CONTROL VALVE HANDBOOK Episode 2 Part 4 pptx

Chapter 10. Engineering Data 207 Refrigerant 717 (Ammonia) Properties of Liquid and Saturated Vapor (continued) TEMP ( _F) ENTROPY (1) BTU/(LB.)(_R) ENTHALPY (1) (BTU/LB.) DENSITY (LB./CU. FT.) VOLUME (CU. FT./LB.) PRESSURE TEMP ( _F) Vapor s g Liquid s f Vapor h g Liquid h f Liquid I/v f Vapor V g psigpsia −59 −58 −57 −56 −55 −54 −53 −52 −51 −50 −49 −48 −47 −46 −45 −44 −43 −42 −41 −40 −39 −38 −37 −36 −35 −34 −33 −32 −31 −30 −29 −28 −27 −26 −25 −24 −23 −22 −21 −20 −19 −18 −17 −16 −15 −14 5.74 5.93 6.13 6.33 6.54 6.75 6.97 7.20 7.43 7.67 7.91 8.16 8.42 8.68 8.95 9.23 9.51 9.81 10.10 10.41 10.72 11.04 11.37 11.71 12.05 12.41 12.77 13.14 13.52 13.90 14.30 14.71 15.12 15.55 15.98 16.24 16.88 17.34 17.81 18.30 18.79 19.30 19.81 20.34 20.88 21.43 18.2 (2) 17.8 (2) 17.4 (2) 17.0 (2) 16.6 (2) 16.2 (2) 15.7 (2) 15.3 (2) 14.8 (2) 14.3 (2) 13.8 (2) 13.3 (2) 12.8 (2) 12.2 (2) 11.7 (2) 11.1 (2) 10.6 (2) 10.0 (2) 9.3 (2) 8.7 (2) 8.1 (2) 7.4 (2) 6.8 (2) 6.1 (2) 5.4 (2) 4.7 (2) 3.9 (2) 3.2 (2) 2.4 (2) 1.6 (2) 0.8 (2) 0.0 0.4 0.8 1.3 1.7 2.2 2.6 3.1 3.6 4.1 4.6 5.1 5.6 6.2 6.7 43.37 42.05 40.79 39.56 38.38 37.24 36.15 35.09 34.06 33.08 32.12 31.20 30.31 29.45 28.62 27.82 27.04 26.29 25.56 24.86 24.18 23.53 22.89 22.27 21.68 21.10 20.54 20.00 19.48 18.97 18.48 18.00 17.54 17.09 16.66 16.24 15.83 15.43 15.05 14.68 14.32 13.97 13.62 13.29 12.97 12.66 43.87 43.83 43.78 43.74 43.70 43.66 43.62 43.58 43.54 43.49 43.45 43.41 43.37 43.33 43.28 43.24 43.20 43.16 43.12 43.08 43.04 42.99 42.95 42.90 42.86 42.82 42.78 42.73 42.69 42.65 42.61 42.57 42.54 42.48 42.44 42.40 42.35 42.31 42.26 42.22 42.18 42.13 42.09 42.04 42.00 41.96 −20.1 −19.1 −18.0 −17.0 −15.9 −14.8 −13.8 −12.7 −11.7 −10.6 −9.6 −8.5 −7.4 −6.4 −5.3 −4.3 −3.2 −2.1 −1.1 0.0 1.1 2.1 3.2 4.3 5.3 6.4 7.4 8.5 9.6 10.7 11.7 12.8 13.9 14.9 16.0 17.1 18.1 19.2 20.3 21.4 22.4 23.5 24.6 25.6 26.7 27.8 590.0 590.4 590.8 591.2 591.6 592.1 592.4 592.9 593.2 593.7 594.0 594.4 594.9 595.2 595.6 596.0 596.4 596.8 597.2 597.6 598.0 598.3 598.7 599.1 599.5 599.9 600.2 600.6 601.0 601.4 601.7 602.1 602.5 602.8 603.2 603.6 603.9 604.3 604.6 605.0 605.3 605.7 606.1 606.4 606.7 607.1 −0.0490 −.0464 −.0438 −.0412 −.0386 −0.0360 −.0334 −.0307 −.0281 −.0256 −0.0230 −.0204 −.0179 −.0153 −.0127 −0.0102 −.0076 −.0051 −.0025 .0000 0.0025 .0051 .0076 .0101 .0126 0.0151 .0176 .0201 .0226 .0250 0.0275 .0300 .0325 .0350 .0374 0.0399 .0423 .0448 .0472 .0497 0.0521 .0545 .0570 .0594 .0618 .0642 1.4741 1.4713 1.4686 1.4658 1.4631 1.4604 1.4577 1.4551 1.4524 1.4497 1.4471 1.4445 1.4419 1.4393 1.4368 1.4342 1.4317 1.4292 1.4267 1.4242 1.4217 1.4193 1.4169 1.4144 1.4120 1.4096 1.4072 1.4048 1.4025 1.4001 1.3978 1.3955 1.3932 1.3909 1.3886 1.3863 1.3840 1.3818 1.3796 1.3774 1.3752 1.3729 1.3708 1.3686 1.3664 1.3642 (continued) Chapter 10. Engineering Data 208 Refrigerant 717 (Ammonia) Properties of Liquid and Saturated Vapor (continued) TEMP ( _F) ENTROPY (1) BTU/(LB.)(_R) ENTHALPY (1) (BTU/LB.) DENSITY (LB./CU. FT.) VOLUME (CU. FT./LB.) PRESSURE TEMP ( _F) Vapor s g Liquid s f Vapor h g Liquid h f Liquid I/v f Vapor V g psigpsia −13 −12 −11 −10 −9 −8 −7 −6 −5 −4 −3 −2 −1 0 1 2 3 4 5 (3) 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 21.99 22.56 23.15 23.74 24.35 24.97 25.61 26.26 26.92 27.59 28.28 28.98 29.69 30.42 31.16 31.92 32.69 33.47 34.27 35.09 35.92 36.77 37.63 38.51 39.40 40.31 41.24 42.18 43.14 44.12 45.12 46.13 47.16 48.21 49.28 50.36 51.47 52.59 53.73 54.90 56.08 57.28 58.50 59.74 61.00 62.29 7.3 7.9 8.5 9.0 9.7 10.3 10.9 11.6 12.2 12.9 13.6 14.3 15.0 15.7 16.5 17.2 18.0 18.8 19.6 20.4 21.2 22.1 22.9 23.8 24.7 25.6 26.5 27.5 28.4 29.4 30.4 31.4 32.5 33.5 34.6 35.7 36.8 37.9 39.0 40.2 41.4 42.6 43.8 45.0 