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TABLE A-2 Properties of Saturated Water (Liquid–Vapor): Temperature Table\n\nSpecific Volume Internal Energy Enthalpy Entropy\nm³/kg kJ/kg kJ/kg kJ/kg·K\nTemp. °C Press.\nbar Sat. Liquid v_f × 10⁻³ Sat. Vapor v_g × 10³ Sat. Liquid h_f Sat. Vapor h_g Evap. h_fg Sat. Liquid s_f Sat. Vapor s_g\n, Press. bar\n0 0.00611 1.0002 206.136 0.00 2375.3 0.01 2501.3 2507.8 0.000 15.632 0.01\n1 0.00813 1.0001 157.232 16.77 2380.6 2419.1 2508.7 0.061 0.054 16.567 0.01\n2 0.00872 1.0001 147.210 20.09 2382.3 2489.1 2516.0 0.076 15.403 16.405 0.01\n//... (more data) TABLE A-2 (Continued)\n\nSpecific Volume Internal Energy Enthalpy Entropy\nm³/kg kJ/kg kJ/kg kJ/kg·K\nTemp. °C Press.\nbar Sat. Liquid v_f × 10⁻³ Sat. Vapor v_g × 10³ Sat. Liquid h_f Sat. Vapor h_g Evap. h_fg Sat. Liquid s_f Sat. Vapor s_g\n, Press. bar\n150 0.56 1.00060 25.216 14.667 242.3 146.68 2563.0 2568.1 1.953 8.059 150\n155 0.597 1.00063 23.940 150.50 242.4 150.86 2416.2 2467.6 1.518 8.536 160\n160 0.612 1.0060 22.114 158.89 241.6 2586.0 2587.9 2.031 8.354 160\n//... (more data) TABLE A-3 Properties of Saturated Water (Liquid–Vapor): Pressure Table\n\nSpecific Volume Internal Energy Enthalpy Entropy\nm³/kg kJ/kg kJ/kg kJ/kg·K\nPress.\nbar Temp. °C Sat. Liquid v_f × 10⁻³ Sat. Vapor v_g × 10³ Sat. Liquid h_f Sat. Vapor h_g Evap. h_fg Sat. Liquid s_f Sat. Vapor s_g Press.\nbar\n0.04 26.96 1.0064 34.800 121.45 2415.2 121.46 2544.2 0.226 4.8746 0.04\n0.06 36.16 1.0064 34.739 2452.0 151.63 2419.5 2564.8 0.521 8.3040 0.06\n0.08 45.11 1.0084 18.103 173.87 2423.2 173.83 2403.1 0.576 8.227 0.08\n0.10 60.00 1.0120 22.674 201.24 2327.6 199.46 2388.7 0.625 8.028 0.10\n0.20 60.10 1.0223 2.529 289.20 289.20 2363.1 2623.3 0.915 7.968 0.20\n0.40 81.31 1.0301 3.402 340.84 2487.9 239.6 2634.9 1.032 7.919 0.40\n0.60 91.71 1.0330 4.732 395.75 2489.60 2653.9 2635.15 1.1453 7.520 0.60\n0.80 100.00 1.0340 2.365 375.24 2441.2 2527.00 2763.9 1.199 7.427 0.80\n1.00 120.0 1.0380 0.679 482.56 2484.9 2576.0 2675.3 1.300 6.952 1.00\n1.50 160.0 1.0480 1.069 663.86 2510.1 2520.6 2698.0 1.503 6.247 1.50\n2.00 180.0 1.0680 0.867 861.82 2489.0 2655.3 2670.6 1.684 5.432 2.00\n//... (more data) TABLE A-3 (Continued)\n\nSpecific Volume Internal Energy Enthalpy Entropy\n m3/kg kJ/kg kJ/kg kJ/kg K\nPress. Sat. Liquid Sat. Vapor Sat. Liquid Sat. Vapor Sat. Liquid Sat. Vapor Sat. Liquid\n bar °C vL x 10^3 vG hL hG Evap hg sL sG\n120 324.8 1.5267 0.04246 1473.20 2517.71 1491.13 1193.6 2684.9 4.9462 5.9423 120.\n130 330.9 1.5671 0.01278 1511.41 2496.1 1531.5 1130.7 2662.2 3.5606 5.4323 130.\n140 336.2 1.6017 0.01149 1548.46 2476.8 1571.1 1065.6 2637.6 3.6322 5.3177 140.\n150 342.2 1.6581 0.01034 1585.8 2455.6 1588.9 1006.0 2610.3 3.6878 5.2086 150.\n160 347.4 1.7017 0.00930 1622.27 2431.47 1601.1 994.0 2580.0 3.7461 5.1458 160.\n170 353.1 1.7702 0.00864 1660.20 2390.5 1690.3 856.9 2547.2 3.9127 5.1177 170.\n180 359.7 1.8937 0.00780 1699.1 2344.9 1785.7 801.4 2510.3 4.0919 5.0585 180.\n190 366.5 1.9243 0.00657 1739.9 2328.1 1776.6 788.0 2464.1 3.9884 5.0228 190.\n200 368.5 2.0365 0.00584 1785.6 2309.6 1826.3 758.1 2409.9 4.8199 4.9269 200.\n220 374.1 3.155 0.003155 2029.6 2099.3 0 2099.3 4.4298 4.4298 220.9 TABLE A-6 Properties of Superheated Water Vapor\n T v u kJ/kg kJ/kg kJ/kg K\n °C m3/kg m2/kg m2/kg m2/kg m3/kg\np = 0.06 bar = 0.006 MPa\n (Tav = 36.16°C) \np = 0.35 bar = 0.035 MPa\n (Tav = 72.67°C)\n Sat. 23.739 2425.2 2567.4 8.3304 4.526 2473.01 2631.14 2657.5 7.564 4.411 5.784\n80 27.112 2487.5 2560.1 5.5804 6.135 2465.7 2535.7 2675.7 7.512 5.753 5.614\n120 30.200 2547.1 2726.0 8.7840 5.504 2596.3 2653.5 2725.6 7.967 5.415 6.118\n140 32.001 2602.7 2796.8 9.8999 5.566 2607.2 2785.9 2810.6 9.715 5.655 6.358\n200 36.363 2651.4 2877.9 9.1923 5.505 2608.2 2781.1 2877.1 8.920 6.827 6.634\n240 39.362 2712.1 2957.8 9.2982 6.758 2720.2 2857.0 2878.4 8.932 7.198 6.557\n280 43.197 2780.2 3035.0 8.3126 2.546 2774.6 2896.0 2580.1 8.315 5.591 7.167\n320 36.753 2841.7 3115.0 8.5044 3.754 2813.8 2943.1 2706.3 8.839 6.075 7.238\n440 44.321 2975.9 3485.8 9.9140 3.673 2916.9 3036.3 3183.5 9.762 6.746 7.997\n500 29.853 3481.0 3488.5 1.0198 3.243 3042.1 3142.5 3287.5 7.717 5.738 7.892 TABLE A-4 (Continued)\n\n T v u kJ/kg kJ/kg kJ/kg K\n °C m3/kg m2/kg m2/kg m2/kg m3/kg\np = 5.0 bar = 0.50 MPa\n (Tav = 151.86°C) \np = 7.0 bar = 0.70 MPa\n (Tav = 164.97°C)\n Sat. 0.3749 2681.2 2748.7 6.8213 0.2729 2572.5 2761.3 12.821 7.088 0.8066\n120 0.4240 2607.9 2816.0 6.9665 0.2487 2599.3 2799.7 14.825 8.780 6.911\n260 0.4250 2643.0 2830.1 7.7400 0.2957 2850.1 2890.6 13.657 7.137 0.721\n360 0.3891 2721.0 2902.1 7.8233 0.2932 2762.3 2921.9 12.482 5.579 6.877\n400 0.3066 2957.3 3269.9 7.4651 0.2030 2915.3 3255.5 7.152 6.129 7.209\n420 0.3357 3036.5 3330.3 7.7046 0.2160 3012.6 3475.5 9.335 6.376 7.596\n540 0.3710 3114.3 3378.1 7.8298 0.1878 3181.9 3560.9 7.699 7.347 7.648\n600 0.4325 3256.4 3506.0 8.4082 0.2159 3700.0 3722.1 8.089 5.596 7.892 TABLE A-6 (Continued)\n\nT \u00b0C kJ/kg kJ/kg m\u00b3/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg\n \n h \n \n \n\np = 40 bar - 40.0 MPa\n (T\u00b0 = 250.4\u00b0C)\nSat. 0.04976 2602.3 2801.4 6.0701 0.03244 2589.77 2754.3 5.8902\n \n320 0.06789 2674.01 3014.5 6.2586 0.03717 2647.16 2657.3 6.1436\n360 0.07891 2865.4 3117.2 6.6215 0.04311 2833.20 2924.1 6.4654\n400 0.09269 3173.4 3210.8 6.7082 0.04739 2951.67 2952.2 6.5076\n440 0.10841 3263.1… TABLE A-4 (Continued)\n\nT \u00b0C v \n m\u00b3/kg kJ/kg kJ/kg\u00b7K \n h \n kJ/kg kJ/kg kJ/kg\u00b7K\n p = 160 bar - 16.0 MPa \n (T\u00b0 = 347.44\u00b0C)\nSat. 0.00931 243.17 2580.6 5.2455 0.00749 2437.43 2509.1 5.1044 \n360 0.01105 259.90 2711.5 5.4641 0.00809 2419.84 2564.5 5.1922 \n400 0.01426 279.84 2947.67 5.8175 0.01190 2672.87 2887.5 5.6887 \n440 0.01625 283.94 3103.67 6.0429 0.01414 2862.8 3062.1 5.9438 \n480 0.01842 293.71 3234.4 6.2215 0.01596 2918.5 3202.6 6.1345 \n520 0.02013 303.11 3353.3 6.3752 0.01757 3011.5 3378.6 6.2960 \n600 0.02216 317.18 3464.5 6.6132 0.02048 3109.7 3555.6 6.4966 \n640 0.02407 324.82 3678.0 6.7980 0.02361 3227.3 3666.3 6.7474 \n700 0.02674 340.6 3823.9 6.9224 0.02362 3396.3 3821.5 6.8580 \n740 0.02806 348.67 3935.7 7.0511 0.02438 3478.0 3925.0 6.9625 \n\np = 200 bar - 20.0 MPa\np = 240 bar - 240 MPa\n\n0.00323 2469.20 4.9269\n0.00400 2679.63 5.5014\n0.00445 3000.2 5.6439\n0.00400 2912.6 5.8660\n0.00400 3186.39 6.1913\n0.00400 3450.52 6.2770\n\np = 280 bar - 28.0 MPa\np = 320 bar - 32.0 MPa\n... TABLE A-5 Properties of Compressed Liquid Water\n\nT \u00b0C \n\nv x 10\u00b3 u \n m\u00b3/kg kJ/kg kJ/kg kJ/kg\u00b7K\n \n \n kJ/kg kJ/kg kJ/kg\u00b7K\n p = 25 bar - 2.5 MPa \n (T\u00b0 = 223.99\u00b0C)\n20 1.0005 83.80 86.30 0.2961 0.9995 83.65 86.85 0.2965 \n40 1.0067 167.25 169.77 0.5715 1.0055 166.10 171.67 0.3286 \n80 1.0242 414.84 420.83 1.0305 1.0410 371.42 332.88 1.0300 \n140 1.0748 587.92 590.52 1.0706 1.0737 614.30 645.21 1.1140 \n180 1.1261 761.16 763.97 1.1375 1.1240 759.63 765.25 1.1341 \n...\n\np = 200 bar - 20.0 MPa\np = 100 bar - 10.0 MPa\n... 732 Tables in SI Units\n\nTABLE A-9 Properties of Superheated Refrigerant 22 Vapor\n\nT \u00baC v u h s v u h \n m\u00b3/kg kJ/kg kJ/kg \t kJ/kg \u00b7 K\n\np = 0.4 bar = 0.04 MPa p = 0.6 bar = 0.06 MPa \n(t\u2090 = -58.86\u00baC)\n\nSat. 0.50509 204.13 224.36 1.0512 0.34665 207.14 227.73 1.0294\n-55 0.51158 205.92 225.63 1.0612 0.34895 208.20 228.74 1.0392\n-50 0.52787 208.26 229.38 1.0741 0.34895 208.20 228.74 1.0392\n-45 0.54087 210.63 232.14 1.0868 0.35747 210.20 231.14 1.0459\n-40 0.55238 213.03 233.13 1.0993 0.36694 211.30 232.14 1.0513\n-35 0.56626 215.48 235.01 1.1117 0.37347 215.06 236.14 1.0562\n-30 0.57576 218.25 238.09 1.1239 0.37721 217.57 237.72 1.0862\n-25 0.59002 220.43 241.06 1.1348 0.39215 220.87 241.38 1.0821\n-20 0.60246 222.88 244.95 1.1479 0.39942 224.18 246.15 1.0921\n-15 0.61485 225.39 247.50 1.1597 0.40230 227.34 249.82 1.0979\n-10 0.62679 227.53 250.91 1.1714 0.40627 229.59 252.81 1.1042\n -5 0.63953 229.60 253.98 1.1812 0.40894 231.64 254.79 1.1152\n 0 0.65113 231.13 251.94 1.1944 0.43261 232.17 256.53 1.1255\n-\n\np = 1.5 bar = 0.15 MPa p = 2.0 bar = 0.20 MPa \n(t\u2090 = -32.0\u00baC)\n\nSat. 0.14721 214.77 238.86 0.9830 0.11322 217.42 239.88 0.9691\n-30 0.14872 215.85 236.16 0.9833 0.11285 217.51 238.00 0.9650\n-25 0.15228 218.45 241.30 1.0011 0.11242 217.50 239.01 0.9660\n-20 0.15882 221.07 244.15 1.0177 0.11179 218.79 240.56 0.9674\n-10 0.16920 225.36 247.16 1.0502 0.12067 225.49 245.39 0.9857\n 0 0.16987 227.20 250.61 1.0621 0.12614 229.63 248.52 0.9883\n 15 0.18153 239.91 263.93 1.0834 0.13397 236.81 257.15 0.9630\n 25 0.18693 245.49 273.53 1.1193 0.13912 240.29 255.69 0.9641\n 733 