxd 4/27/05 3:02 PM Page 959

Appendix 2 TABLE A17EIdeal-gas properties of air (Concluded) T R 4000 4050 4100 4150 4200 4300 4400 4500 h Btu/lbm 1088.3 1103.4 1118.5 1133.6 1148.7 1179.0 1209.4 1239.9 Pr 3280 3464 3656 3858 4067 4513 4997 5521 u Btu/lbm 814.06 825.72 837.40 849.09 860.81 884.28 907.81 931.39 vr 0.4518 0.4331 0.4154 0.3985 0.3826 0.3529 0.3262 0.3019 s Btu/lbm R 1.13334 1.13709 1.14079 1.14446 1.14809 1.15522 1.16221 1.16905 T R 4600 4700 4800 4900 5000 5100 5200 5300 h Btu/lbm 1270.4 1300.9 1331.5 1362.2 1392.9 1423.6 1454.4 1485.3 Pr 6089 6701 7362 8073 8837 9658 10,539 11,481 u Btu/lbm 955.04 978.73 1002.5 1026.3 1050.1 1074.0 1098.0 1122.0 vr 0.2799 0.2598 0.2415 0.2248 0.2096 0.1956 0.1828 0.1710

|

959

s Btu/lbm R 1.17575 1.18232 1.18876 1.19508 1.20129 1.20738 1.21336 1.21923

Note: The properties Pr (relative pressure) and vr (relative specific volume) are dimensionless quantities used in the analysis of isentropic processes, and should not be confused with the properties pressure and specific volume. Source: Kenneth Wark, Thermodynamics, 4th ed. (New York: McGraw-Hill, 1983), pp. 83233, Table A5. Originally published in J. H. Keenan and J. Kaye, Gas Tables (New York: John Wiley & Sons, 1948).

cen84959_ap02.qxd 4/27/05 3:02 PM Page 960

960

|

Thermodynamics

TABLE A18EIdeal-gas properties of nitrogen, N2 _ _ T h u R Btu/lbmol Btu/lbmol 300 320 340 360 380 400 420 440 460 480 500 520 537 540 560 580 600 620 640 660 680 700 720 740 760 780 800 820 840 860 880 900 920 940 960 980 1000 1020 1040 1060 2,082.0 2,221.0 2,360.0 2,498.9 2,638.0 2,777.0 2,916.1 3,055.1 3,194.1 3,333.1 3,472.2 3,611.3 3,729.5 3,750.3 3,889.5 4,028.7 4,167.9 4,307.1 4,446.4 4,585.8 4,725.3 4,864.9 5,004.5 5,144.3 5,284.1 5,424.2 5,564.4 5,704.7 5,845.3 5,985.9 6,126.9 6,268.1 6,409.6 6,551.2 6,693.1 6,835.4 6,977.9 7,120.7 7,263.8 7,407.2 1,486.2 1,585.5 1,684.4 1,784.0 1,883.4 1,982.6 2,082.0 2,181.3 2,280.6 2,379.9 2,479.3 2,578.6 2,663.1 2,678.0 2,777.4 2,876.9 2,976.4 3,075.9 3,175.5 3,275.2 3,374.9 3,474.8 3,574.7 3,674.7 3,774.9 3,875.2 3,975.7 4,076.3 4,177.1 4,278.1 4,379.4 4,480.8 4,582.6 4,684.5 4,786.7 4,889.3 4,992.0 5,095.1 5,198.5 5,302.2 _ s Btu/lbmol R 41.695 42.143 42.564 42.962 43.337 43.694 44.034 44.357 44.665 44.962 45.246 45.519 45.743 45.781 46.034 46.278 46.514 46.742 46.964 47.178 47.386 47.588 47.785 47.977 48.164 48.345 48.522 48.696 48.865 49.031 49.193 49.352 49.507 49.659 49.808 49.955 50.099 50.241 50.380 50.516 T R 1080 1100 1120 1140 1160 1180 1200 1220 1240 1260 1280 1300 1320 1340 1360 1380 1400 1420 1440 1460 1480 1500 1520 1540 1560 1580 1600 1620 1640 1660 1680 1700 1720 1740 1760 1780 1800 1820 1840 1860 _ h Btu/lbmol 7,551.0 7,695.0 7,839.3 7,984.0 8,129.0 8,274.4 8,420.0 8,566.1 8,712.6 8,859.3 9,006.4 9,153.9 9,301.8 9,450.0 9,598.6 9,747.5 9,896.9 10,046.6 10,196.6 10,347.0 10,497.8 10,648.0 10,800.4 10,952.2 11,104.3 11,256.9 11,409.7 11,562.8 11,716.4 11,870.2 12,024.3 12,178.9 12,333.7 12,488.8 12,644.3 12,800.2 12,956.3 13,112.7 13,269.5 13,426.5 _ u Btu/lbmol 5,406.2 5,510.5 5,615.2 5,720.1 5,825.4 5,931.0 6,037.0 6,143.4 6,250.1 6,357.2 6,464.5 6,572.3 6,680.4 6,788.9 6,897.8 7,007.0 7,116.7 7,226.7 7,337.0 7,447.6 7,558.7 7,670.1 7,781.9 7,893.9 8,006.4 8,119.2 8,232.3 8,345.7 8,459.6 8,573.6 8,688.1 8,802.9 8,918.0 9,033.4 9,149.2 9,265.3 9,381.7 9,498.4 9,615.5 9,732.8 _ s Btu/lbmol R 50.651 50.783 50.912 51.040 51.167 51.291 51.143 51.534 51.653 51.771 51.887 51.001 52.114 52.225 52.335 52.444 52.551 52.658 52.763 52.867 52.969 53.071 53.171 53.271 53.369 53.465 53.561 53.656 53.751 53.844 53.936 54.028 54.118 54.208 54.297 54.385 54.472 54.559 54.645 54.729