46.3 47.6 12.36 12.06 11.78 11.50 11.23 10.97 10.71 10.47 10.23 9.991 9.763 9.541 9.326 9.116 8.912 8.714 8.521 8.333 8.150 7.971 7.798 7.629 7.464 7.304 7.148 6.996 6.847 6.703 6.562 6.425 6.291 6.161 6.034 5.910 5.789 5.671 5.556 5.443 5.334 5.227 5.123 5.021 4.922 4.825 4.730 4.637 41.91 41.87 41.82 41.78 41.74 41.69 41.65 41.60 41.56 41.52 41.47 41.43 41.38 41.34 41.29 41.25 41.20 41.16 41.11 41.07 41.01 40.98 40.93 40.89 40.84 40.80 40.75 40.71 40.66 40.61 40.57 40.52 40.48 40.43 40.38 40.34 40.29 40.25 40.20 40.15 40.10 40.06 40.01 39.96 39.91 39.86 28.9 30.0 31.0 32.1 33.2 34.3 35.4 36.4 37.5 38.6 39.7 40.7 41.8 42.9 44.0 45.1 46.2 47.2 48.3 49.4 50.5 51.6 52.7 53.8 54.9 56.0 57.1 58.2 59.2 60.3 61.4 62.5 63.6 64.7 65.8 66.9 68.0 69.1 70.2 71.3 72.4 73.5 74.6 75.7 76.8 77.9 607.5 607.8 608.1 608.5 608.8 609.2 609.5 609.8 610.1 610.5 610.8 611.1 611.4 611.8 612.1 612.4 612.7 613.0 613.3 613.6 613.9 614.3 614.6 614.9 615.2 615.5 615.8 616.1 616.3 616.6 616.9 617.2 617.5 617.8 618.0 618.3 618.6 618.9 619.1 619.4 619.7 619.9 620.2 620.5 620.7 621.0 0.0666 .0690 .0714 .0738 .0762 0.0786 .0809 .0833 .0857 .0880 0.0909 .0928 .0951 .0975 .0998 0.1022 .1045 .1069 .1092 .1115 0.1138 .1162 .1185 .1208 .1231 0.1254 .1277 .1300 .1323 .1346 0.1369 .1392 .1415 .1437 .1460 0.1483 .1505 .1528 .1551 .1573 0.1596 .1618 .1641 .1663 .1686 .1708 1.3624 1.3600 1.3579 1.3558 1.3537 1.3516 1.3493 1.3474 1.3454 1.3433 1.3413 1.3393 1.3372 1.3352 1.3332 1.3312 1.3292 1.3273 1.3253 1.3234 1.3214 1.3195 1.3176 1.3157 1.3137 1.3118 1.3099 1.3081 1.3062 1.3043 1.3025 1.3006 1.2988 1.2969 1.2951 1.2933 1.2915 1.2897 1.2879 1.2861 1.2843 1.2823 1.2809 1.2790 1.2773 1.2755 (continued) Chapter 10. Engineering Data 209 Refrigerant 717 (Ammonia) Properties of Liquid and Saturated Vapor (continued) TEMP ( _F) ENTROPY (1) BTU/(LB.)(_R) ENTHALPY (1) (BTU/LB.) DENSITY (LB./CU. FT.) VOLUME (CU. FT./LB.) PRESSURE TEMP ( _F) Vapor s g Liquid s f Vapor h g Liquid h f Liquid I/v f Vapor V g psigpsia 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 63.59 64.91 66.26 67.63 69.02 70.43 71.87 73.32 74.80 76.31 77.83 79.38 80.96 82.55 84.18 85.82 87.49 89.19 90.91 92.66 94.43 96.23 98.06 99.91 101.8 103.7 105.6 107.6 109.6 111.6 113.6 115.7 117.8 120.0 122.1 124.3 126.5 128.8 131.1 133.4 135.7 138.1 140.5 143.0 145.4 147.9 48.9 50.2 51.6 52.9 54.3 55.7 57.2 58.6 60.1 61.6 63.1 64.7 66.3 67.9 69.5 71.1 72.8 74.5 76.2 78.0 79.7 81.5 83.4 85.2 87.1 89.0 90.9 92.9 94.9 96.9 98.9 101.0 103.1 105.3 107.4 109.6 111.8 114.1 116.4 118.7 121.0 123.4 125.8 128.3 130.7 133.2 4.547 4.459 4.373 4.289 4.207 4.126 4.048 3.971 3.897 3.823 3.752 3.682 3.614 3.547 3.481 3.418 3.355 3.294 3.234 3.176 3.119 3.063 3.008 2.954 2.902 2.851 2.800 2.751 2.703 2.656 2.610 2.565 2.520 2.477 2.435 2.393 2.352 2.312 2.273 2.235 2.197 2.161 2.125 2.089 2.055 2.021 39.82 39.77 39.72 39.67 39.63 39.58 39.54 39.49 39.44 39.39 39.34 39.29 39.24 39.19 39.14 39.10 39.05 39.00 38.95 38.90 38.85 38.80 38.75 38.70 38.65 38.60 38.55 38.50 38.45 38.40 38.35 38.30 38.25 38.20 38.15 38.10 38.05 38.00 37.95 37.90 37.84 37.79 37.74 37.69 37.64 37.58 79.0 80.1 81.2 82.3 83.4 84.6 85.7 86.8 87.9 89.0 90.1 91.2 92.3 93.5 94.6 95.7 96.8 97.9 99.1 100.2 101.3 102.4 103.5 104.7 105.8 106.9 108.1 109.2 110.3 111.5 112.6 113.7 114.8 116.0 117.1 118.3 119.4 120.5 121.7 122.8 124.0 125.1 126.2 127.4 128.5 129.7 621.2 621.5 621.7 622.0 622.2 622.5 622.7 623.0 623.2 623.4 623.7 623.9 624.1 624.4 624.6 624.8 625.0 625.2 625.5 625.7 625.9 626.1 626.3 626.5 626.7 626.9 627.1 627.3 627.5 627.7 627.9 628.0 628.2 628.4 628.6 628.8 628.9 629.1 629.3 629.4 629.6 629.8 629.9 630.1 630.2 630.4 0.1730 .1753 .1775 .1797 .1819 0.1841 .1863 .1885 .1908 .1930 0.1952 .1974 .1996 .2018 .2040 0.2062 .2083 .2105 .2127 .2149 0.2171 .2192 .2214 .2236 .2257 0.2279 .2301 .2322 .2344 .2365 0.2387 .2408 .2430 .2451 .2473 0.2494 .2515 .2537 .2558 .2579 0.2601 .2622 .2643 .2664 .2685 .2706 1.2738 1.2721 1.2704 1.2686 1.2669 1.2652 1.2635 1.2618 1.2602 1.2585 1.2568 1.2552 1.2535 1.2518 1.2492 1.2484 1.2469 1.2453 1.2437 1.2421 1.2405 1.2382 1.2372 1.2357 1.2341 1.2325 1.2310 1.2294 1.2273 1.2263 1.2247 1.2231 1.2213 1.2201 1.2183 1.2179 1.2155 1.2140 1.2125 1.2110 1.2095 1.2080 1.2065 1.2050 1.2035 1.2020 (continued) Chapter 10. Engineering Data 210 Refrigerant 717 (Ammonia) Properties of Liquid and Saturated Vapor (continued) TEMP ( _F) ENTROPY (1) BTU/(LB.)(_R) ENTHALPY (1) (BTU/LB.) DENSITY (LB./CU. FT.) VOLUME (CU. FT./LB.) PRESSURE TEMP ( _F) Vapor s g Liquid s f Vapor h g Liquid h f Liquid I/v f Vapor V g psigpsia 79 80 81 82 83 84 85 86 (3) 87 88 89 90 91 92 93 94 95 96 97 98 99 100 101 102 103 104 105 106 107 108 109 110 111 112 113 114 115 116 117 118 119 120 121 122 123 124 125 150.5 153.0 155.6 158.3 161.0 163.7 166.4 169.2 172.0 174.8 177.7 180.6 183.6 186.6 189.6 192.7 195.8 198.9 202.1 205.3 208.6 211.9 215.2 218.6 222.0 225.4 228.9 232.5 236.0 239.7 243.3 247.0 250.8 254.5 258.4 262.2 266.2 270.1 274.1 278.2 282.3 286.4 290.6 294.8 299.1 303.4 307.8 135.8 138.3 140.9 143.6 146.3 149.0 151.7 154.5 157.3 160.1 163.0 165.9 168.9 171.9 174.9 178.0 181.1 184.2 187.4 190.6 193.9 197.2 200.5 203.9 207.3 210.7 214.2 217.8 221.3 225.0 228.6 232.3 236.1 239.8 243.7 247.5 251.5 255.4 259.4 263.5 267.6 271.7 275.9 280.1 284.4 288.7 293.1 1.988 1.955 1.923 1.892 1.861 1.831 1.801 1.772 1.744 1.716 1.688 1.661 1.635 1.609 1.584 1.559 1.534 1.510 1.487 1.464 1.441 1.419 1.397 1.375 1.354 1.334 1.313 1.293 1.274 1.254 1.235 1.217 1.198 1.180 1.163 1.145 1.128 1.112 1.095 1.079 1.063 1.047 1.032 1.017 1.002 0.987 0.973 37.53 37.48 37.43 37.37 37.32 37.26 37.21 37.16 37.11 37.05 37.00 36.95 36.89 36.84 36.78 36.73 36.67 36.62 36.56 36.51 36.45 36.40 36.34 36.29 36.23 36.18 36.12 36.06 36.01 35.95 35.90 35.84 35.78 35.72 35.67 35.61 35.55 35.49 35.43 35.38 35.32 35.26 35.20 35.14 35.08 35.02 34.96 130.8 132.0 133.1 134.3 135.4 136.6 137.8 138.9 140.1 141.2 142.4 143.5 144.7 145.8 147.0 148.2 149.4 150.5 151.7 152.9 154.0 155.2 156.4 157.6 158.7 159.9 161.1 162.3 163.5 164.6 165.8 167.0 168.2 169.4 170.6 171.8 173.0 174.2 175.4 176.6 177.8 179.0 180.2 181.4 182.6 183.9 185.1 630.5 630.7 630.8 631.0 631.1 631.3 631.4 631.5 631.7 631.8 631.9 632.0 632.1 632.2 632.3 632.5 632.6 632.6 632.8 632.9 632.9 633.0 633.1 633.2 633.3 633.4 633.4 633.5 633.6 633.6 633.7 633.7 633.8 633.8 633.9 633.9 633.9 634.0 634.0 634.0 634.0 634.0 634.0 634.0 634.0 634.0 634.0 0.2728 .2749 .2769 .2791 .2812 0.2833 .2854 .2875 .2895 .2917 0.2937 .2958 .2979 .3000 .3021 0.3041 .3062 .3083 .3104 .3125 0.3145 .3166 .3187 .3207 .3228 0.3248 .3269 .3289 .3310 .3330 0.3351 .3372 .3392 .3413 .3433 0.3453 .3474 .3495 .3515 .3535 3556 0.3576 .3597 .3618 .3638 .3659 .3679 1.2006 1.1991 1.1976 1.1962 1.1947 1.1933 1.1918 1.1904 1.1889 1.1875 1.1860 1.1846 1.1832 1.1818 1.1804 1.1789 1.1775 1.1761 1.1747 1.1733 1.1719 1.1705 1.1691 1.1677 1.1663 1.1649 1.1635 1.1621 1.1607 1.1593 1.1580 1.1566 1.1552 1.1538 1.1524 1.1510 1.1497 1.1483 1.1469 1.1455 1.1441 1.1427 1.1414 1.1400 1.1386 1.1372 1.1358 1. Based on 0 for the saturated liquid at −40_F. 2. Inches of mercury below one standard atmosphere. 