Tables in SI Units\n\nTABLE A-9 (Continued)\n\nT \u00baC v u h s v u h \n m\u00b3/kg kJ/kg kJ/kg \t kJ/kg \u00b7 K\n\np = 2.5 bar = 0.25 MPa p = 3.0 bar = 0.30 MPa \n(t\u2090 = -14.66\u00baC)\n\nSat. 0.09097 219.15 242.29 0.9566 0.07651 221.34 244.29 0.9502\n 0 0.09303 222.30 245.29 0.9730 0.07823 223.39 247.46 0.9623\n -5 0.09521 225.47 246.81 0.9813 0.08025 226.89 250.86 0.9751\n-10 0.09761 227.13 249.57 0.9860 0.08339 229.05 253.70 0.9790\n-15 0.09941 227.32 250.85 0.9860 0.08389 229.37 254.09 0.9794\n-20 0.10183 229.23 251.62 0.9931 0.08415 229.73 255.82 0.9831\n-25 0.10325 231.14 253.06 1.0074 0.08572 231.87 258.01 0.9847\n-30 0.10492 232.67 254.63 1.0146 0.08740 233.07 260.17 0.9850\n-35 0.10601 234.39 256.14 1.0198 0.08875 234.76 261.32 0.9874\n-40 0.10626 235.31 257.64 1.0207 0.08918 235.18 262.30 0.9890\n-45 0.10767 236.87 259.66 1.0243 0.08973 236.70 263.37 0.9915\n-50 0.10966 238.94 261.71 1.0390 0.09079 238.79 264.98 0.9947\n-55 0.11068 239.76 262.16 1.0451 0.09101 239.90 265.05 0.9933\n-60 0.11203 243.22 268.12 1.0696 0.09155 242.20 267.59 1.0043\n-70 0.11329 247.22 270.95 1.0756 0.09214 243.17 269.25 1.0056\n-80 0.11502 249.15 275.33 1.0867 0.09346 246.12 270.79 1.0076\n-90 0.11631 250.05 276.27 1.0917 0.09387 247.51 273.06 1.0101\n-100 0.11711 250.75 278.59 1.0952 0.09404 248.56 274.75 1.0115\n \n\np = 3.5 bar = 0.35 MPa p = 4.0 bar = 0.40 MPa \n(t\u2090 = -6.56\u00baC)\n\nSat. 0.06512 222.88 246.00 0.9431 0.05812 224.24 247.48 0.9370\n-10 0.06701 224.47 247.74 0.9516 0.06000 226.16 248.00 0.9411\n-15 0.06807 225.07 248.71 0.9589 0.06029 226.93 248.36 0.9434\n-20 0.06951 225.74 249.07 0.9622 0.06213 227.80 248.78 0.9455\n-25 0.07081 226.19 249.89 0.9667 0.06292 228.30 249.23 0.9482\n-30 0.07291 226.63 250.59 0.9711 0.06512 229.66 249.54 0.9548\n-35 0.07521 228.12 251.03 0.9757 0.06764 230.00 251.22 0.9615\n-40 0.07701 228.97 252.11 0.9781 0.07082 230.11 252.62 0.9685\n-45 0.07882 229.55 252.80 0.9797 0.07819 231.02 253.17 0.9792\n-50 0.08072 230.38 253.52 0.9798 0.07992 231.78 254.70 0.9851\n-55 0.08221 230.43 254.63 0.9837 0.08338 234.15 255.23 0.9918\n-60 0.08372 231.36 255.21 0.9900 0.08520 235.15 256.99 0.9947\n-70 0.08583 233.73 257.78 0.9922 0.08732 235.20 258.12 0.9951\n \n 734 Tables in SI Units\n\nTABLE A-9 (Continued)\n\nT \u00baC v u h s v u h \n m\u00b3/kg kJ/kg kJ/kg \t kJ/kg \u00b7 K\n\np = 5.5 bar = 0.55 MPa p = 6.0 bar = 0.60 MPa \n(t\u2090 = 3.08\u00baC)\n\nSat. 0.04271 227.53 512.02 0.926 0.03923 228.44 251.96 0.9186\n 10 0.04311 226.72 252.46 0.9278 0.04015 255.41 251.18 0.9299\n 15 0.04437 231.81 252.60 0.9411 0.04122 241.18 258.91 0.9431\n 20 0.04685 237.895 263.67 0.9660 0.04340 249.47 266.37 0.9783\n 25 0.04761 241.01 267.83 0.9770 0.04370 256.50 266.57 0.9805\n 30 0.04874 247.30 270.28 0.9912 0.04390 263.55 269.00 0.9893\n 35 0.04989 247.17 273.19 1.0034 0.04490 267.40 270.20 0.9810\n 40 0.05068 250.76 276.17 1.0148 0.04568 272.77 275.35 1.0048\n 45 0.05358 256.63 280.62 1.0281 0.04698 277.91 278.90 1.0506\n 50 0.05939 263.85 283.43 1.0378 0.04812 282.35 282.81 1.0619\n 55 0.06195 267.36 284.50 1.0450 0.04876 285.71 285.58 1.0737\n 60 0.06405 267.98 285.12 1.0510 0.04928 287.16 287.74 1.0865\n \n\np = 7.0 bar = 0.70 MPa p = 8.0 bar = 0.80 MPa \n(t\u2090 = 10.19\u00baC)\n\nSat. 0.03371 230.24 253.64 0.9117 0.02953 231.71 257.28 0.9066\n 10 0.03342 229.22 252.60 0.9063 0.02944 255.64 261.18 0.9093\n 15 0.03191 227.03 251.24 0.8990 0.02558 259.21 264.91 0.9102\n 20 0.03067 224.31 249.26 0.8898 0.02209 261.81 266.67 0.9111\n 25 0.02989 223.94 250.20 0.8961 0.01609 262.47 267.76 0.9264\n 30 0.02761 221.85 248.60 0.8843 0.01570 265.36 270.22 0.9343\n 35 0.02675 221.47 249.03 0.8847 0.01550 266.84 271.98 0.9352\n 40 0.02551 220.39 249.45 0.8743 0.01451 267.69 272.41 0.9415\n 45 0.02441 218.58 248.80 0.8607 0.01347 268.38 272.82 0.9473\n 50 0.02379 217.58 248.35 0.8550 0.01309 269.16 273.37 0.9544\n 55 0.02231 215.54 247.02 0.8397 0.01253 270.23 274.98 0.9656\n 60 0.02149 214.00 246.07 0.8229 0.01206 270.25 275.09 0.9746\n \n\np = 9.0 bar = 0.90 MPa p = 10.0 bar = 1.0 MPa \n(t\u2090 = 19.95\u00baC)\n\nSat. 0.02623 232.64 256.25 0.9001 0.02358 237.31 257.28 0.8952\n 20 0.02630 239.27 256.89 0.9013 0.02439 241.38 261.91 0.9139\n 30 0.02789 239.73 264.83 0.9289 0.02457 238.34 262.91 0.9139\n 40 0.02929 240.76 272.82 0.9494 0.02598 240.38 267.17 0.9179\n 50 0.03032 253.39 280.68 0.9756 0.02715 246.07 271.48 0.9722\n 60 0.03020 252.95 280.68 0.9750 0.02753 251.49 278.49 0.9660\n 70 0.03356 260.64 294.21 1.0282 0.02808 256.19 283.00 0.9725\n 80 0.03473 272.62 306.36 1.0480 0.02861 265.23 288.69 0.9780\n100 0.03776 285.39 319.53 1.0913 0.03372 273.45 291.66 0.9834\n110 0.03860 288.10 325.37 1.0918 0.03388 285.71 303.22 0.9938\n130 0.04103 306.36 343.21 1.1523 0.03672 305.76 313.05 1.0312\n140 0.04233 312.31 351.12 1.1799 0.03781 310.70 317.50 1.0388\n150 0.04342 320.21 359.29 1.1912 0.03889 319.74 319.74 1.0428\n TABLE A-9 (Continued)\n\nT °C \n ρ m/kg³ h kJ/kg k kJ/kg K\n u m³/kg \n ρ m/kg³ k kJ/kg h kJ/kg k kJ/kg K\n\np = 1.20 MPa\n\n - 0.02028 238.25 266.72 0.91416 0.01708 239.78 263.70 0.8900\n 50 0.02204 249.69 276.14 0.91413 0.01823 247.29 272.81 0.9186\n 60 0.02426 259.60 284.96 0.9666 0.01929 252.81 294.52 0.9432\n 70 0.02482 263.41 289.29 0.9097 0.02229 260.01 290.01 0.9702\n 80 0.02534 270.03 306.86 1.0193 0.02125 268.68 298.34 0.9492\n 90 0.02567 277.09 310.75 1.0363 0.02180 276.50 306.01 0.9775\n100 0.02736 284.30 316.84 1.0562 0.02280 284.52 314.00 1.0153\n110 0.02778 289.97 324.87 1.0794 0.02398 289.18 318.21 1.0681\n120 0.02844 298.57 332.85 1.1002 0.02478 296.92 326.43 1.1205\n130 0.02910 304.68 340.95 1.1205 0.02636 303.55 339.11 1.1292\n140 0.02983 314.55 347.37 1.1601 0.02664 311.11 340.62 1.1452\n150 0.03012 324.39 354.02 1.1793 0.02875 319.28 353.56 1.1624\n160 0.03206 334.57 365.84 1.1983 0.02842 328.32 372.64 1.1815\n170 0.03340 343.37 374.18 1.2172 0.02907 336.72 376.64 1.1996\n\np = 1.60 MPa\n\n - 0.01440 261.04 871.5 0.01265 236.88 261.61 0.8469\n 50 0.01634 269.18 892.4 0.01201 241.76 265.14 0.8602\n 60 0.01845 277.76 913.8 0.01199 246.84 267.80 0.8729\n 70 0.02049 285.78 935.4 0.01549 248.56 272.09 0.8919\n 80 0.02233 294.32 957.3 0.01565 256.94 278.45 0.9504\n 90 0.02262 300.66 973.1 0.01642 262.00 282.27 0.9613\n100 0.02551 314.69 992.8 0.01720 266.83 288.67 0.9817\n110 0.02684 322.73 1024.0 0.01834 274.18 294.90 1.0039\n120 0.02709 330.20 1050.0 0.01855 278.56 298.79 1.0189\n130 0.02869 338.71 1088.0 0.01900 286.67 306.27 1.0454\n140 0.03002 350.92 1120.0 0.01922 294.58 314.08 1.0730\n150 0.03141 363.97 1152.0 0.02003 302.11 318.97 1.0963\n160 0.03270 377.16 1182.0 0.02058 310.21 327.45 1.1198\n170 0.03416 390.00 1215.0 0.02101 318.76 334.12 1.1444\n\np = 1.80 MPa\n\n - 0.00927 261.61 872.1 0.02884 237.03 262.42 0.8342\n 50 0.01123 269.96 893.4 0.02810 242.14 265.12 0.8429\n 60 0.01454 278.23 915.2 0.02901 247.32 267.97 0.8519\n 70 0.01768 286.17 935.9 0.02705 250.07 272.87 0.8597\n 80 0.01958 293.62 956.8 0.02928 256.63 278.85 0.8891\n 90 0.02445 300.49 975.1 0.02949 262.98 283.45 0.9121\n100 0.02618 314.00 998.2 0.02947 269.05 288.05 0.9263\n110 0.02789 322.50 1022.0 0.03098 275.81 293.10 0.9560\n120 0.02963 330.29 1048.0 0.03132 281.87 298.29 0.9831\n130 0.03032 338.73 1076.6 0.03199 289.12 305.57 1.0110\n140 0.03147 350.36 1100.0 0.03210 298.08 313.84 1.0436\n150 0.03286 363.75 1130.0 0.03290 304.28 318.89 1.0772\n160 0.03433 377.61 1164.0 0.03309 310.30 327.72 1.1106\n170 0.03581 390.74 1200.0 0.03300 318.02 334.18 1.1439\n\np = 2.00 MPa\n\n - 0.00687 269.56 873.4 0.00097 240.27 261.99 0.8463\n 50 0.00812 278.11 895.7 0.00043 241.02 264.82 0.8484\n 60 0.01000 286.48 918.2 0.00100 250.70 274.03 0.8431\n 70 0.01159 294.13 939.4 0.00109 256.07 279.78 0.8553\n 80 0.01217 301.92 962.0 0.00115 265.30 285.42 0.8674\n 90 0.01329 310.47 985.2 0.00180 273.89 292.02 0.8922\n100 0.01402 318.60 1008.0 0.00235 280.69 299.10 0.9111\n110 0.01640 326.95 1034.0 0.00286 287.93 307.28 0.9338\n120 0.01790 335.21 1060.0 0.00312 294.87 315.32 0.9508\n130 0.01978 343.21 1088.0 0.00348 302.89 324.63 0.9749\n140 0.02084 352.26 1115.0 0.00405 309.69 331.49 0.9989\n150 0.02210 360.73 1140.0 0.00478 318.30 340.76 1.0278\n160 0.02350 369.32 1164.0 0.00516 326.62 347.64 1.0656\n170 0.02548 378.11 1190.0 0.00476 335.43 355.98 1.0901\n\np = 2.40 MPa\n\n - 0.00458 294.08 873.0 0.00070 240.27 261.99 0.8342\n 50 0.00695 302.10 898.4 0.00146 248.36 266.51 0.8429\n 60 0.00847 311.48 920.9 0.00211 256.08 272.05 0.8553\n 70 0.01119 319.20 943.5 0.00284 265.40 277.93 0.8674\n 80 0.01267 328.23 966.4 0.00282 274.27 285.42 0.8786\n 90 0.01352 338.07 988.8 0.00348 280.08 291.01 0.8940\n100 0.01400 346.01 1011.0 0.00403 288.17 299.93 0.9143\n110 0.01606 354.02 1033.0 0.00478 292.87 305.67 0.9324\n120 0.01708 362.09 1059.0 0.00510 307.23 322.30 0.9511\n130 0.01903 370.10 1088.0 0.00560 314.91 331.20 0.9723\n140 0.02026 378.27 1116.0 0.00599 320.21 338.83 0.9984\n150 0.02171 387.20 1140.0 0.00694 328.81 347.43 1.0241\n160 0.02308 396.10 1166.0 0.00786 336.82 353.42 1.0544\n170 0.02537 404.91 1191.0 0.00819 343.35 362.23 1.0860\n\n TABLE A-10\n\nProperties of Saturated Refrigerant 134a (Liquid-Vapor): Temperature Table\n\nTemp. °C\nPress. bar\n Sat. Liquid \n v m³×10³ n₄\n Sat. Vapor\n v m³/kg h kJ/kg k kJ/kg Temp.