cen84959_ap02.qxd 4/27/05 3:02 PM Page 961

Appendix 2 TABLE A18EIdeal-gas properties of nitrogen, N2 (Concluded) _ _ _ T h u s R Btu/lbmol Btu/lbmol Btu/lbmol R 1900 1940 1980 2020 2060 2100 2140 2180 2220 2260 2300 2340 2380 2420 2460 2500 2540 2580 2620 2660 2700 2740 2780 2820 2860 2900 2940 2980 3020 3060 3100 3140 3180 3220 3260 3300 3340 3380 3420 3460 13,742 14,058 14,375 14,694 15,013 15,334 15,656 15,978 16,302 16,626 16,951 17,277 17,604 17,392 18,260 18,590 18,919 19,250 19,582 19,914 20,246 20,580 20,914 21,248 21,584 21,920 22,256 22,593 22,930 23,268 23,607 23,946 24,285 24,625 24,965 25,306 25,647 25,989 26,331 26,673 9,968 10,205 10,443 10,682 10,923 11,164 11,406 11,649 11,893 12,138 12,384 12,630 12,878 13,126 13,375 13,625 13,875 14,127 14,379 14,631 14,885 15,139 15,393 15,648 15,905 16,161 16,417 16,675 16,933 17,192 17,451 17,710 17,970 18,231 18,491 18,753 19,014 19,277 19,539 19,802 54.896 55.061 55.223 55.383 55.540 55.694 55.846 55.995 56.141 56.286 56.429 56.570 56.708 56.845 56.980 57.112 57.243 57.372 57.499 57.625 57.750 57.872 57.993 58.113 58.231 58.348 58.463 58.576 58.688 58.800 58.910 59.019 59.126 59.232 59.338 59.442 59.544 59.646 59.747 59.846 T R 3500 3540 3580 3620 3660 3700 3740 3780 3820 3860 3900 3940 3980 4020 4060 4100 4140 4180 4220 4260 4300 4340 4380 4420 4460 4500 4540 4580 4620 4660 4700 4740 4780 4820 4860 4900 5000 5100 5200 5300 _ h Btu/lbmol 27,016 27,359 27,703 28,046 28,391 28,735 29,080 29,425 29,771 30,117 30,463 30,809 31,156 31,503 31,850 32,198 32,546 32,894 33,242 33,591 33,940 34,289 34,638 34,988 35,338 35,688 36,038 36,389 36,739 37,090 37,441 37,792 38,144 38,495 38,847 39,199 40,080 40,962 41,844 42,728 _ u Btu/lbmol 20,065 20,329 20,593 20,858 21,122 21,387 21,653 21,919 22,185 22,451 22,718 22,985 23,252 23,520 23,788 24,056 24,324 24,593 24,862 25,131 25,401 25,670 25,940 26,210 26,481 26,751 27,022 27,293 27,565 27,836 28,108 28,379 28,651 28,924 29,196 29,468 30,151 30,834 31,518 32,203