3. Standard cycle temperatures. Chapter 10. Engineering Data 211 Properties of Water Temperature (_F) Saturation Pressure (Pounds Per Square Inch Absolute) Weight (Pounds Per Gallon) Specific Gravity 60/60 _F Conversion Factor, (1) lbs./hr. to GPM 32 .0885 8.345 1.0013 .00199 40 .1217 8.345 1.0013 .00199 50 .1781 8.340 1.0007 .00199 60 .2653 8.334 1.0000 .00199 70 .3631 8.325 .9989 .00200 80 .5069 8.314 .9976 .00200 90 .6982 8.303 .9963 .00200 100 .9492 8.289 .9946 .00201 110 1.2748 8.267 .9919 .00201 120 1.6924 8.253 .9901 .00201 130 2.2225 8.227 .9872 .00202 140 2.8886 8.207 .9848 .00203 150 3.718 8.182 .9818 .00203 160 4.741 8.156 .9786 .00204 170 5.992 8.127 .9752 .00205 180 7.510 8.098 .9717 .00205 190 9.339 8.068 .9681 .00206 200 11.526 8.039 .9646 .00207 210 14.123 8.005 .9605 .00208 212 14.696 7.996 .9594 .00208 220 17.186 7.972 .9566 .00209 240 24.969 7.901 .9480 .00210 260 35.429 7.822 .9386 .00211 280 49.203 7.746 .9294 .00215 300 67.013 7.662 .9194 .00217 350 134.63 7.432 .8918 .00224 400 247.31 7.172 .8606 .00232 450 422.6 6.892 .8270 .00241 500 680.8 6.553 .7863 .00254 550 1045.2 6.132 .7358 .00271 600 1542.9 5.664 .6796 .00294 700 3093.7 3.623 .4347 .00460 1. Multiply flow in pounds per hour by the factor to get equivalent flow in gallons per minute. Weight per gallon is based on 7.48 gallons per cubic foot. Chapter 10. Engineering Data 212 Properties of Saturated Steam ABSOLUTE PRESSURE VACUUM (INCHES OF Hg) TEMPER− ATURE t (_F) HEAT OF THE LIQUID (BTU/LB ) LATENT HEAT OF EVAPOR− ATION (BTU/LB) TOTAL HEAT OF STEAM H g (BTU/LB) SPECIFIC VOLUME r (CU FT PER LB) Lbs Per Sq In. P’ Inches of Hg 0.20 0.25 0.30 0.35 0.40 0.45 0.50 0.60 0.70 0.80 0.90 1.0 1.2 1.4 1.6 1.8 2.0 2.2 2.4 2.6 2.8 3.0 3.5 4.0 4.5 5.0 5.5 6.0 6.5 7.0 7.5 8.0 8.5 9.0 9.5 10.0 11.0 12.0 13.0 14.0 0.41 0.51 0.61 0.71 0.81 0.92 1.02 1.22 1.43 1.63 1.83 2.04 2.44 2.85 3.26 3.66 4.07 4.48 4.89 5.29 5.70 6.11 7.13 8.14 9.16 10.18 11.20 12.22 13.23 14.25 15.27 16.29 17.31 18.32 19.34 20.36 22.40 24.43 26.47 28.50 29.51 29.41 29.31 29.21 29.11 29.00 28.90 28.70 28.49 28.29 28.09 27.88 27.48 27.07 26.66 26.26 25.85 25.44 25.03 24.63 24.22 23.81 22.79 21.78 20.76 19.74 18.72 17.70 16.69 15.67 14.65 13.63 12.61 11.60 10.58 9.56 7.52 5.49 3.45 1.42 53.14 59.30 64.47 68.93 72.86 76.38 79.58 85.21 90.08 94.38 98.24 101.74 107.92 113.26 117.99 122.23 126.08 129.62 132.89 135.94 138.79 141.48 147.57 152.97 157.83 162.24 166.30 170.06 173.56 176.85 179.94 182.86 185.64 188.28 190.80 193.21 197.75 201.96 205.88 209.56 21.21 27.36 32.52 36.97 40.89 44.41 47.60 53.21 58.07 62.36 66.21 69.70 75.87 81.20 85.91 90.14 93.99 97.52 100.79 103.83 106.68 109.37 115.46 120.86 125.71 130.13 134.19 137.96 141.47 144.76 147.86 150.79 153.57 156.22 158.75 161.17 165.73 169.96 173.91 177.61 1063.8 1060.3 1057.4 1054.9 1052.7 1050.7 1048.8 1045.7 1042.9 1040.4 1038.3 1036.3 1032.7 1029.6 1026.9 1024.5 1022.2 1020.2 1018.3 1016.5 1014.8 1013.2 1009.6 1006.4 1003.6 1001.0 998.5 996.2 994.1 992.1 990.2 988.5 986.8 985.2 983.6 982.1 979.3 976.6 974.2 971.9 1085.0 1087.7 1090.0 1091.9 1093.6 1095.1 1096.4 1098.9 1101.0 1102.8 1104.5 1106.0 1108.6 1110.8 1112.8 1114.6 1116.2 1117.7 1119.1 1120.3 1121.5 1122.6 1125.1 1127.3 1129.3 1131.1 1132.7 1134.2 1135.6 1136.9 1138.1 1139.3 1140.4 1141.4 1142.3 1143.3 1145.0 1146.6 1148.1 1149.5 1526.0 1235.3 1039.5 898.5 791.9 708.5 641.4 540.0 466.9 411.7 368.4 333.6 280.9 243.0 214.3 191.8 173.73 158.85 146.38 135.78 126.65 118.71 102.72 90.63 81.16 73.52 67.24 61.98 57.50 53.64 50.29 47.34 44.73 42.40 40.31 38.42 35.14 32.40 30.06 28.04 Chapter 10. Engineering Data 213 Properties of Saturated Steam PRESSURE (LBS. PER SQ IN.) TEMPER− ATURE t (_F) HEAT OF THE LIQUID (BTU/LB) LATENT HEAT OF EVAPOR− ATION (BTU/LB) TOTAL HEAT OF STEAM H g (BTU/LB) SPECIFIC VOLUME r (CU FT PER LB) Absolute P’ Gauge P 14.696 15.0 16.0 17.0 18.0 19.0 20.0 21.0 22.0 23.0 24.0 25.0 26.0 27.0 28.0 29.0 30.0 31.0 32.0 33.0 34.0 35.0 36.0 37.0 38.0 39.0 40.0 41.0 42.0 43.0 44.0 45.0 46.0 47.0 48.0 49.0 50.0 51.0 