\n\n -36 0.5164 0.7055 0.3569 -0.004 204.45 0.00 222.88 228.88 0.0000 0.9500\n -26 0.6332 0.7113 0.2947 -0.464 206.73 220.67 228.67 0.0001 0.9560\n -20 0.7740 0.7172 0.2451 -0.478 209.01 0.952 218.77 227.90 0.0401 0.9486\n -15 0.7884 0.7243 0.2022 14.31 216.01 230.38 0.0600 0.9190 0.9300\n -5 0.8140 0.7331 0.1886 16.72 212.43 216.84 0.0699 0.9690 0.9199\n 0 0.8871 0.7482 0.1454 19.21 213.57 219.23 223.85 0.0714 0.9377\n 5 0.9155 0.7532 0.1362 21.81 215.60 220.24 226.88 0.0742 0.8890\n 10 0.9270 0.7615 0.1223 24.05 216.10 223.01 229.77 0.0771 0.8560\n 15 0.9390 0.7699 0.1111 25.57 217.02 224.35 231.73 0.0793 0.8310\n 20 0.9331 0.7715 0.1135 27.48 218.04 225.98 233.65 0.0809 0.8120\n 25 0.9495 0.7794 0.0927 29.99 219.08 227.00 235.55 0.0825 0.7889\n 30 0.9646 0.7919 0.0677 31.80 220.67 228.02 237.58 0.0859 0.7630\n 35 0.9788 0.8052 0.0438 33.33 221.79 229.23 238.90 0.0887 0.7460\n 40 0.9727 0.8119 0.0301 34.60 222.35 230.20 240.10 0.0904 0.7240\n 45 0.7317 0.4311 0.0322 36.50 223.62 231.59 242.19 0.0910 0.6971\n 50 1.0170 0.8644 0.0299 38.41 224.70 233.34 244.99 0.0937 0.6741\n 55 1.0121 0.8280 0.0282 39.40 226.81 234.02 246.31 0.0864 0.6475\n 60 1.0235 0.8889 0.0164 40.85 226.97 235.67 247.25 0.0888 0.6223\n 65 1.0297 0.9805 0.0261 42.88 227.51 236.43 248.32 0.0907 0.5981\n 70 1.0442 1.0516 0.0145 44.65 228.17 237.20 249.09 0.0893 0.5728\n80 1.0470 1.040 0.0147 46.90 229.00 238.03 250.50 0.0855 0.5551\n TABLE A-11\n\nProperties of Saturated Refrigerant 134a (Liquid-Vapor): Pressure Table\n\nPress. bar\nTemp. °C\n Sat. Liquid\n v m³/kg n₄ Sat. Vapor\n v m³/kg h kJ/kg h₄ kJ/kg Temp. °C\n\n0.6 -37.07 0.7097 0.3100 3.41 206.12 217.22 224.72 0.9520\n0.8 -31.21 0.7184 0.2366 10.47 209.40 211.92 224.36 0.9447\n1.0 -26.43 0.7258 0.1917 16.29 212.12 215.06 224.46 0.9335\n1.2 -23.03 0.7328 0.1641 22.54 214.50 216.42 225.08 0.9287\n1.4 -17.61 0.7347 0.1395 21.23 216.57 218.91 225.68 0.9175\n1.6 -16.82 0.7381 0.1343 22.46 218.62 220.73 227.02 0.9235\n2.0 -10.09 0.7332 0.0983 22.34 239.01 241.12 240.49 0.9369\n5.0 20.00 0.7362 0.0942 22.65 259.79 261.40 239.52 0.9119\n10.0 30.00 0.9549 0.0831 24.62 261.38 260.08 254.87 0.8718\n18.0 62.91 0.9631 0.0105 140.49 257.88 246.22 276.83 0.9945\n20.0 67.49 0.9878 0.0093 148.02 259.41 149.99 127.95 0.9171\n25.0 77.59 1.0562 0.0009 165.48 261.84 168.12 111.06 0.9094\n30.0 86.22 1.1416 0.0053 181.88 262.16 185.30 927.71 0.6165\n TABLE A-12 \n \n Properties of Superheated Refrigerant 134a Vapor\n \n T \n (°C) \n u \n m/k \n kJ/kg \n kJ/kg \n K \n v \n m/kg \n h \n kJ/kg \n kJ/kg \n K \n s \n kJ/kg \n K \n \n P = 0.6 bar = 0.06 MPa\n (Tref = -37.0°C) \n P = 1.0 bar = 0.10 MPa\n (Tref = 11.10°C)\n \n Sat. 0.31000 206.12 227.24 0.9520 0.19170 212.16 231.15 0.9395\n -20 0.33538 217.87 237.96 1.0620 0.19770 216.64 244.64 0.9062\n -10 0.34992 224.97 245.26 1.0371 0.20686 224.70 251.25 0.9268\n 0 0.36343 232.43 254.10 1.0675 0.21587 231.41 259.29 1.002\n 20 0.37869 239.69 263.15 1.093 0.22309 237.71 268.12 1.008\n 30 0.39279 247.32 270.89 1.116 0.22994 244 276 1.021\n 40 0.40628 255.86 278.09 1.139 0.23682 250.60 284 1.043\n 50 0.42061 263.10 285.41 1.164 0.24384 256.03 291.26 1.057\n 60 0.43501 270.16 292.79 1.188 0.25099 261.70 298.63 1.080\n 70 0.44960 277.12 300.05 1.210 0.25814 267.48 306.00 1.098\n 80 0.46431 283.96 308.20 1.230 0.26550 273.08 313.13 1.115\n 90 0.47925 290.73 316.30 1.250 0.27309 278.42 320.22 1.136\n 100 0.49420 297.37 324.46 1.271 0.28073 283.80 327.38 1.156\n 110 0.50937 303.89 332.56 1.292 0.28849 289.21 334.32 1.175\n 120 0.52455 310.25 340.35 1.313 0.29625 294.84 341.22 1.195\n TABLE A-12 (Continued)\n \n T \n (°C) \n u \n m/k \n kJ/kg \n kJ/kg \n K \n v \n m/kg \n h \n kJ/kg \n kJ/kg \n K \n s \n kJ/kg \n K \n \n P = 2 bar = 0.28 MPa \n (Tref = 13°C) \n P = 3 bar = 0.32 MPa \n (Tref = 4.8°C) \n Sat. 0.07193 236.26 246.52 0.9197 0.06322 228.43 248.66 0.9177\n \n 0.07040 237.27 247.64 0.9288 0.06576 234.61 265.65 0.9427\n \n 0.07163 238.45 248.53 0.9339 0.06901 242.87 264.95 0.9749\n \n 0.08026 251.83 275.12 1.049 0.07241 251.91 274.28 1.0022\n \n 0.08290 260.17 274.42 1.049 0.07518 259.21 283.67 1.067\n \n 0.08969 266.84 281.81 1.0789 0.07815 266.41 291.75 1.065\n \n 0.09179 271.23 305.32 1.079 0.08106 276.78 302.72 1.129\n \n 0.09641 275.96 312.95 1.1364 0.0892 286.56 312.41 1.1243\n \n 0.09699 280.39 322.01 1.1644 0.08674 294.40 322.2 1.125\n \n 0.10203 285.80 332.60 1.1989 0.08903 304.94 324.5 1.1403\n \n 0.10717 319.32 342.62 1.2193 0.02932 312.82 342.21 1.2076\n \n 0.10897 322.27 345.18 1.2461 0.05322 309.79 360 1.2345\n \n 120 1.02105 301.87 363.08 1.2727 0.09774 318.73 1.2611\n \n \n T = 40 bar = 0.40 MPa\n P = 0.50 bar = 0.50 MPa\n (Tref = 15.74°C)\n \n 0.05199 223.87 253.35 0.9182 0.04188 239.40 260.34 0.9264\n \n 0.06067 225.30 257.98 0.9132 0.05676 240.44 266.68 0.9319\n \n 0.06177 227.48 260.92 0.9406 0.06849 244.16 267.42 0.9358\n \n 0.06546 232.17 265.80 0.9528 0.06188 246.49 270.67 0.9487\n \n 0.06420 234.16 267.51 0.9624 0.07146 254.77 272.40 0.9669\n \n 0.07989 235.79 284 1.069 0.0875 268 287.63 1.002\n \n 0.00325 240.16 290.13 1.071 0.01206 241 292.70 1.003\n \n 0.00123 241.87 266 1.078 0.01456 282 260 0.952\n \n 0.00014 123 DATA 123 \n \n \n \n \n TABLE A-12 (Continued)\n \n T \n (°C) \n h \n m/kg \n kJ/kg \n kJ/kg \n K \n v \n m/kg \n h \n kJ/kg \n kJ/kg \n K \n s \n kJ/kg \n K \n \n P = 8.0 bar = 0.80 MPa \n (Tref = 31.3°C) \n P = 9.0 bar = 0.90 MPa \n \n Sat. 0.02547 243.78 263.25 0.9066 0.02225 245.38 266.18 0.9054\n \n 0.02691 251.73 273.65 0.9374 0.02325 245.76 265.57 0.9177\n \n 0.02684 261.64 284.92 0.9711 0.02272 269.79 271.41 0.9204\n \n 0.02929 271.40 294.98 1.03474 0.02136 267.45 261.45 1.014\n \n 0.03146 301.84 307.38 1.048 0.0134 307.71 307.38 0.9607\n \n 0.03329 299.37 321.48 1.077 0.02214 306.23 324.10 1.04\n \n 0.03634 307.50 327.64 1.096 0.02398 315.60 327.00 1.13\n \n 0.03995 320.57 332.70 1.113 0.02971 325.90 331.61 1.21\n \n 0.03598 337.10 373.80 1.130 0.03066 340.80 342.11 1.14\n \n 0.02000 326.72 353.05 1.160 0.03566 374 368 1.25\n \n 0.05243 352.87 389.01 1.294 0.03776 317.72 346 1.458\n \n 0.06156 370.20 398.45 1.291 0.05322 354 372 1.591\n \n 0.06674 391.18 418.39 1.318 0.06389 378 392.20 1.85\n TABLE A-13 Properties of Saturated Ammonia (Liquid–Vapor): Temperature Table\nSpecific Volume Internal Energy Enthalpy Entropy\nm³/kg kJ/kg kJ/kg K\nTemp.\n°C Press.\nbar × 10\n3 Sat. Sat.\nLiquid Vapor Sat.\nLiquid Sat.\nVapor Evap.\nhfg Sat.\nLiquid Sat.\nVapor Temp.\n°C\n 50 0.4086 1.4245 2.2665 43.94 1264.99 43.88 1416.20 1372.32 1.129 6.143\n -40 -0.5434 1.4367 2.0600 2.006 1271.19 21.95 1420.52 1380.07 0.503 5.40\n -30 0.7174 1.4391 1.5254 0.10 1277.20 0.00 1388.56 1386.56 0.000 5.9577\n -20 0.8580 1.4597 1.2757 17.47 1281.17 12.77 1377.11 1390.14 0.947 8.5819\n -10 1.0821 1.4703 1.0610 39.68 1286.41 36.65 1365.56 1400.81 1.205 9.1487\n 0 1.1590 1.4877 0.9643 43.30 1359.68 41.40 1385.05 1405.73 1.184 6.277\n 10 1.1591 1.4878 0.9803 28.72 1398.52 43.73 1406.65 1406.65 0.746 5.916\n 20 1.4465 1.4872 0.8066 61.65 1292.87 61.62 1437.66 1409.51 0.227 7.510\n 30 1.7390 1.4980 0.6780 79.27 1291.79 79.33 1415.08 1415.08 0.024 7.801\n 40 1.9191 1.5008 0.6238 98.48 1293.28 98.68 1329.10 1417.79 0.132 7.998\n 50 2.4645 1.5155 0.5750 113.32 1301.23 113.32 1425.05 1425.05 0.466 6.136\n 60 2.4653 1.5215 0.4985 115.37 1310.10 117.75 1309.86 1425.01 0.606 5.739\n 70 2.5661 1.5276 0.4616 139.11 1317.38 124.16 1310.23 1425.01 0.606 5.646\n 80 2.7240 1.5348 0.4292 164.94 1322.39 129.98 1261.43 1425.00 0.634 5.329\n 90 2.8804 1.5424 0.4005 191.80 1330.29 137.84 1205.31 1425.00 0.938 5.499\n 100 3.0419 1.5509 0.3740 219.40 1338.91 147.21 1157.06 1425.00 0.966 5.421\n TABLE A-14 Properties of Saturated Ammonia (Liquid–Vapor): Pressure Table\nSpecific Volume Internal Energy Enthalpy Entropy\nm³/kg kJ/kg kJ/kg K\nPress. Temp.\n°C Bar × 10\n3 Sat. Sat.\nLiquid Vapor Sat.\nLiquid Sat.\nVapor Evap.\nhfg Sat.\nLiquid Sat.\nVapor Press.