|

961

_ s Btu/lbmol R 59.944 60.041 60.138 60.234 60.328 60.422 60.515 60.607 60.698 60.788 60.877 60.966 61.053 61.139 61.225 61.310 61.395 61.479 61.562 61.644 61.726 61.806 61.887 61.966 62.045 62.123 62.201 62.278 62.354 62.429 62.504 62.578 62.652 62.725 62.798 62.870 63.049 63.223 63.395 63.563

Source: Tables A18E through A23E are adapted from Kenneth Wark, Thermodynamics, 4th ed. (New York: McGraw-Hill, 1983), pp. 83444. Originally published in J. H. Keenan and J. Kaye, Gas Tables (New York: John Wiley & Sons, 1945).

cen84959_ap02.qxd 4/27/05 3:02 PM Page 962

962

|

Thermodynamics

TABLE A19EIdeal-gas properties of oxygen, O2 _ _ T h u R Btu/lbmol Btu/lbmol 300 320 340 360 380 400 420 440 460 480 500 520 537 540 560 580 600 620 640 660 680 700 720 740 760 780 800 820 840 860 880 900 920 940 960 980 1000 1020 1040 1060 2,073.5 2,212.6 2,351.7 2,490.8 2,630.0 2,769.1 2,908.3 3,047.5 3,186.9 3,326.5 3,466.2 3,606.1 3,725.1 3,746.2 3,886.6 4,027.3 4,168.3 4,309.7 4,451.4 4,593.5 4,736.2 4,879.3 5,022.9 5,167.0 5,311.4 5,456.4 5,602.0 5,748.1 5,894.8 6,041.9 6,189.6 6,337.9 6,486.7 6,636.1 6,786.0 6,936.4 7,087.5 7,238.9 7,391.0 7,543.6 1,477.8 1,577.1 1,676.5 1,775.9 1,875.3 1,974.8 2,074.3 2,173.8 2,273.4 2,373.3 2,473.2 2,573.4 2,658.7 2,673.8 2,774.5 2,875.5 2,976.8 3,078.4 3,180.4 3,282.9 3,385.8 3,489.2 3,593.1 3,697.4 3,802.4 3,907.5 4,013.3 4,119.7 4,226.6 4,334.1 4,442.0 4,550.6 4,659.7 4,769.4 4,879.5 4,990.3 5,101.6 5,213.3 5,325.7 5,438.6 _ s Btu/lbmol R 44.927 45.375 45.797 46.195 46.571 46.927 47.267 47.591 47.900 48.198 48.483 48.757 48.982 49.021 49.276 49.522 49.762 49.993 50.218 50.437 50.650 50.858 51.059 51.257 51.450 51.638 51.821 52.002 52.179 52.352 52.522 52.688 52.852 53.012 53.170 53.326 53.477 53.628 53.775 53.921 T R 1080 1100 1120 1140 1160 1180 1200 1220 1240 1260 1280 1300 1320