52.0 53.0 54.0 0.0 0.3 1.3 2.3 3.3 4.3 5.3 6.3 7.3 8.3 9.3 10.3 11.3 12.3 13.3 14.3 15.3 16.3 17.3 18.3 19.3 20.3 21.3 22.3 23.3 24.3 25.3 26.3 27.3 28.3 29.3 30.3 31.3 32.3 33.3 34.3 35.3 36.3 37.3 38.3 39.3 212.00 213.03 216.32 219.44 222.41 225.24 227.96 230.57 233.07 235.49 237.82 240.07 242.25 244.36 246.41 248.40 250.33 252.22 254.05 255.84 257.58 259.28 260.95 262.57 264.16 265.72 267.25 268.74 270.21 271.64 273.05 274.44 275.80 277.13 278.45 279.74 281.01 282.26 283.49 284.70 285.90 180.07 181.11 184.42 187.56 190.56 193.42 196.16 198.79 201.33 203.78 206.14 208.42 210.62 212.75 214.83 216.86 218.82 220.73 222.59 224.41 226.18 227.91 229.60 231.26 232.89 234.48 236.03 237.55 239.04 240.51 241.95 243.36 244.75 246.12 247.47 248.79 250.09 251.37 252.63 253.87 255.09 970.3 969.7 967.6 965.5 963.6 961.9 960.1 958.4 956.8 955.2 953.7 952.1 950.7 949.3 947.9 946.5 945.3 944.0 942.8 941.6 940.3 939.2 938.0 936.9 935.8 934.7 933.7 932.6 931.6 930.6 929.6 928.6 927.7 926.7 925.8 924.9 924.0 923.0 922.2 921.3 920.5 1150.4 1150.8 1152.0 1153.1 1154.2 1155.3 1156.3 1157.2 1158.1 1159.0 1159.8 1160.6 1161.3 1162.0 1162.7 1163.4 1164.1 1164.7 1165.4 1166.0 1166.5 1167.1 1167.6 1168.2 1168.7 1169.2 1169.7 1170.2 1170.7 1171.1 1171.6 1172.0 1172.4 1172.9 1173.3 1173.7 1174.1 1174.4 1174.8 1175.2 1175.6 26.80 26.29 24.75 23.39 22.17 21.08 20.089 19.192 18.375 17.627 16.938 16.303 15.715 15.170 14.663 14.189 13.746 13.330 12.940 12.572 12.226 11.898 11.588 11.294 11.015 10.750 10.498 10.258 10.029 9.810 9.601 9.401 9.209 9.025 8.848 8.678 8.515 8.359 8.208 8.062 7.922 (continued) Chapter 10. Engineering Data 214 Properties of Saturated Steam (continued) PRESSURE (LBS. PER SQ IN.) SPECIFIC VOLUME r (CU FT PER LB) TOTAL HEAT OF STEAM H g (BTU/LB) LATENT HEAT OF EVAPOR− ATION (BTU/LB) HEAT OF THE LIQUID (BTU/LB) TEMPER− ATURE t (_F) Absolute P’ SPECIFIC VOLUME r (CU FT PER LB) TOTAL HEAT OF STEAM H g (BTU/LB) LATENT HEAT OF EVAPOR− ATION (BTU/LB) HEAT OF THE LIQUID (BTU/LB) TEMPER− ATURE t (_F) Gauge P 55.0 56.0 57.0 58.0 59.0 60.0 61.0 62.0 63.0 64.0 65.0 66.0 67.0 68.0 69.0 70.0 71.0 72.0 73.0 74.0 75.0 76.0 77.0 78.0 79.0 80.0 81.0 82.0 83.0 84.0 85.0 86.0 87.0 88.0 89.0 90.0 91.0 92.0 93.0 94.0 95.0 96.0 97.0 98.0 99.0 40.3 41.3 42.3 43.3 44.3 45.3 46.3 47.3 48.3 49.3 50.3 51.3 52.3 53.3 54.3 55.3 56.3 57.3 58.3 59.3 60.3 61.3 62.3 63.3 64.3 65.3 66.3 67.3 68.3 69.3 70.3 71.3 72.3 73.3 74.3 75.3 76.3 77.3 78.3 79.3 80.3 81.3 82.3 83.3 84.3 287.07 288.23 289.37 290.50 291.61 292.71 293.79 294.85 295.90 296.94 297.97 298.99 299.99 300.98 301.96 302.92 303.88 304.83 305.76 306.68 307.60 308.50 309.40 310.29 311.16 312.03 312.89 313.74 314.59 315.42 316.25 317.07 317.88 318.68 319.48 320.27 321.06 321.83 322.60 323.36 324.12 324.87 325.61 326.35 327.08 256.30 257.50 258.67 259.82 260.96 262.09 263.20 264.30 265.38 266.45 267.50 268.55 269.58 270.60 291.61 272.61 273.60 274.57 275.54 276.49 277.43 278.37 279.30 280.21 281.12 282.02 282.91 283.79 284.66 285.53 286.39 287.24 288.08 288.91 289.74 290.56 291.38 292.18 292.98 293.78 294.56 295.34 296.12 296.89 297.65 919.6 918.8 917.9 917.1 916.3 915.5 914.7 913.9 913.1 912.3 911.6 910.8 910.1 909.4 908.7 907.9 907.2 906.5 905.8 905.1 904.5 903.7 903.1 902.4 901.7 901.1 900.4 899.7 899.1 898.5 897.8 897.2 896.5 895.9 895.3 894.7 894.1 893.5 892.9 892.3 891.7 891.1 890.5 889.9 889.4 1175.9 1176.3 1176.6 1176.9 1177.3 1177.6 1177.9 1178.2 1178.5 1178.8 1179.1 1179.4 1179.7 1180.0 1180.3 1180.6 1180.8 1181.1 1181.3 1181.6 1181.9 1182.1 1182.4 1182.6 1182.8 1183.1 1183.3 1183.5 1183.8 1184.0 1184.2 1184.4 1184.6 1184.8 1185.1 1185.3 1185.5 1185.7 1185.9 1186.1 1186.2 1186.4 1186.6 1186.8 1187.0 7.787 7.656 7.529 7.407 7.289 7.175 7.064 