\nbar\n 0.40 -50 -36 4.236 2.6795 45.52 1264.54 45.46 1417.18 1371.72 1.199 6.618\n 0.60 -50 -36 4.330 2.1752 45.52 1266.41 28.66 1406.73 1377.06 0.124 6.026\n 0.80 -50 -36 4.442 1.8345 123.71 -14.42 1397.17 1384.37 -0.026 6.076\n 1.00 -50 -36 4.454 1.5844 127.31 -14.42 1393.57 1384.25 0.045 6.079\n 1.20 -50 -36 4.466 1.4592 127.31 -3.94 1390.95 1387.20 0.120 5.878\n 1.50 0 -36 4.572 1.4528 52.84 -14.14 1388.66 1390.29 0.052 5.699\n 1.80 0 0 4.586 1.4818 52.12 1385.09 1407.91 4.168 4.870\n 2.00 0 50 4.654 1.48600 30.84 1406.68 1408.14 3.929 7.027\n TABLE A-15 Properties of Superheated Ammonia Vapor\nT u u u h h s\n \n°C m³/kg kJ/kg kJ/kg.K m³/kg kJ/kg kJ/kg K\n p = 0.04 MPa t = -36°C\n 2.6795 1264.54 1371.72 6.1618 1.8345 1273.27 1383.34 6.0186\n -10 1.8344 1325.85 1425.31 6.1615 1261.32 1324.43 1450.54 6.0467\n -25 1.4692 1287.24 1232.51 6.0667 1.8640 1349.52 1420.77 6.0599\n -30 1.2952 1290.16 1265.47 5.8538 6.1850 1379.12 1494.28 5.9795\n -35 1.8926 1391.31 1358.82 5.9818 1.4986 1359.96 1516.47 5.1734\n -40 2.9800 1383.88 1390.70 6.4885 0.1425 1423.81 1570.75 5.0140\n 744\nTables in SI Units\n\nTABLE A-15 (Continued)\n\nT v u h s v u h s \n°C m³/kg kJ/kg kJ/kg·K kJ/kg·K\n\np = 2.5 bar or 0.25 MPa (Tcr = 43.67°C)\nSat. 0.48213 1306.49 1425.03 5.1900 0.40607 1309.65 1431.47 5.4544\n0 0.49081 1312.71 1447.10 5.5344 - - - - \n...\n200 0.65772 1691.51 1920.65 6.7460 - - - - \n\np = 3.0 bar or 0.30 MPa (Tcr = 94°C)\n...\n200 0.66872 1408.70 1460.00 5.8998\n\np = 3.5 bar or 0.35 MPa (Tcr = 36°C)\n...\n200 0.65112 1408.70 1460.00 5.8998 745\nTables in SI Units\n\nTABLE A-15 (Continued)\n\nT v u h s v u h s \n°C m³/kg kJ/kg kJ/kg·K kJ/kg·K\n\np = 5.5 bar or 0.55 MPa (Tcr = 67.9°C)\nSat. 0.23861 1230.06 1448.80 5.2430 0.21038 1328.97 1451.12 5.2122\n20 0.22273 1239.88 1457.63 5.2731 0.21115 1326.47 1453.05 5.3145\n...\n200 0.25717 1687.02 1919.41 6.3988\n\np = 6.0 bar or 0.60 MPa (Tcr = 97.2°C)\n...\n200 0.32871 1687.02 1919.41 6.3988 746\nTables in SI Units\n\nTABLE A-15 (Continued)\n\nT v u h s v u h s \n°C m³/kg kJ/kg kJ/kg·K kJ/kg·K\n\np = 12.0 bar or 1.20 MPa (Tcr = 30.94°C)\nSat. 0.10751 1337.52 1466.53 4.9625 0.09231 1349.15 1468.79 4.9050\n60 0.11287 1397.75 1503.53 5.9433 0.10423 1349.74 1497.69 5.1375\n...\n200 0.12284 1841.03 2105.50 2.2665 TABLE A-16 Properties of Saturated Propane (Liquid-Vapor): Temperature Table\nSpecific Volume Internal Energy Enthalpy Entropy\nTemp. Press. Sat. Liquid Vapour Liquid Evap. Vapour Liquid Vapour Sat. Liquid Temp.\n\"C\" bar m^3/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg\n-100 0.08288 1.553 11.27 2.319 -1284.480 352.0 0.634 2.140 319.0\n-90 0.04624 1.578 5.345 -107.8 207.1 471.4 36.5 -0.519 2.005 -90.0\n-80 0.13010 1.608 -87.0 339.9 870. 462.4 37.5 -0.408 1.986 -80.0\n-70 0.24434 1.633 1.551 -59.0 430. 57.-341.03 -0.198 1.929 -70.0\n-60 0.2461 1.631 0.921 -44.4 0.454 433.9 -0.199 -180.0 60.0\n-50 0.7061 1.694 0.573 -27.2 424. 411.2 -0.855 1.85 60.0\n-40 1.11 1.728 0.379 22.0 396. 406.9 -0.119 1.731 70.0\n-30 1.677 1.763 0.258 22.6 391.6 422.1 43.6 0.906 1.791 30.0\n-20 2.441 1.802 0.181 46.2 391.6 12.3 439. 466.8 1.069 20.0\n-10 3.453 1.844 0.190 43.2 350.30 458. 456.8 1.191 1.747 10.0\n 0 4.411 1.887 0.096 21.82 366.8 91.3 19.10 57.5 1.358 0.851 0.95 TABLE A-17 Properties of Saturated Propane (Liquid-Vapor): Pressure Table\nSpecific Volume Internal Energy Enthalpy Entropy\nPress. Temp. Saturated Liquid Vapour Liquid Evap. Vapour Liquid Vapour Temp. Press.\nbar 'C' m3/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg K\n0.05 -93.28 1.570 6.752 -1146 474.4 359.8 0.506 2.061 0.10\n-90 -83.87 1.594 3.542 -951. 335.4 465.9 370.0 -0.450 2.57 0.10\n-60 -69.5 1.634 1.513 -360.0 649. 452.7 387.8 -0.297 1.927 0.25\n-50 -69.0 1.672 0.796 -951 376.0 400.2 402.0 0.13 1.75 1.00\n-40 0.01 1.698 0.547 65.7 572.5 410.0 430.2 2.06 18.01 0.50 TABLE A-18 Properties of Superheated Propane\nT v u h v h\n\'C\' m3/kg kJ/kg kJ/kg kJ/kg kJ/kg\n0 1.752 3260.39 2.081 3.542 367.3 370.8 2.011\n-100 6.807 3294.36 363.8 2.103\n-80 7.258 3361.3 2.166 3.617 339.5 375.5 2.037\n-70 7.390 350.8 4.897 0.831\n-60 8.397 373.3 4.259 4.53\n-50 8.397 373.3 4.53 6.08 8.09 0.8 TABLE A-18 (Continued)\nT v u h j v h \n°C m³/kg kJ/kg kJ/kg·K m³/kg kJ/kg kJ/kg·K\nP = 4.0 bar = 0.4 MPa (T\\_r = -54.46°C)\n Sat. 0.1137 418.0 463.5 1.751 0.09172 425.7 471.6 1.743\n 0.1169 426.1 472.1 1.786 0.09577 438.4 486.3 1.796\n 10 0.1227 441.4 490.3 1.848 0.1005 454.1 504.3 1.858\n 20 0.1283 456.6 507.9 1.909 0.105 471.3 522.3 1.919\n 30 0.1332 472.2 525.7 1.969 0.1103 486.1 540.9 1.979\n 40 0.1392 488.1 543.8 2.027 0.1169 502.7 560.5 2.041\n 50 0.1444 504.4 562.2 2.085 0.1236 519.2 580.1 2.105\n 60 0.1498 518.1 581.0 2.143 0.1303 536.4 599.7 2.191\n 70 0.1508 528.4 601.1 2.199 0.1286 554.9 619.5 2.278\n 80 0.1601 540.6 622.5 2.255 0.1361 573.7 639.7 2.367\n 90 0.1622 553.1 643.1 2.311 0.1438 593.0 659.9 2.458\n 100 0.1733 573.9 663.9 2.366 0.1518 611.7 680.3 2.550\n 110 0.1744 586.6 684.9 2.421 0.1392 630.7 700.7 2.636\n\nP = 6.0 bar = 0.6 MPa (T\\_r = -79.3°C)\n Sat. 0.7658 472.3 478.3 1.737 0.0698 470.4 515.0 1.733\n 10 0.7786 469.3 476.1 1.751 0.0687 472.0 516.6 1.761\n 20 0.8074 455.0 460.6 1.815 0.0684 474.0 518.7 1.789\n 30 0.8303 446.8 451.1 1.848 0.0756 475.5 520.1 1.797\n 40 0.8623 436.7 441.4 1.871 0.0738 479.1 523.2 1.806\n 50 0.8853 424.8 430.1 1.887 0.0802 480.5 523.3 1.814\n 60 0.9017 417.9 421.6 1.901 0.0785 482.9 524.5 1.822\n 70 0.9178 416.2 419.2 1.914 0.0758 484.8 525.8 1.830\n 80 0.9207 410.5 414.5 1.924 0.0738 486.7 526.1 1.839\n 90 0.9229 401.2 405.4 1.937 0.0721 489.0 529.5 1.846\n 100 0.9361 397.5 403.8 1.956 0.0716 491.6 532.2 1.856\n 110 0.9549 393.7 399.3 1.962 0.0708 495.5 533.2 1.862\n\nP = 7.0 bar = 0.7 MPa (T\\_r = -136.1°C)\n Sat. 0.9700 388.7 398.7 2.003 0.0687 487.1 530.2 1.875\n 10 0.9828 377.8 393.2 2.033 0.0666 483.9 526.9 1.868\n 20 0.9912 368.2 388.8 2.056 0.0652 479.0 527.0 1.870\n 30 1.0021 358.1 383.2 2.078 0.0648 474.0 526.9 1.875\n 40 1.0067 351.4 376.5 2.097 0.0646 468.7 524.9 1.894\n 50 1.0150 345.0 371.1 2.115 0.0645 463.9 525.2 1.914\n 60 1.0165 339.5 365.6 2.135 0.0642 459.0 522.1 1.917\n TABLE A-18 (Continued)\nT v u h j v h \n°C m³/kg kJ/kg kJ/kg·K m³/kg kJ/kg kJ/kg·K\nP = 10.0 bar = 1.0 MPa (T\\_r = 26-95°C)\n Sat. 0.040606 451.8 497.9 1.723 0.03810 459.1 504.8 1.718\n 40 0.04976 457.1 501.1 1.744 0.03957 469.4 516.8 1.757\n 50 0.04890 478.4 524.6 1.816 0.04036 484.8 529.1 1.787\n 60 0.05240 482.5 545.9 1.874 0.04204 487.3 538.2 1.824\n 70 0.05650 512.2 565.2 1.936 0.04436 505.8 559.3 1.889\n 80 0.05752 528.8 585.7 1.974 0.04667 524.4 580.3 1.951\n 90 0.05818 539.6 602.7 2.006 0.04846 543.5 584.1 1.972\n 100 0.06226 546.1 619.0 2.038 0.05075 562.3 592.0 2.007\n 110 0.06374 556.8 635.0 2.069 0.05243 584.1 610.0 2.057\n 120 0.06441 569.6 650.1 2.102 0.05412 606.5 623.0 2.106\n 130 0.06512 579.5 668.2 2.134 0.05570 627.6 635.5 2.147\n 140 0.06638 594.1 683.0 2.167 0.05748 634.8 646.1 2.191\n 150 0.06825 609.7 699.1 2.200 0.05894 646.7 656.1 2.191\n 160 0.07020 619.3 710.7 2.234 0.05935 660.5 667.4 2.235\n 170 0.07260 629.0 722.6 2.267 0.06020 678.5 674.0 2.284\n 180 0.07378 639.8 735.7 2.301 0.06103 694.9 684.1 2.298\n 190 0.07492 650.9 745.3 2.331 0.06225 708.3 693.0 2.312\n 200 0.07573 663.8 751.0 2.364 0.06327 724.3 702.1 2.321\n\nP = 12.0 bar = 1.2 MPa (T\\_r = 34.39°C)\n Sat. 0.06136 457.7 498.8 1.802 0.06144 462.1 509.3 1.822\n 20 0.06289 455.0 497.3 1.806 0.06194 474.5 520.7 1.842\n 30 0.06361 459.4 499.9 1.810 0.06202 485.3 523.0 1.854\n 40 0.06411 466.3 508.9 1.820 0.06245 494.9 535.0 1.869\n 50 0.06443 473.5 515.7 1.825 0.06289 501.2 540.5 1.870\n TABLE A-18 (Continued)\nT v u h j v h \n°C m³/kg kJ/kg kJ/kg·K m³/kg kJ/kg kJ/kg·K\nP = 18.0 bar = 1.8 MPa (T\\_r = 52.30°C)\n Sat. 0.04241 474.9 518.5 1.705 0.02157 478.7 521.8 1.700\n 20 0.06020 494.1 531.4 1.763 0.02216 484.8 529.1 1.722\n 30 0.07278 514.6 580.4 1.834 0.02426 505.4 534.5 1.797\n 40 0.08020 532.9 590.3 1.845 0.02558 509.8 538.0 1.804\n 50 0.08226 543.8 602.8 1.877 0.02792 511.9 545.6 1.817\n 60 0.08540 556.2 610.0 1.898 0.02918 516.8 552.2 1.832\n 70 0.09030 570.7 617.2 1.912 0.03100 520.1 562.8 1.850\n 80 0.09215 586.1 624.0 1.929 0.03242 522.5 572.4 1.871\n 90 0.09246 590.8 629.4 1.936 0.03455 523.5 576.1 1.892\n 100 0.09500 593.5 632.2 1.940 0.03589 523.4 579.2 1.910\n 110 0.09656 596.1 633.7 1.952 0.03792 524.8 583.1 1.926\n 120 0.09787 597.8 635.4 1.965 0.04041 525.2 585.2 1.935\n 130 0.09911 598.5 637.7 1.971 0.04267 526.3 588.7 1.959\n 140 0.09946 599.1 638.7 1.983 0.04449 527.1 590.7 1.968\n 150 0.09972 599.6 639.1 1.993 0.04610 528.3 592.4 1.975\n 160 0.10000 600.1 640.4 2.004 0.04772 529.8 593.9 1.984\n 170 0.10031 600.8 641.7 2.015 0.04797 530.8 594.8 1.993\n 180 0.10062 601.5 643.0 2.026 0.04812 531.8 596.2 2.000\n