6.957 6.853 6.752 6.655 6.560 6.468 6.378 6.291 6.206 6.124 6.044 5.966 5.890 5.816 5.743 5.673 5.604 5.537 5.472 5.408 5.346 5.285 5.226 5.168 5.111 5.055 5.001 4.948 4.896 4.845 4.796 4.747 4.699 4.652 4.606 4.561 4.517 4.474 (continued) Chapter 10. Engineering Data 215 Properties of Saturated Steam (continued) PRESSURE (LBS. PER SQ IN.) SPECIFIC VOLUME r (CU FT PER LB) TOTAL HEAT OF STEAM H g (BTU/LB) LATENT HEAT OF EVAPOR− ATION (BTU/LB) HEAT OF THE LIQUID (BTU/LB) TEMPER− ATURE t (_F) Absolute P’ SPECIFIC VOLUME r (CU FT PER LB) TOTAL HEAT OF STEAM H g (BTU/LB) LATENT HEAT OF EVAPOR− ATION (BTU/LB) HEAT OF THE LIQUID (BTU/LB) TEMPER− ATURE t (_F) Gauge P 100.0 101.0 102.0 103.0 104.0 105.0 106.0 107.0 108.0 109.0 110.0 111.0 112.0 113.0 114.0 115.0 116.0 117.0 118.0 119.0 120.0 121.0 122.0 123.0 124.0 125.0 126.0 127.0 128.0 129.0 130.0 131.0 132.0 133.0 134.0 135.0 136.0 137.0 138.0 139.0 140.0 141.0 142.0 143.0 144.0 85.3 86.3 87.3 88.3 89.3 90.3 91.3 92.3 93.3 94.3 95.3 96.3 97.3 98.3 99.3 100.3 101.3 102.3 103.3 104.3 105.3 106.3 107.3 108.3 109.3 110.3 111.3 112.3 113.3 114.3 115.3 116.3 117.3 118.3 119.3 120.3 121.3 122.3 123.3 124.3 125.3 126.3 127.3 128.3 129.3 327.81 328.53 329.25 329.96 330.66 331.36 332.05 332.74 333.42 334.10 334.77 335.44 336.11 336.77 337.42 338.07 338.72 339.36 339.99 340.62 341.25 341.88 342.50 343.11 343.72 344.33 344.94 345.54 346.13 346.73 347.32 347.90 348.48 349.06 349.64 350.21 350.78 351.35 351.91 352.47 353.02 353.57 354.12 354.67 355.21 298.40 299.15 299.90 300.64 301.37 302.10 302.82 303.54 304.26 304.97 305.66 306.37 307.06 307.75 308.43 309.11 309.79 310.46 311.12 311.78 312.44 313.10 313.75 314.40 315.04 315.68 316.31 316.94 317.57 318.19 318.81 319.43 320.04 320.65 321.25 321.85 322.45 323.05 323.64 324.23 324.82 325.40 325.98 326.56 327.13 888.8 888.2 887.6 887.1 886.5 886.0 885.4 884.9 884.3 883.7 883.2 882.6 882.1 881.6 881.1 880.6 880.0 879.5 879.0 878.4 877.9 877.4 876.9 876.4 875.9 875.4 874.9 874.4 873.9 873.4 872.9 872.5 872.0 871.5 871.0 870.6 870.1 869.6 869.1 868.7 868.2 867.7 867.2 866.7 866.3 1187.2 1187.4 1187.5 1187.7 1187.9 1188.1 1188.2 1188.4 1188.6 1188.7 1188.9 1189.0 1189.2 1189.4 1189.5 1189.7 1189.8 1190.0 1190.1 1190.2 1190.4 1190.5 1190.7 1190.8 1190.9 1191.1 1191.2 1191.3 1191.5 1191.6 1191.7 1191.9 1192.0 1192.1 1192.2 1192.4 1192.5 1192.6 1192.7 1192.9 1193.0 1193.1 1193.2 1193.3 1193.4 4.432 4.391 4.350 4.310 4.271 4.232 4.194 4.157 4.120 4.084 4.049 4.015 3.981 3.947 3.914 3.882 3.850 3.819 3.788 3.758 3.728 3.699 3.670 3.642 3.614 3.587 3.560 3.533 3.507 3.481 3.455 3.430 3.405 3.381 3.357 3.333 3.310 3.287 3.264 3.242 3.220 3.198 3.177 3.155 3.134 (continued) Chapter 10. Engineering Data 216 Properties of Saturated Steam (continued) PRESSURE (LBS. PER SQ IN.) SPECIFIC VOLUME r (CU FT PER LB) TOTAL HEAT OF STEAM H g (BTU/LB) LATENT HEAT OF EVAPOR− ATION (BTU/LB) HEAT OF THE LIQUID (BTU/LB) TEMPER− ATURE t (_F) Absolute P’ SPECIFIC VOLUME r (CU FT PER LB) TOTAL HEAT OF STEAM H g (BTU/LB) LATENT HEAT OF EVAPOR− ATION (BTU/LB) HEAT OF THE LIQUID (BTU/LB) TEMPER− ATURE t (_F) Gauge P 145.0 146.0 147.0 148.0 149.0 150.0 152.0 154.0 156.0 158.0 160.0 162.0 164.0 166.0 168.0 170.0 172.0 174.0 176.0 178.0 180.0 182.0 184.0 186.0 188.0 190.0 192.0 194.0 196.0 198.0 200.0 205.0 210.0 215.0 220.0 225.0 230.0 235.0 240.0 245.0 250.0 255.0 260.0 265.0 270.0 130.3 131.3 132.3 133.3 134.3 135.3 137.3 139.3 141.3 143.3 145.3 147.3 149.3 151.3 153.3 155.3 157.3 159.3 161.3 163.3 165.3 167.3 169.3 171.3 173.3 175.3 177.3 179.3 181.3 183.3 185.3 190.3 195.3 200.3 205.3 210.3 215.3 220.3 225.3 230.3 235.3 240.3 245.3 250.3 255.3 355.76 356.29 356.83 357.36 357.89 358.42 359.46 360.49 361.52 362.53 363.53 364.53 365.51 366.48 367.45 368.41 369.35 370.29 371.22 372.14 373.06 373.96 374.86 375.75 376.64 377.51 378.38 379.24 380.10 380.95 381.79 383.86 385.90 387.89 389.86 391.79 393.68 395.54 397.37 399.18 400.95 402.70 404.42 406.11 407.78 327.70 328.27 328.83 329.39 329.95 330.51 331.61 332.70 333.79 334.86 335.93 336.98 338.02 339.05 340.07 341.09 342.10 343.10 344.09 345.06 346.03 347.00 347.96 348.92 349.86 350.79 351.72 352.64 353.55 354.46 355.36 357.58 359.77 361.91 364.02 366.09 368.13 370.14 372.12 374.08 376.00 377.89 379.76 381.60 383.42 865.8 865.3 864.9 864.5 864.0 863.6 862.7 861.8 860.9 860.0 859.2 858.3 857.5 856.6 855.7 854.9 854.1 853.3 852.4 851.6 850.8 850.0 849.2 848.4 847.6 846.8 846.1 845.3 844.5 843.7 843.0 841.1 839.2 837.4 835.6 833.8 832.0 830.3 828.5 826.8 825.1 823.4 821.8 820.1 818.5 1193.5 1193.6 1193.8 1193.9 1194.0 1194.1 1194.3 1194.5 1194.7 1194.9 1195.1 1195.3 1195.5 1195.7 1195.8 1196.0 1196.2 1196.4 1196.5 1196.7 1196.9 1197.0 1197.2 1197.3 1197.5 1197.6 1197.8 1197.9 1198.1 1198.2 1198.4 1198.7 1199.0 1199.3 1199.6 1199.9 1200.1 1200.4 1200.6 1200.9 1201.1 1201.3 1201.5 1201.7 1201.9 3.114 3.094 3.074 3.054 3.034 3.015 2.977 2.940 2.904 2.869 2.834 2.801 2.768 2.736 2.705 2.675 2.645 2.616 2.587 2.559 2.532 2.505 2.479 2.454 2.429 2.404 2.380 2.356 2.333 2.310 2.288 2.234 2.183 2.134 2.087 2.0422 1.9992 1.9579 1.9183 1.8803 1.8438 1.8086 1.7748 1.7422 1.7107 (continued) [...]... 120 3 .4 120 3.7 120 4. 1 120 4. 3 1. 543 3 1 .44 85 1.3 645 1 .28 95 1 .22 22 40 0.0 42 0 .0 44 0.0 46 0.0 48 0.0 385.3 40 5.3 42 5 .3 44 5.3 46 5.3 44 4.59 44 9.39 45 4. 02 45 8.50 4 62. 82 42 4 .0 42 9 .4 4 34. 6 43 9.7 44 4.6 780.5 775 .2 770.0 7 64. 9 759.9 120 4. 5 120 4. 6 120 4. 6 120 4. 6 120 4. 5 1.1613 1.1061 1.0556 1.00 94 0.9670 500.0 520 .0 540 .0 560.0 580.0 48 5.3 505.3 525 .3 545 .3 565.3 46 7.01 47 1.07 47 5.01 47 8.85 4 82. 58 44 9 .4 4 54. 1 45 8.6 46 3.0... 126 6.7 2. 7 72 1 320 .7 3.066 13 72. 6 3.3 52 1 42 4 .0 3.6 34 147 5.5 3.913 1 527 .5 4. 467 1633.3 24 0.0 22 5.3 397.37 r hg - 1. 927 6 120 2.5 2. 0 62 122 8.8 2. 187 125 3.0 2. 247 126 4. 5 2. 533 1319 .2 2.8 04 1371.5 3.068 1 42 3 .2 3. 327 147 4.8 3.5 84 1 526 .9 4. 093 16 32. 9 26 0.0 24 5.3 40 4. 42 r hg - - 1.88 82 122 5.7 2. 006 125 0.5 2. 063 126 2.3 2. 330 1317.7 2. 5 82 1370 .4 2. 827 1 42 2 .3 3.067 147 4 .2 3.305 1 526 .3 3.776 16 32. 5 28 0.0 26 5.3 41 1.05... 146 8.7 2. 031 1 521 .9 2. 327 1 629 .2 44 0.0 42 5 .3 45 4. 02 r hg 1.1 526 123 9.8 1 .22 82 126 6.7 1.3 327 1303.6 1.39 84 1 326 .9 1 .43 06 1338 .2 1 .49 34 1360 .4 1.5 549 13 82. 3 1. 645 4 141 4.7 1.7 925 146 8.1 1.9368 1 521 .3 2. 220 1 628 .8 46 0.0 44 5.3 45 8.50 r hg 1.0 948 123 7.0 1.1685 126 4. 5 1 .26 98 13 02. 0 1.33 34 1 325 .4 1.3 644 1336.9 1. 42 5 0 1359.3 1 .48 42 1381.3 1.5711 141 3.8 1.7 1 24 146 7 .4 1.8508 1 520 .7 2. 122 1 628 .4 480.0 46 5.3 4 62. 82. .. 6.1 52 16 34. 5 180.0 165.3 373.06 r hg - 2. 649 121 4. 0 2. 813 123 7.8 2. 969 126 0 .2 3. 044 127 1.0 3 .41 1 1 323 .5 3.7 64 13 74. 7 4. 110 1 42 5 .6 4. 4 52 147 6.8 4. 7 92 1 528 .6 5 .46 6 16 34. 1 20 0.0 185.3 381.79 r hg - 2. 361 121 0.3 2. 513 123 4. 9 2. 656 125 7.8 2. 726 126 8.9 3.060 1 322 .1 3.380 1373.6 3.693 1 42 4 .8 4. 0 02 147 6 .2 4. 309 1 528 .0 4. 917 1633.7 22 0.0 20 5.3 389.86 r hg - 2. 125 120 6.5 2. 267 123 1.9 2. 40 0 125 5 .4 2. 46 5 126 6.7... TEMP t 360_ 40 0_ 44 0_ 48 0_ 500_ 600_ 700_ 800_ 900_ 1000_ 120 0_ 0.0 21 2.00 r hg 33.03 122 1.1 34. 68 123 9.9 36. 32 125 8.8 37.96 127 7.6 38.78 128 7.1 42 . 86 13 34. 8 46 . 94 1383 .2 51.00 14 32. 3 55.07 14 82. 3 59.13 1533.1 67 .25 1637.5 20 .0 5.3 22 7.96 r hg 24 .21 122 0.3 25 .43 123 9 .2 26.65 125 8 .2 27.86 127 7.1 28 .46 128 6.6 31 .47 13 34. 4 34. 47 13 82. 