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TABLE A-2 Properties of Saturated Water (Liquid–Vapor): Temperature Table\n\nSpecific Volume Internal Energy Enthalpy Entropy\nm³/kg kJ/kg kJ/kg kJ/kg·K\nTemp. °C Press.\nbar Sat. Liquid v_f × 10⁻³ Sat. Vapor v_g × 10³ Sat. Liquid h_f Sat. Vapor h_g Evap. h_fg Sat. Liquid s_f Sat. Vapor s_g\n, Press. bar\n0 0.00611 1.0002 206.136 0.00 2375.3 0.01 2501.3 2507.8 0.000 15.632 0.01\n1 0.00813 1.0001 157.232 16.77 2380.6 2419.1 2508.7 0.061 0.054 16.567 0.01\n2 0.00872 1.0001 147.210 20.09 2382.3 2489.1 2516.0 0.076 15.403 16.405 0.01\n//... (more data) TABLE A-2 (Continued)\n\nSpecific Volume Internal Energy Enthalpy Entropy\nm³/kg kJ/kg kJ/kg kJ/kg·K\nTemp. °C Press.\nbar Sat. Liquid v_f × 10⁻³ Sat. Vapor v_g × 10³ Sat. Liquid h_f Sat. Vapor h_g Evap. h_fg Sat. Liquid s_f Sat. Vapor s_g\n, Press. bar\n150 0.56 1.00060 25.216 14.667 242.3 146.68 2563.0 2568.1 1.953 8.059 150\n155 0.597 1.00063 23.940 150.50 242.4 150.86 2416.2 2467.6 1.518 8.536 160\n160 0.612 1.0060 22.114 158.89 241.6 2586.0 2587.9 2.031 8.354 160\n//... (more data) TABLE A-3 Properties of Saturated Water (Liquid–Vapor): Pressure Table\n\nSpecific Volume Internal Energy Enthalpy Entropy\nm³/kg kJ/kg kJ/kg kJ/kg·K\nPress.\nbar Temp. °C Sat. Liquid v_f × 10⁻³ Sat. Vapor v_g × 10³ Sat. Liquid h_f Sat. Vapor h_g Evap. h_fg Sat. Liquid s_f Sat. Vapor s_g Press.\nbar\n0.04 26.96 1.0064 34.800 121.45 2415.2 121.46 2544.2 0.226 4.8746 0.04\n0.06 36.16 1.0064 34.739 2452.0 151.63 2419.5 2564.8 0.521 8.3040 0.06\n0.08 45.11 1.0084 18.103 173.87 2423.2 173.83 2403.1 0.576 8.227 0.08\n0.10 60.00 1.0120 22.674 201.24 2327.6 199.46 2388.7 0.625 8.028 0.10\n0.20 60.10 1.0223 2.529 289.20 289.20 2363.1 2623.3 0.915 7.968 0.20\n0.40 81.31 1.0301 3.402 340.84 2487.9 239.6 2634.9 1.032 7.919 0.40\n0.60 91.71 1.0330 4.732 395.75 2489.60 2653.9 2635.15 1.1453 7.520 0.60\n0.80 100.00 1.0340 2.365 375.24 2441.2 2527.00 2763.9 1.199 7.427 0.80\n1.00 120.0 1.0380 0.679 482.56 2484.9 2576.0 2675.3 1.300 6.952 1.00\n1.50 160.0 1.0480 1.069 663.86 2510.1 2520.6 2698.0 1.503 6.247 1.50\n2.00 180.0 1.0680 0.867 861.82 2489.0 2655.3 2670.6 1.684 5.432 2.00\n//... (more data) TABLE A-3 (Continued)\n\nSpecific Volume Internal Energy Enthalpy Entropy\n m3/kg kJ/kg kJ/kg kJ/kg K\nPress. Sat. Liquid Sat. Vapor Sat. Liquid Sat. Vapor Sat. Liquid Sat. Vapor Sat. Liquid\n bar °C vL x 10^3 vG hL hG Evap hg sL sG\n120 324.8 1.5267 0.04246 1473.20 2517.71 1491.13 1193.6 2684.9 4.9462 5.9423 120.\n130 330.9 1.5671 0.01278 1511.41 2496.1 1531.5 1130.7 2662.2 3.5606 5.4323 130.\n140 336.2 1.6017 0.01149 1548.46 2476.8 1571.1 1065.6 2637.6 3.6322 5.3177 140.\n150 342.2 1.6581 0.01034 1585.8 2455.6 1588.9 1006.0 2610.3 3.6878 5.2086 150.\n160 347.4 1.7017 0.00930 1622.27 2431.47 1601.1 994.0 2580.0 3.7461 5.1458 160.\n170 353.1 1.7702 0.00864 1660.20 2390.5 1690.3 856.9 2547.2 3.9127 5.1177 170.\n180 359.7 1.8937 0.00780 1699.1 2344.9 1785.7 801.4 2510.3 4.0919 5.0585 180.\n190 366.5 1.9243 0.00657 1739.9 2328.1 1776.6 788.0 2464.1 3.9884 5.0228 190.\n200 368.5 2.0365 0.00584 1785.6 2309.6 1826.3 758.1 2409.9 4.8199 4.9269 200.\n220 374.1 3.155 0.003155 2029.6 2099.3 0 2099.3 4.4298 4.4298 220.9 TABLE A-6 Properties of Superheated Water Vapor\n T v u kJ/kg kJ/kg kJ/kg K\n °C m3/kg m2/kg m2/kg m2/kg m3/kg\np = 0.06 bar = 0.006 MPa\n (Tav = 36.16°C) \np = 0.35 bar = 0.035 MPa\n (Tav = 72.67°C)\n Sat. 23.739 2425.2 2567.4 8.3304 4.526 2473.01 2631.14 2657.5 7.564 4.411 5.784\n80 27.112 2487.5 2560.1 5.5804 6.135 2465.7 2535.7 2675.7 7.512 5.753 5.614\n120 30.200 2547.1 2726.0 8.7840 5.504 2596.3 2653.5 2725.6 7.967 5.415 6.118\n140 32.001 2602.7 2796.8 9.8999 5.566 2607.2 2785.9 2810.6 9.715 5.655 6.358\n200 36.363 2651.4 2877.9 9.1923 5.505 2608.2 2781.1 2877.1 8.920 6.827 6.634\n240 39.362 2712.1 2957.8 9.2982 6.758 2720.2 2857.0 2878.4 8.932 7.198 6.557\n280 43.197 2780.2 3035.0 8.3126 2.546 2774.6 2896.0 2580.1 8.315 5.591 7.167\n320 36.753 2841.7 3115.0 8.5044 3.754 2813.8 2943.1 2706.3 8.839 6.075 7.238\n440 44.321 2975.9 3485.8 9.9140 3.673 2916.9 3036.3 3183.5 9.762 6.746 7.997\n500 29.853 3481.0 3488.5 1.0198 3.243 3042.1 3142.5 3287.5 7.717 5.738 7.892 TABLE A-4 (Continued)\n\n T v u kJ/kg kJ/kg kJ/kg K\n °C m3/kg m2/kg m2/kg m2/kg m3/kg\np = 5.0 bar = 0.50 MPa\n (Tav = 151.86°C) \np = 7.0 bar = 0.70 MPa\n (Tav = 164.97°C)\n Sat. 0.3749 2681.2 2748.7 6.8213 0.2729 2572.5 2761.3 12.821 7.088 0.8066\n120 0.4240 2607.9 2816.0 6.9665 0.2487 2599.3 2799.7 14.825 8.780 6.911\n260 0.4250 2643.0 2830.1 7.7400 0.2957 2850.1 2890.6 13.657 7.137 0.721\n360 0.3891 2721.0 2902.1 7.8233 0.2932 2762.3 2921.9 12.482 5.579 6.877\n400 0.3066 2957.3 3269.9 7.4651 0.2030 2915.3 3255.5 7.152 6.129 7.209\n420 0.3357 3036.5 3330.3 7.7046 0.2160 3012.6 3475.5 9.335 6.376 7.596\n540 0.3710 3114.3 3378.1 7.8298 0.1878 3181.9 3560.9 7.699 7.347 7.648\n600 0.4325 3256.4 3506.0 8.4082 0.2159 3700.0 3722.1 8.089 5.596 7.892 TABLE A-6 (Continued)\n\nT \u00b0C kJ/kg kJ/kg m\u00b3/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg\n \n h \n \n \n\np = 40 bar - 40.0 MPa\n (T\u00b0 = 250.4\u00b0C)\nSat. 0.04976 2602.3 2801.4 6.0701 0.03244 2589.77 2754.3 5.8902\n \n320 0.06789 2674.01 3014.5 6.2586 0.03717 2647.16 2657.3 6.1436\n360 0.07891 2865.4 3117.2 6.6215 0.04311 2833.20 2924.1 6.4654\n400 0.09269 3173.4 3210.8 6.7082 0.04739 2951.67 2952.2 6.5076\n440 0.10841 3263.1… TABLE A-4 (Continued)\n\nT \u00b0C v \n m\u00b3/kg kJ/kg kJ/kg\u00b7K \n h \n kJ/kg kJ/kg kJ/kg\u00b7K\n p = 160 bar - 16.0 MPa \n (T\u00b0 = 347.44\u00b0C)\nSat. 0.00931 243.17 2580.6 5.2455 0.00749 2437.43 2509.1 5.1044 \n360 0.01105 259.90 2711.5 5.4641 0.00809 2419.84 2564.5 5.1922 \n400 0.01426 279.84 2947.67 5.8175 0.01190 2672.87 2887.5 5.6887 \n440 0.01625 283.94 3103.67 6.0429 0.01414 2862.8 3062.1 5.9438 \n480 0.01842 293.71 3234.4 6.2215 0.01596 2918.5 3202.6 6.1345 \n520 0.02013 303.11 3353.3 6.3752 0.01757 3011.5 3378.6 6.2960 \n600 0.02216 317.18 3464.5 6.6132 0.02048 3109.7 3555.6 6.4966 \n640 0.02407 324.82 3678.0 6.7980 0.02361 3227.3 3666.3 6.7474 \n700 0.02674 340.6 3823.9 6.9224 0.02362 3396.3 3821.5 6.8580 \n740 0.02806 348.67 3935.7 7.0511 0.02438 3478.0 3925.0 6.9625 \n\np = 200 bar - 20.0 MPa\np = 240 bar - 240 MPa\n\n0.00323 2469.20 4.9269\n0.00400 2679.63 5.5014\n0.00445 3000.2 5.6439\n0.00400 2912.6 5.8660\n0.00400 3186.39 6.1913\n0.00400 3450.52 6.2770\n\np = 280 bar - 28.0 MPa\np = 320 bar - 32.0 MPa\n... TABLE A-5 Properties of Compressed Liquid Water\n\nT \u00b0C \n\nv x 10\u00b3 u \n m\u00b3/kg kJ/kg kJ/kg kJ/kg\u00b7K\n \n \n kJ/kg kJ/kg kJ/kg\u00b7K\n p = 25 bar - 2.5 MPa \n (T\u00b0 = 223.99\u00b0C)\n20 1.0005 83.80 86.30 0.2961 0.9995 83.65 86.85 0.2965 \n40 1.0067 167.25 169.77 0.5715 1.0055 166.10 171.67 0.3286 \n80 1.0242 414.84 420.83 1.0305 1.0410 371.42 332.88 1.0300 \n140 1.0748 587.92 590.52 1.0706 1.0737 614.30 645.21 1.1140 \n180 1.1261 761.16 763.97 1.1375 1.1240 759.63 765.25 1.1341 \n...\n\np = 200 bar - 20.0 MPa\np = 100 bar - 10.0 MPa\n... 732 Tables in SI Units\n\nTABLE A-9 Properties of Superheated Refrigerant 22 Vapor\n\nT \u00baC v u h s v u h \n m\u00b3/kg kJ/kg kJ/kg \t kJ/kg \u00b7 K\n\np = 0.4 bar = 0.04 MPa p = 0.6 bar = 0.06 MPa \n(t\u2090 = -58.86\u00baC)\n\nSat. 0.50509 204.13 224.36 1.0512 0.34665 207.14 227.73 1.0294\n-55 0.51158 205.92 225.63 1.0612 0.34895 208.20 228.74 1.0392\n-50 0.52787 208.26 229.38 1.0741 0.34895 208.20 228.74 1.0392\n-45 0.54087 210.63 232.14 1.0868 0.35747 210.20 231.14 1.0459\n-40 0.55238 213.03 233.13 1.0993 0.36694 211.30 232.14 1.0513\n-35 0.56626 215.48 235.01 1.1117 0.37347 215.06 236.14 1.0562\n-30 0.57576 218.25 238.09 1.1239 0.37721 217.57 237.72 1.0862\n-25 0.59002 220.43 241.06 1.1348 0.39215 220.87 241.38 1.0821\n-20 0.60246 222.88 244.95 1.1479 0.39942 224.18 246.15 1.0921\n-15 0.61485 225.39 247.50 1.1597 0.40230 227.34 249.82 1.0979\n-10 0.62679 227.53 250.91 1.1714 0.40627 229.59 252.81 1.1042\n -5 0.63953 229.60 253.98 1.1812 0.40894 231.64 254.79 1.1152\n 0 0.65113 231.13 251.94 1.1944 0.43261 232.17 256.53 1.1255\n-\n\np = 1.5 bar = 0.15 MPa p = 2.0 bar = 0.20 MPa \n(t\u2090 = -32.0\u00baC)\n\nSat. 0.14721 214.77 238.86 0.9830 0.11322 217.42 239.88 0.9691\n-30 0.14872 215.85 236.16 0.9833 0.11285 217.51 238.00 0.9650\n-25 0.15228 218.45 241.30 1.0011 0.11242 217.50 239.01 0.9660\n-20 0.15882 221.07 244.15 1.0177 0.11179 218.79 240.56 0.9674\n-10 0.16920 225.36 247.16 1.0502 0.12067 225.49 245.39 0.9857\n 0 0.16987 227.20 250.61 1.0621 0.12614 229.63 248.52 0.9883\n 15 0.18153 239.91 263.93 1.0834 0.13397 236.81 257.15 0.9630\n 25 0.18693 245.49 273.53 1.1193 0.13912 240.29 255.69 0.9641\n 733 Tables in SI Units\n\nTABLE A-9 (Continued)\n\nT \u00baC v u h s v u h \n m\u00b3/kg kJ/kg kJ/kg \t kJ/kg \u00b7 K\n\np = 2.5 bar = 0.25 MPa p = 3.0 bar = 0.30 MPa \n(t\u2090 = -14.66\u00baC)\n\nSat. 0.09097 219.15 242.29 0.9566 0.07651 221.34 244.29 0.9502\n 0 0.09303 222.30 245.29 0.9730 0.07823 223.39 247.46 0.9623\n -5 0.09521 225.47 246.81 0.9813 0.08025 226.89 250.86 0.9751\n-10 0.09761 227.13 249.57 0.9860 0.08339 229.05 253.70 0.9790\n-15 0.09941 227.32 250.85 0.9860 0.08389 229.37 254.09 0.9794\n-20 0.10183 229.23 251.62 0.9931 0.08415 229.73 255.82 0.9831\n-25 0.10325 231.14 253.06 1.0074 0.08572 231.87 258.01 0.9847\n-30 0.10492 232.67 254.63 1.0146 0.08740 233.07 260.17 0.9850\n-35 0.10601 234.39 256.14 1.0198 0.08875 234.76 261.32 0.9874\n-40 0.10626 235.31 257.64 1.0207 0.08918 235.18 262.30 0.9890\n-45 0.10767 236.87 259.66 1.0243 0.08973 236.70 263.37 0.9915\n-50 0.10966 238.94 261.71 1.0390 0.09079 238.79 264.98 0.9947\n-55 0.11068 239.76 262.16 1.0451 0.09101 239.90 265.05 0.9933\n-60 0.11203 243.22 268.12 1.0696 0.09155 242.20 267.59 1.0043\n-70 0.11329 247.22 270.95 1.0756 0.09214 243.17 269.25 1.0056\n-80 0.11502 249.15 275.33 1.0867 0.09346 246.12 270.79 1.0076\n-90 0.11631 250.05 276.27 1.0917 0.09387 247.51 273.06 1.0101\n-100 0.11711 250.75 278.59 1.0952 0.09404 248.56 274.75 1.0115\n \n\np = 3.5 bar = 0.35 MPa p = 4.0 bar = 0.40 MPa \n(t\u2090 = -6.56\u00baC)\n\nSat. 0.06512 222.88 246.00 0.9431 0.05812 224.24 247.48 0.9370\n-10 0.06701 224.47 247.74 0.9516 0.06000 226.16 248.00 0.9411\n-15 0.06807 225.07 248.71 0.9589 0.06029 226.93 248.36 0.9434\n-20 0.06951 225.74 249.07 0.9622 0.06213 227.80 248.78 0.9455\n-25 0.07081 226.19 249.89 0.9667 0.06292 228.30 249.23 0.9482\n-30 0.07291 226.63 250.59 0.9711 0.06512 229.66 249.54 0.9548\n-35 0.07521 228.12 251.03 0.9757 0.06764 230.00 251.22 0.9615\n-40 0.07701 228.97 252.11 0.9781 0.07082 230.11 252.62 0.9685\n-45 0.07882 229.55 252.80 0.9797 0.07819 231.02 253.17 0.9792\n-50 0.08072 230.38 253.52 0.9798 0.07992 231.78 254.70 0.9851\n-55 0.08221 230.43 254.63 0.9837 0.08338 234.15 255.23 0.9918\n-60 0.08372 231.36 255.21 0.9900 0.08520 235.15 256.99 0.9947\n-70 0.08583 233.73 257.78 0.9922 0.08732 235.20 258.12 0.9951\n \n 734 Tables in SI Units\n\nTABLE A-9 (Continued)\n\nT \u00baC v u h s v u h \n m\u00b3/kg kJ/kg kJ/kg \t kJ/kg \u00b7 K\n\np = 5.5 bar = 0.55 MPa p = 6.0 bar = 0.60 MPa \n(t\u2090 = 3.08\u00baC)\n\nSat. 0.04271 227.53 512.02 0.926 0.03923 228.44 251.96 0.9186\n 10 0.04311 226.72 252.46 0.9278 0.04015 255.41 251.18 0.9299\n 15 0.04437 231.81 252.60 0.9411 0.04122 241.18 258.91 0.9431\n 20 0.04685 237.895 263.67 0.9660 0.04340 249.47 266.37 0.9783\n 25 0.04761 241.01 267.83 0.9770 0.04370 256.50 266.57 0.9805\n 30 0.04874 247.30 270.28 0.9912 0.04390 263.55 269.00 0.9893\n 35 0.04989 247.17 273.19 1.0034 0.04490 267.40 270.20 0.9810\n 40 0.05068 250.76 276.17 1.0148 0.04568 272.77 275.35 1.0048\n 45 0.05358 256.63 280.62 1.0281 0.04698 277.91 278.90 1.0506\n 50 0.05939 263.85 283.43 1.0378 0.04812 282.35 282.81 1.0619\n 55 0.06195 267.36 284.50 1.0450 0.04876 285.71 285.58 1.0737\n 60 0.06405 267.98 285.12 1.0510 0.04928 287.16 287.74 1.0865\n \n\np = 7.0 bar = 0.70 MPa p = 8.0 bar = 0.80 MPa \n(t\u2090 = 10.19\u00baC)\n\nSat. 0.03371 230.24 253.64 0.9117 0.02953 231.71 257.28 0.9066\n 10 0.03342 229.22 252.60 0.9063 0.02944 255.64 261.18 0.9093\n 15 0.03191 227.03 251.24 0.8990 0.02558 259.21 264.91 0.9102\n 20 0.03067 224.31 249.26 0.8898 0.02209 261.81 266.67 0.9111\n 25 0.02989 223.94 250.20 0.8961 0.01609 262.47 267.76 0.9264\n 30 0.02761 221.85 248.60 0.8843 0.01570 265.36 270.22 0.9343\n 35 0.02675 221.47 249.03 0.8847 0.01550 266.84 271.98 0.9352\n 40 0.02551 220.39 249.45 0.8743 0.01451 267.69 272.41 0.9415\n 45 0.02441 218.58 248.80 0.8607 0.01347 268.38 272.82 0.9473\n 50 0.02379 217.58 248.35 0.8550 0.01309 269.16 273.37 0.9544\n 55 0.02231 215.54 247.02 0.8397 0.01253 270.23 274.98 0.9656\n 60 0.02149 214.00 246.07 0.8229 0.01206 270.25 275.09 0.9746\n \n\np = 9.0 bar = 0.90 MPa p = 10.0 bar = 1.0 MPa \n(t\u2090 = 19.95\u00baC)\n\nSat. 0.02623 232.64 256.25 0.9001 0.02358 237.31 257.28 0.8952\n 20 0.02630 239.27 256.89 0.9013 0.02439 241.38 261.91 0.9139\n 30 0.02789 239.73 264.83 0.9289 0.02457 238.34 262.91 0.9139\n 40 0.02929 240.76 272.82 0.9494 0.02598 240.38 267.17 0.9179\n 50 0.03032 253.39 280.68 0.9756 0.02715 246.07 271.48 0.9722\n 60 0.03020 252.95 280.68 0.9750 0.02753 251.49 278.49 0.9660\n 70 0.03356 260.64 294.21 1.0282 0.02808 256.19 283.00 0.9725\n 80 0.03473 272.62 306.36 1.0480 0.02861 265.23 288.69 0.9780\n100 0.03776 285.39 319.53 1.0913 0.03372 273.45 291.66 0.9834\n110 0.03860 288.10 325.37 1.0918 0.03388 285.71 303.22 0.9938\n130 0.04103 306.36 343.21 1.1523 0.03672 305.76 313.05 1.0312\n140 0.04233 312.31 351.12 1.1799 0.03781 310.70 317.50 1.0388\n150 0.04342 320.21 359.29 1.1912 0.03889 319.74 319.74 1.0428\n TABLE A-9 (Continued)\n\nT °C \n ρ m/kg³ h kJ/kg k kJ/kg K\n u m³/kg \n ρ m/kg³ k kJ/kg h kJ/kg k kJ/kg K\n\np = 1.20 MPa\n\n - 0.02028 238.25 266.72 0.91416 0.01708 239.78 263.70 0.8900\n 50 0.02204 249.69 276.14 0.91413 0.01823 247.29 272.81 0.9186\n 60 0.02426 259.60 284.96 0.9666 0.01929 252.81 294.52 0.9432\n 70 0.02482 263.41 289.29 0.9097 0.02229 260.01 290.01 0.9702\n 80 0.02534 270.03 306.86 1.0193 0.02125 268.68 298.34 0.9492\n 90 0.02567 277.09 310.75 1.0363 0.02180 276.50 306.01 0.9775\n100 0.02736 284.30 316.84 1.0562 0.02280 284.52 314.00 1.0153\n110 0.02778 289.97 324.87 1.0794 0.02398 289.18 318.21 1.0681\n120 0.02844 298.57 332.85 1.1002 0.02478 296.92 326.43 1.1205\n130 0.02910 304.68 340.95 1.1205 0.02636 303.55 339.11 1.1292\n140 0.02983 314.55 347.37 1.1601 0.02664 311.11 340.62 1.1452\n150 0.03012 324.39 354.02 1.1793 0.02875 319.28 353.56 1.1624\n160 0.03206 334.57 365.84 1.1983 0.02842 328.32 372.64 1.1815\n170 0.03340 343.37 374.18 1.2172 0.02907 336.72 376.64 1.1996\n\np = 1.60 MPa\n\n - 0.01440 261.04 871.5 0.01265 236.88 261.61 0.8469\n 50 0.01634 269.18 892.4 0.01201 241.76 265.14 0.8602\n 60 0.01845 277.76 913.8 0.01199 246.84 267.80 0.8729\n 70 0.02049 285.78 935.4 0.01549 248.56 272.09 0.8919\n 80 0.02233 294.32 957.3 0.01565 256.94 278.45 0.9504\n 90 0.02262 300.66 973.1 0.01642 262.00 282.27 0.9613\n100 0.02551 314.69 992.8 0.01720 266.83 288.67 0.9817\n110 0.02684 322.73 1024.0 0.01834 274.18 294.90 1.0039\n120 0.02709 330.20 1050.0 0.01855 278.56 298.79 1.0189\n130 0.02869 338.71 1088.0 0.01900 286.67 306.27 1.0454\n140 0.03002 350.92 1120.0 0.01922 294.58 314.08 1.0730\n150 0.03141 363.97 1152.0 0.02003 302.11 318.97 1.0963\n160 0.03270 377.16 1182.0 0.02058 310.21 327.45 1.1198\n170 0.03416 390.00 1215.0 0.02101 318.76 334.12 1.1444\n\np = 1.80 MPa\n\n - 0.00927 261.61 872.1 0.02884 237.03 262.42 0.8342\n 50 0.01123 269.96 893.4 0.02810 242.14 265.12 0.8429\n 60 0.01454 278.23 915.2 0.02901 247.32 267.97 0.8519\n 70 0.01768 286.17 935.9 0.02705 250.07 272.87 0.8597\n 80 0.01958 293.62 956.8 0.02928 256.63 278.85 0.8891\n 90 0.02445 300.49 975.1 0.02949 262.98 283.45 0.9121\n100 0.02618 314.00 998.2 0.02947 269.05 288.05 0.9263\n110 0.02789 322.50 1022.0 0.03098 275.81 293.10 0.9560\n120 0.02963 330.29 1048.0 0.03132 281.87 298.29 0.9831\n130 0.03032 338.73 1076.6 0.03199 289.12 305.57 1.0110\n140 0.03147 350.36 1100.0 0.03210 298.08 313.84 1.0436\n150 0.03286 363.75 1130.0 0.03290 304.28 318.89 1.0772\n160 0.03433 377.61 1164.0 0.03309 310.30 327.72 1.1106\n170 0.03581 390.74 1200.0 0.03300 318.02 334.18 1.1439\n\np = 2.00 MPa\n\n - 0.00687 269.56 873.4 0.00097 240.27 261.99 0.8463\n 50 0.00812 278.11 895.7 0.00043 241.02 264.82 0.8484\n 60 0.01000 286.48 918.2 0.00100 250.70 274.03 0.8431\n 70 0.01159 294.13 939.4 0.00109 256.07 279.78 0.8553\n 80 0.01217 301.92 962.0 0.00115 265.30 285.42 0.8674\n 90 0.01329 310.47 985.2 0.00180 273.89 292.02 0.8922\n100 0.01402 318.60 1008.0 0.00235 280.69 299.10 0.9111\n110 0.01640 326.95 1034.0 0.00286 287.93 307.28 0.9338\n120 0.01790 335.21 1060.0 0.00312 294.87 315.32 0.9508\n130 0.01978 343.21 1088.0 0.00348 302.89 324.63 0.9749\n140 0.02084 352.26 1115.0 0.00405 309.69 331.49 0.9989\n150 0.02210 360.73 1140.0 0.00478 318.30 340.76 1.0278\n160 0.02350 369.32 1164.0 0.00516 326.62 347.64 1.0656\n170 0.02548 378.11 1190.0 0.00476 335.43 355.98 1.0901\n\np = 2.40 MPa\n\n - 0.00458 294.08 873.0 0.00070 240.27 261.99 0.8342\n 50 0.00695 302.10 898.4 0.00146 248.36 266.51 0.8429\n 60 0.00847 311.48 920.9 0.00211 256.08 272.05 0.8553\n 70 0.01119 319.20 943.5 0.00284 265.40 277.93 0.8674\n 80 0.01267 328.23 966.4 0.00282 274.27 285.42 0.8786\n 90 0.01352 338.07 988.8 0.00348 280.08 291.01 0.8940\n100 0.01400 346.01 1011.0 0.00403 288.17 299.93 0.9143\n110 0.01606 354.02 1033.0 0.00478 292.87 305.67 0.9324\n120 0.01708 362.09 1059.0 0.00510 307.23 322.30 0.9511\n130 0.01903 370.10 1088.0 0.00560 314.91 331.20 0.9723\n140 0.02026 378.27 1116.0 0.00599 320.21 338.83 0.9984\n150 0.02171 387.20 1140.0 0.00694 328.81 347.43 1.0241\n160 0.02308 396.10 1166.0 0.00786 336.82 353.42 1.0544\n170 0.02537 404.91 1191.0 0.00819 343.35 362.23 1.0860\n\n TABLE A-10\n\nProperties of Saturated Refrigerant 134a (Liquid-Vapor): Temperature Table\n\nTemp. °C\nPress. bar\n Sat. Liquid \n v m³×10³ n₄\n Sat. Vapor\n v m³/kg h kJ/kg k kJ/kg Temp.\n\n -36 0.5164 0.7055 0.3569 -0.004 204.45 0.00 222.88 228.88 0.0000 0.9500\n -26 0.6332 0.7113 0.2947 -0.464 206.73 220.67 228.67 0.0001 0.9560\n -20 0.7740 0.7172 0.2451 -0.478 209.01 0.952 218.77 227.90 0.0401 0.9486\n -15 0.7884 0.7243 0.2022 14.31 216.01 230.38 0.0600 0.9190 0.9300\n -5 0.8140 0.7331 0.1886 16.72 212.43 216.84 0.0699 0.9690 0.9199\n 0 0.8871 0.7482 0.1454 19.21 213.57 219.23 223.85 0.0714 0.9377\n 5 0.9155 0.7532 0.1362 21.81 215.60 220.24 226.88 0.0742 0.8890\n 10 0.9270 0.7615 0.1223 24.05 216.10 223.01 229.77 0.0771 0.8560\n 15 0.9390 0.7699 0.1111 25.57 217.02 224.35 231.73 0.0793 0.8310\n 20 0.9331 0.7715 0.1135 27.48 218.04 225.98 233.65 0.0809 0.8120\n 25 0.9495 0.7794 0.0927 29.99 219.08 227.00 235.55 0.0825 0.7889\n 30 0.9646 0.7919 0.0677 31.80 220.67 228.02 237.58 0.0859 0.7630\n 35 0.9788 0.8052 0.0438 33.33 221.79 229.23 238.90 0.0887 0.7460\n 40 0.9727 0.8119 0.0301 34.60 222.35 230.20 240.10 0.0904 0.7240\n 45 0.7317 0.4311 0.0322 36.50 223.62 231.59 242.19 0.0910 0.6971\n 50 1.0170 0.8644 0.0299 38.41 224.70 233.34 244.99 0.0937 0.6741\n 55 1.0121 0.8280 0.0282 39.40 226.81 234.02 246.31 0.0864 0.6475\n 60 1.0235 0.8889 0.0164 40.85 226.97 235.67 247.25 0.0888 0.6223\n 65 1.0297 0.9805 0.0261 42.88 227.51 236.43 248.32 0.0907 0.5981\n 70 1.0442 1.0516 0.0145 44.65 228.17 237.20 249.09 0.0893 0.5728\n80 1.0470 1.040 0.0147 46.90 229.00 238.03 250.50 0.0855 0.5551\n TABLE A-11\n\nProperties of Saturated Refrigerant 134a (Liquid-Vapor): Pressure Table\n\nPress. bar\nTemp. °C\n Sat. Liquid\n v m³/kg n₄ Sat. Vapor\n v m³/kg h kJ/kg h₄ kJ/kg Temp. °C\n\n0.6 -37.07 0.7097 0.3100 3.41 206.12 217.22 224.72 0.9520\n0.8 -31.21 0.7184 0.2366 10.47 209.40 211.92 224.36 0.9447\n1.0 -26.43 0.7258 0.1917 16.29 212.12 215.06 224.46 0.9335\n1.2 -23.03 0.7328 0.1641 22.54 214.50 216.42 225.08 0.9287\n1.4 -17.61 0.7347 0.1395 21.23 216.57 218.91 225.68 0.9175\n1.6 -16.82 0.7381 0.1343 22.46 218.62 220.73 227.02 0.9235\n2.0 -10.09 0.7332 0.0983 22.34 239.01 241.12 240.49 0.9369\n5.0 20.00 0.7362 0.0942 22.65 259.79 261.40 239.52 0.9119\n10.0 30.00 0.9549 0.0831 24.62 261.38 260.08 254.87 0.8718\n18.0 62.91 0.9631 0.0105 140.49 257.88 246.22 276.83 0.9945\n20.0 67.49 0.9878 0.0093 148.02 259.41 149.99 127.95 0.9171\n25.0 77.59 1.0562 0.0009 165.48 261.84 168.12 111.06 0.9094\n30.0 86.22 1.1416 0.0053 181.88 262.16 185.30 927.71 0.6165\n TABLE A-12 \n \n Properties of Superheated Refrigerant 134a Vapor\n \n T \n (°C) \n u \n m/k \n kJ/kg \n kJ/kg \n K \n v \n m/kg \n h \n kJ/kg \n kJ/kg \n K \n s \n kJ/kg \n K \n \n P = 0.6 bar = 0.06 MPa\n (Tref = -37.0°C) \n P = 1.0 bar = 0.10 MPa\n (Tref = 11.10°C)\n \n Sat. 0.31000 206.12 227.24 0.9520 0.19170 212.16 231.15 0.9395\n -20 0.33538 217.87 237.96 1.0620 0.19770 216.64 244.64 0.9062\n -10 0.34992 224.97 245.26 1.0371 0.20686 224.70 251.25 0.9268\n 0 0.36343 232.43 254.10 1.0675 0.21587 231.41 259.29 1.002\n 20 0.37869 239.69 263.15 1.093 0.22309 237.71 268.12 1.008\n 30 0.39279 247.32 270.89 1.116 0.22994 244 276 1.021\n 40 0.40628 255.86 278.09 1.139 0.23682 250.60 284 1.043\n 50 0.42061 263.10 285.41 1.164 0.24384 256.03 291.26 1.057\n 60 0.43501 270.16 292.79 1.188 0.25099 261.70 298.63 1.080\n 70 0.44960 277.12 300.05 1.210 0.25814 267.48 306.00 1.098\n 80 0.46431 283.96 308.20 1.230 0.26550 273.08 313.13 1.115\n 90 0.47925 290.73 316.30 1.250 0.27309 278.42 320.22 1.136\n 100 0.49420 297.37 324.46 1.271 0.28073 283.80 327.38 1.156\n 110 0.50937 303.89 332.56 1.292 0.28849 289.21 334.32 1.175\n 120 0.52455 310.25 340.35 1.313 0.29625 294.84 341.22 1.195\n TABLE A-12 (Continued)\n \n T \n (°C) \n u \n m/k \n kJ/kg \n kJ/kg \n K \n v \n m/kg \n h \n kJ/kg \n kJ/kg \n K \n s \n kJ/kg \n K \n \n P = 2 bar = 0.28 MPa \n (Tref = 13°C) \n P = 3 bar = 0.32 MPa \n (Tref = 4.8°C) \n Sat. 0.07193 236.26 246.52 0.9197 0.06322 228.43 248.66 0.9177\n \n 0.07040 237.27 247.64 0.9288 0.06576 234.61 265.65 0.9427\n \n 0.07163 238.45 248.53 0.9339 0.06901 242.87 264.95 0.9749\n \n 0.08026 251.83 275.12 1.049 0.07241 251.91 274.28 1.0022\n \n 0.08290 260.17 274.42 1.049 0.07518 259.21 283.67 1.067\n \n 0.08969 266.84 281.81 1.0789 0.07815 266.41 291.75 1.065\n \n 0.09179 271.23 305.32 1.079 0.08106 276.78 302.72 1.129\n \n 0.09641 275.96 312.95 1.1364 0.0892 286.56 312.41 1.1243\n \n 0.09699 280.39 322.01 1.1644 0.08674 294.40 322.2 1.125\n \n 0.10203 285.80 332.60 1.1989 0.08903 304.94 324.5 1.1403\n \n 0.10717 319.32 342.62 1.2193 0.02932 312.82 342.21 1.2076\n \n 0.10897 322.27 345.18 1.2461 0.05322 309.79 360 1.2345\n \n 120 1.02105 301.87 363.08 1.2727 0.09774 318.73 1.2611\n \n \n T = 40 bar = 0.40 MPa\n P = 0.50 bar = 0.50 MPa\n (Tref = 15.74°C)\n \n 0.05199 223.87 253.35 0.9182 0.04188 239.40 260.34 0.9264\n \n 0.06067 225.30 257.98 0.9132 0.05676 240.44 266.68 0.9319\n \n 0.06177 227.48 260.92 0.9406 0.06849 244.16 267.42 0.9358\n \n 0.06546 232.17 265.80 0.9528 0.06188 246.49 270.67 0.9487\n \n 0.06420 234.16 267.51 0.9624 0.07146 254.77 272.40 0.9669\n \n 0.07989 235.79 284 1.069 0.0875 268 287.63 1.002\n \n 0.00325 240.16 290.13 1.071 0.01206 241 292.70 1.003\n \n 0.00123 241.87 266 1.078 0.01456 282 260 0.952\n \n 0.00014 123 DATA 123 \n \n \n \n \n TABLE A-12 (Continued)\n \n T \n (°C) \n h \n m/kg \n kJ/kg \n kJ/kg \n K \n v \n m/kg \n h \n kJ/kg \n kJ/kg \n K \n s \n kJ/kg \n K \n \n P = 8.0 bar = 0.80 MPa \n (Tref = 31.3°C) \n P = 9.0 bar = 0.90 MPa \n \n Sat. 0.02547 243.78 263.25 0.9066 0.02225 245.38 266.18 0.9054\n \n 0.02691 251.73 273.65 0.9374 0.02325 245.76 265.57 0.9177\n \n 0.02684 261.64 284.92 0.9711 0.02272 269.79 271.41 0.9204\n \n 0.02929 271.40 294.98 1.03474 0.02136 267.45 261.45 1.014\n \n 0.03146 301.84 307.38 1.048 0.0134 307.71 307.38 0.9607\n \n 0.03329 299.37 321.48 1.077 0.02214 306.23 324.10 1.04\n \n 0.03634 307.50 327.64 1.096 0.02398 315.60 327.00 1.13\n \n 0.03995 320.57 332.70 1.113 0.02971 325.90 331.61 1.21\n \n 0.03598 337.10 373.80 1.130 0.03066 340.80 342.11 1.14\n \n 0.02000 326.72 353.05 1.160 0.03566 374 368 1.25\n \n 0.05243 352.87 389.01 1.294 0.03776 317.72 346 1.458\n \n 0.06156 370.20 398.45 1.291 0.05322 354 372 1.591\n \n 0.06674 391.18 418.39 1.318 0.06389 378 392.20 1.85\n TABLE A-13 Properties of Saturated Ammonia (Liquid–Vapor): Temperature Table\nSpecific Volume Internal Energy Enthalpy Entropy\nm³/kg kJ/kg kJ/kg K\nTemp.\n°C Press.\nbar × 10\n3 Sat. Sat.\nLiquid Vapor Sat.\nLiquid Sat.\nVapor Evap.\nhfg Sat.\nLiquid Sat.\nVapor Temp.\n°C\n 50 0.4086 1.4245 2.2665 43.94 1264.99 43.88 1416.20 1372.32 1.129 6.143\n -40 -0.5434 1.4367 2.0600 2.006 1271.19 21.95 1420.52 1380.07 0.503 5.40\n -30 0.7174 1.4391 1.5254 0.10 1277.20 0.00 1388.56 1386.56 0.000 5.9577\n -20 0.8580 1.4597 1.2757 17.47 1281.17 12.77 1377.11 1390.14 0.947 8.5819\n -10 1.0821 1.4703 1.0610 39.68 1286.41 36.65 1365.56 1400.81 1.205 9.1487\n 0 1.1590 1.4877 0.9643 43.30 1359.68 41.40 1385.05 1405.73 1.184 6.277\n 10 1.1591 1.4878 0.9803 28.72 1398.52 43.73 1406.65 1406.65 0.746 5.916\n 20 1.4465 1.4872 0.8066 61.65 1292.87 61.62 1437.66 1409.51 0.227 7.510\n 30 1.7390 1.4980 0.6780 79.27 1291.79 79.33 1415.08 1415.08 0.024 7.801\n 40 1.9191 1.5008 0.6238 98.48 1293.28 98.68 1329.10 1417.79 0.132 7.998\n 50 2.4645 1.5155 0.5750 113.32 1301.23 113.32 1425.05 1425.05 0.466 6.136\n 60 2.4653 1.5215 0.4985 115.37 1310.10 117.75 1309.86 1425.01 0.606 5.739\n 70 2.5661 1.5276 0.4616 139.11 1317.38 124.16 1310.23 1425.01 0.606 5.646\n 80 2.7240 1.5348 0.4292 164.94 1322.39 129.98 1261.43 1425.00 0.634 5.329\n 90 2.8804 1.5424 0.4005 191.80 1330.29 137.84 1205.31 1425.00 0.938 5.499\n 100 3.0419 1.5509 0.3740 219.40 1338.91 147.21 1157.06 1425.00 0.966 5.421\n TABLE A-14 Properties of Saturated Ammonia (Liquid–Vapor): Pressure Table\nSpecific Volume Internal Energy Enthalpy Entropy\nm³/kg kJ/kg kJ/kg K\nPress. Temp.\n°C Bar × 10\n3 Sat. Sat.\nLiquid Vapor Sat.\nLiquid Sat.\nVapor Evap.\nhfg Sat.\nLiquid Sat.\nVapor Press.\nbar\n 0.40 -50 -36 4.236 2.6795 45.52 1264.54 45.46 1417.18 1371.72 1.199 6.618\n 0.60 -50 -36 4.330 2.1752 45.52 1266.41 28.66 1406.73 1377.06 0.124 6.026\n 0.80 -50 -36 4.442 1.8345 123.71 -14.42 1397.17 1384.37 -0.026 6.076\n 1.00 -50 -36 4.454 1.5844 127.31 -14.42 1393.57 1384.25 0.045 6.079\n 1.20 -50 -36 4.466 1.4592 127.31 -3.94 1390.95 1387.20 0.120 5.878\n 1.50 0 -36 4.572 1.4528 52.84 -14.14 1388.66 1390.29 0.052 5.699\n 1.80 0 0 4.586 1.4818 52.12 1385.09 1407.91 4.168 4.870\n 2.00 0 50 4.654 1.48600 30.84 1406.68 1408.14 3.929 7.027\n TABLE A-15 Properties of Superheated Ammonia Vapor\nT u u u h h s\n \n°C m³/kg kJ/kg kJ/kg.K m³/kg kJ/kg kJ/kg K\n p = 0.04 MPa t = -36°C\n 2.6795 1264.54 1371.72 6.1618 1.8345 1273.27 1383.34 6.0186\n -10 1.8344 1325.85 1425.31 6.1615 1261.32 1324.43 1450.54 6.0467\n -25 1.4692 1287.24 1232.51 6.0667 1.8640 1349.52 1420.77 6.0599\n -30 1.2952 1290.16 1265.47 5.8538 6.1850 1379.12 1494.28 5.9795\n -35 1.8926 1391.31 1358.82 5.9818 1.4986 1359.96 1516.47 5.1734\n -40 2.9800 1383.88 1390.70 6.4885 0.1425 1423.81 1570.75 5.0140\n 744\nTables in SI Units\n\nTABLE A-15 (Continued)\n\nT v u h s v u h s \n°C m³/kg kJ/kg kJ/kg·K kJ/kg·K\n\np = 2.5 bar or 0.25 MPa (Tcr = 43.67°C)\nSat. 0.48213 1306.49 1425.03 5.1900 0.40607 1309.65 1431.47 5.4544\n0 0.49081 1312.71 1447.10 5.5344 - - - - \n...\n200 0.65772 1691.51 1920.65 6.7460 - - - - \n\np = 3.0 bar or 0.30 MPa (Tcr = 94°C)\n...\n200 0.66872 1408.70 1460.00 5.8998\n\np = 3.5 bar or 0.35 MPa (Tcr = 36°C)\n...\n200 0.65112 1408.70 1460.00 5.8998 745\nTables in SI Units\n\nTABLE A-15 (Continued)\n\nT v u h s v u h s \n°C m³/kg kJ/kg kJ/kg·K kJ/kg·K\n\np = 5.5 bar or 0.55 MPa (Tcr = 67.9°C)\nSat. 0.23861 1230.06 1448.80 5.2430 0.21038 1328.97 1451.12 5.2122\n20 0.22273 1239.88 1457.63 5.2731 0.21115 1326.47 1453.05 5.3145\n...\n200 0.25717 1687.02 1919.41 6.3988\n\np = 6.0 bar or 0.60 MPa (Tcr = 97.2°C)\n...\n200 0.32871 1687.02 1919.41 6.3988 746\nTables in SI Units\n\nTABLE A-15 (Continued)\n\nT v u h s v u h s \n°C m³/kg kJ/kg kJ/kg·K kJ/kg·K\n\np = 12.0 bar or 1.20 MPa (Tcr = 30.94°C)\nSat. 0.10751 1337.52 1466.53 4.9625 0.09231 1349.15 1468.79 4.9050\n60 0.11287 1397.75 1503.53 5.9433 0.10423 1349.74 1497.69 5.1375\n...\n200 0.12284 1841.03 2105.50 2.2665 TABLE A-16 Properties of Saturated Propane (Liquid-Vapor): Temperature Table\nSpecific Volume Internal Energy Enthalpy Entropy\nTemp. Press. Sat. Liquid Vapour Liquid Evap. Vapour Liquid Vapour Sat. Liquid Temp.\n\"C\" bar m^3/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg\n-100 0.08288 1.553 11.27 2.319 -1284.480 352.0 0.634 2.140 319.0\n-90 0.04624 1.578 5.345 -107.8 207.1 471.4 36.5 -0.519 2.005 -90.0\n-80 0.13010 1.608 -87.0 339.9 870. 462.4 37.5 -0.408 1.986 -80.0\n-70 0.24434 1.633 1.551 -59.0 430. 57.-341.03 -0.198 1.929 -70.0\n-60 0.2461 1.631 0.921 -44.4 0.454 433.9 -0.199 -180.0 60.0\n-50 0.7061 1.694 0.573 -27.2 424. 411.2 -0.855 1.85 60.0\n-40 1.11 1.728 0.379 22.0 396. 406.9 -0.119 1.731 70.0\n-30 1.677 1.763 0.258 22.6 391.6 422.1 43.6 0.906 1.791 30.0\n-20 2.441 1.802 0.181 46.2 391.6 12.3 439. 466.8 1.069 20.0\n-10 3.453 1.844 0.190 43.2 350.30 458. 456.8 1.191 1.747 10.0\n 0 4.411 1.887 0.096 21.82 366.8 91.3 19.10 57.5 1.358 0.851 0.95 TABLE A-17 Properties of Saturated Propane (Liquid-Vapor): Pressure Table\nSpecific Volume Internal Energy Enthalpy Entropy\nPress. Temp. Saturated Liquid Vapour Liquid Evap. Vapour Liquid Vapour Temp. Press.\nbar 'C' m3/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg kJ/kg K\n0.05 -93.28 1.570 6.752 -1146 474.4 359.8 0.506 2.061 0.10\n-90 -83.87 1.594 3.542 -951. 335.4 465.9 370.0 -0.450 2.57 0.10\n-60 -69.5 1.634 1.513 -360.0 649. 452.7 387.8 -0.297 1.927 0.25\n-50 -69.0 1.672 0.796 -951 376.0 400.2 402.0 0.13 1.75 1.00\n-40 0.01 1.698 0.547 65.7 572.5 410.0 430.2 2.06 18.01 0.50 TABLE A-18 Properties of Superheated Propane\nT v u h v h\n\'C\' m3/kg kJ/kg kJ/kg kJ/kg kJ/kg\n0 1.752 3260.39 2.081 3.542 367.3 370.8 2.011\n-100 6.807 3294.36 363.8 2.103\n-80 7.258 3361.3 2.166 3.617 339.5 375.5 2.037\n-70 7.390 350.8 4.897 0.831\n-60 8.397 373.3 4.259 4.53\n-50 8.397 373.3 4.53 6.08 8.09 0.8 TABLE A-18 (Continued)\nT v u h j v h \n°C m³/kg kJ/kg kJ/kg·K m³/kg kJ/kg kJ/kg·K\nP = 4.0 bar = 0.4 MPa (T\\_r = -54.46°C)\n Sat. 0.1137 418.0 463.5 1.751 0.09172 425.7 471.6 1.743\n 0.1169 426.1 472.1 1.786 0.09577 438.4 486.3 1.796\n 10 0.1227 441.4 490.3 1.848 0.1005 454.1 504.3 1.858\n 20 0.1283 456.6 507.9 1.909 0.105 471.3 522.3 1.919\n 30 0.1332 472.2 525.7 1.969 0.1103 486.1 540.9 1.979\n 40 0.1392 488.1 543.8 2.027 0.1169 502.7 560.5 2.041\n 50 0.1444 504.4 562.2 2.085 0.1236 519.2 580.1 2.105\n 60 0.1498 518.1 581.0 2.143 0.1303 536.4 599.7 2.191\n 70 0.1508 528.4 601.1 2.199 0.1286 554.9 619.5 2.278\n 80 0.1601 540.6 622.5 2.255 0.1361 573.7 639.7 2.367\n 90 0.1622 553.1 643.1 2.311 0.1438 593.0 659.9 2.458\n 100 0.1733 573.9 663.9 2.366 0.1518 611.7 680.3 2.550\n 110 0.1744 586.6 684.9 2.421 0.1392 630.7 700.7 2.636\n\nP = 6.0 bar = 0.6 MPa (T\\_r = -79.3°C)\n Sat. 0.7658 472.3 478.3 1.737 0.0698 470.4 515.0 1.733\n 10 0.7786 469.3 476.1 1.751 0.0687 472.0 516.6 1.761\n 20 0.8074 455.0 460.6 1.815 0.0684 474.0 518.7 1.789\n 30 0.8303 446.8 451.1 1.848 0.0756 475.5 520.1 1.797\n 40 0.8623 436.7 441.4 1.871 0.0738 479.1 523.2 1.806\n 50 0.8853 424.8 430.1 1.887 0.0802 480.5 523.3 1.814\n 60 0.9017 417.9 421.6 1.901 0.0785 482.9 524.5 1.822\n 70 0.9178 416.2 419.2 1.914 0.0758 484.8 525.8 1.830\n 80 0.9207 410.5 414.5 1.924 0.0738 486.7 526.1 1.839\n 90 0.9229 401.2 405.4 1.937 0.0721 489.0 529.5 1.846\n 100 0.9361 397.5 403.8 1.956 0.0716 491.6 532.2 1.856\n 110 0.9549 393.7 399.3 1.962 0.0708 495.5 533.2 1.862\n\nP = 7.0 bar = 0.7 MPa (T\\_r = -136.1°C)\n Sat. 0.9700 388.7 398.7 2.003 0.0687 487.1 530.2 1.875\n 10 0.9828 377.8 393.2 2.033 0.0666 483.9 526.9 1.868\n 20 0.9912 368.2 388.8 2.056 0.0652 479.0 527.0 1.870\n 30 1.0021 358.1 383.2 2.078 0.0648 474.0 526.9 1.875\n 40 1.0067 351.4 376.5 2.097 0.0646 468.7 524.9 1.894\n 50 1.0150 345.0 371.1 2.115 0.0645 463.9 525.2 1.914\n 60 1.0165 339.5 365.6 2.135 0.0642 459.0 522.1 1.917\n TABLE A-18 (Continued)\nT v u h j v h \n°C m³/kg kJ/kg kJ/kg·K m³/kg kJ/kg kJ/kg·K\nP = 10.0 bar = 1.0 MPa (T\\_r = 26-95°C)\n Sat. 0.040606 451.8 497.9 1.723 0.03810 459.1 504.8 1.718\n 40 0.04976 457.1 501.1 1.744 0.03957 469.4 516.8 1.757\n 50 0.04890 478.4 524.6 1.816 0.04036 484.8 529.1 1.787\n 60 0.05240 482.5 545.9 1.874 0.04204 487.3 538.2 1.824\n 70 0.05650 512.2 565.2 1.936 0.04436 505.8 559.3 1.889\n 80 0.05752 528.8 585.7 1.974 0.04667 524.4 580.3 1.951\n 90 0.05818 539.6 602.7 2.006 0.04846 543.5 584.1 1.972\n 100 0.06226 546.1 619.0 2.038 0.05075 562.3 592.0 2.007\n 110 0.06374 556.8 635.0 2.069 0.05243 584.1 610.0 2.057\n 120 0.06441 569.6 650.1 2.102 0.05412 606.5 623.0 2.106\n 130 0.06512 579.5 668.2 2.134 0.05570 627.6 635.5 2.147\n 140 0.06638 594.1 683.0 2.167 0.05748 634.8 646.1 2.191\n 150 0.06825 609.7 699.1 2.200 0.05894 646.7 656.1 2.191\n 160 0.07020 619.3 710.7 2.234 0.05935 660.5 667.4 2.235\n 170 0.07260 629.0 722.6 2.267 0.06020 678.5 674.0 2.284\n 180 0.07378 639.8 735.7 2.301 0.06103 694.9 684.1 2.298\n 190 0.07492 650.9 745.3 2.331 0.06225 708.3 693.0 2.312\n 200 0.07573 663.8 751.0 2.364 0.06327 724.3 702.1 2.321\n\nP = 12.0 bar = 1.2 MPa (T\\_r = 34.39°C)\n Sat. 0.06136 457.7 498.8 1.802 0.06144 462.1 509.3 1.822\n 20 0.06289 455.0 497.3 1.806 0.06194 474.5 520.7 1.842\n 30 0.06361 459.4 499.9 1.810 0.06202 485.3 523.0 1.854\n 40 0.06411 466.3 508.9 1.820 0.06245 494.9 535.0 1.869\n 50 0.06443 473.5 515.7 1.825 0.06289 501.2 540.5 1.870\n TABLE A-18 (Continued)\nT v u h j v h \n°C m³/kg kJ/kg kJ/kg·K m³/kg kJ/kg kJ/kg·K\nP = 18.0 bar = 1.8 MPa (T\\_r = 52.30°C)\n Sat. 0.04241 474.9 518.5 1.705 0.02157 478.7 521.8 1.700\n 20 0.06020 494.1 531.4 1.763 0.02216 484.8 529.1 1.722\n 30 0.07278 514.6 580.4 1.834 0.02426 505.4 534.5 1.797\n 40 0.08020 532.9 590.3 1.845 0.02558 509.8 538.0 1.804\n 50 0.08226 543.8 602.8 1.877 0.02792 511.9 545.6 1.817\n 60 0.08540 556.2 610.0 1.898 0.02918 516.8 552.2 1.832\n 70 0.09030 570.7 617.2 1.912 0.03100 520.1 562.8 1.850\n 80 0.09215 586.1 624.0 1.929 0.03242 522.5 572.4 1.871\n 90 0.09246 590.8 629.4 1.936 0.03455 523.5 576.1 1.892\n 100 0.09500 593.5 632.2 1.940 0.03589 523.4 579.2 1.910\n 110 0.09656 596.1 633.7 1.952 0.03792 524.8 583.1 1.926\n 120 0.09787 597.8 635.4 1.965 0.04041 525.2 585.2 1.935\n 130 0.09911 598.5 637.7 1.971 0.04267 526.3 588.7 1.959\n 140 0.09946 599.1 638.7 1.983 0.04449 527.1 590.7 1.968\n 150 0.09972 599.6 639.1 1.993 0.04610 528.3 592.4 1.975\n 160 0.10000 600.1 640.4 2.004 0.04772 529.8 593.9 1.984\n 170 0.10031 600.8 641.7 2.015 0.04797 530.8 594.8 1.993\n 180 0.10062 601.5 643.0 2.026 0.04812 531.8 596.2 2.000\n