9 37 .46 14 32. 1 40 .45 14 82. 1 43 .44 1533.0 49 .41 1637 .4 30.0 15.3 25 0.33 r... 11.309 128 3.9 12. 5 32 13 32. 5 13. 744 1381 .4 14. 950 143 0.9 16.1 52 148 1.1 17.3 52 15 32. 1 19. 747 1636.8 60.0 45 .3 29 2.71 r hg 7. 927 121 3 .4 8.357 123 3.6 8.779 125 3.5 9.196 127 3 .2 9 .40 3 128 3.0 10. 42 7 1331.8 11 .44 1 1380.9 12. 44 9 143 0.5 13 .4 52 148 0.8 14. 4 54 1531.9 16 .45 1 1636.6 70.0 55.3 3 02. 92 r hg 6.7 62 121 1.5 7.136 123 2.1 7.5 02 125 2.3 7.863 127 2 .2 8. 041 128 2.0 8. 9 24 1331.1 9.796 1380 .4 10.6 62 143 0.1 11. 5 24 148 0.5... (_F) 27 5.0 28 0.0 28 5.0 29 0.0 29 5.0 26 0.3 26 5.3 27 0.3 27 5.3 28 0.3 40 9 .43 41 1.05 4 12. 65 41 4 .23 41 5.79 385 .21 386.98 388.73 390 .46 3 92. 16 816.9 815.3 813.7 8 12. 1 810.5 120 2.1 120 2.3 120 2 .4 120 2.6 120 2.7 1.68 04 1.6511 1. 622 8 1.59 54 1.5689 300.0 320 .0 340 .0 360.0 380.0 28 5.3 305.3 325 .3 345 .3 365.3 41 7.33 42 3 .29 42 8 .97 43 4 .40 43 9.60 393. 84 400.39 40 6.66 4 12. 67 41 8 .45 809.0 803.0 797.1 791 .4 785.8 120 2.8 120 3 .4. .. 360_ 40 0_ 44 0_ 48 0_ 500_ 600_ 700_ 800_ 900_ 1000_ 120 0_ 320 .0 305.3 42 3 .29 r hg - - 1 .49 50 121 5.6 1.5985 1 24 2.6 1. 64 72 125 5 .2 1.87 34 1313 .2 2.083 1367 .2 2 .28 5 141 9.8 2. 48 3 14 72. 1 2. 678 1 5 24 .7 3.063 1631.3 340 .0 325 .3 42 8 .97 r hg - - 1.3 941 121 2.1 1 .49 41 123 9.9 1. 541 0 125 2.8 1.7569 1311.6 1.95 62 1366.1 2. 147 141 9.0 2. 3 34 147 1.5 2. 518 1 5 24 .1 2. 881 1630.9 360.0 345 .3 43 4 .40 r hg - - 1.3 041 120 8 .4. .. 16.0 72 121 8.6 16.897 123 7.9 17.7 14 125 7.0 18. 528 127 6 .2 18.933 128 5.7 20 .95 1333.8 22 .96 13 82. 4 24 .96 143 1.7 26 .95 148 1.8 28 .95 15 32. 7 32. 93 1637 .2 40 .0 25 .3 26 7 .25 r hg 12. 001 121 6.9 12. 628 123 6.5 13 . 24 7 125 5.9 13.8 62 127 5 .2 14. 168 128 4. 8 15.688 1333.1 17.198 1381.9 18.7 02 143 1.3 20 .20 148 1 .4 21 .70 15 32. 4 24 .69 1637.0 50.0 35.3 28 1.01 r hg 9.557 121 5 .2 10.065 123 5.1 10.567 125 4. 7 11.0 62 127 4 .2 11.309... 1. 741 9 1363.8 1.8118 1385.3 1.9 149 141 7.3 2. 083 147 0.1 2. 249 1 523 .0 2. 575 1630.0 40 0.0 385.3 44 4.59 r hg 1 .28 51 1 24 5.1 1.36 52 127 1.0 1 .47 70 1306.9 1. 548 0 1 329 .6 1.5 827 1 340 .8 1.6508 13 62. 7 1.7177 13 84. 3 1.8161 141 6 .4 1.9767 146 9 .4 2. 1 34 1 522 .4 2. 44 5 1 629 .6 42 0 .0 40 5.3 44 9.39 r hg 1 .21 58 1 24 2.5 1 .29 35 126 8.9 1 .40 14 1305.3 1 .46 97 1 328 .3 1.5030 1339.5 1.56 84 1361.6 1.6 3 24 1383.3 1. 726 7 141 5.5 1.88 02 146 8.7 . P 14. 696 15.0 16.0 17.0 18.0 19.0 20 .0 21 .0 22 .0 23 .0 24 .0 25 .0 26 .0 27 .0 28 .0 29 .0 30.0 31.0 32. 0 33.0 34. 0 35.0 36.0 37.0 38.0 39.0 40 .0 41 .0 42 . 0 43 .0 44 .0 45 .0 46 .0 47 .0 48 .0 49 .0 50.0 51.0 52. 0 53.0 54. 0 0.0 0.3 1.3 2. 3 3.3 4. 3 5.3 6.3 7.3 8.3 9.3 10.3 11.3 12. 3 13.3 14. 3 15.3 16.3 17.3 18.3 19.3 20 .3 21 .3 22 .3 23 .3 24 .3 25 .3 26 .3 27 .3 28 .3 29 .3 30.3 31.3 32. 3 33.3 34. 3 35.3 36.3 37.3 38.3 39.3 21 2.00 21 3.03 21 6. 32 219 .44 22 2 .41 22 5 . 24 22 7.96 23 0.57 23 3.07 23 5 .49 23 7. 82 240 .07 24 2 .25 24 4.36 24 6 .41 24 8 .40 25 0.33 25 2 .22 25 4. 05 25 5. 84 25 7.58 25 9 .28 26 0.95 26 2.57 26 4. 16 26 5. 72 267 .25 26 8. 74 27 0 .21 27 1. 64 27 3.05 27 4. 44 27 5.80 27 7.13 27 8 .45 27 9. 74 28 1.01 28 2 .26 28 3 .49 28 4. 70 28 5.90 180.07 181.11 1 84. 42 187.56 190.56 193. 42 196.16 198.79 20 1.33 20 3.78 20 6. 14 20 8. 42 210. 62 2 12. 75 21 4. 83 21 6.86 21 8. 82 220 .73 22 2.59 22 4. 41 22 6.18 22 7.91 22 9.60 23 1 .26 23 2.89 23 4. 48 23 6.03 23 7.55 23 9. 04 24 0.51 24 1.95 24 3.36 24 4.75 24 6. 12 247 .47 24 8.79 25 0.09 25 1.37 25 2.63 25 3.87 25 5.09 970.3 969.7 967.6 965.5 963.6 961.9 960.1 958 .4 956.8 955 .2 953.7 9 52. 1 950.7 949 .3 947 .9 946 .5 945 .3 944 .0 9 42 . 8 941 .6 940 .3 939 .2 938.0 936.9 935.8 9 34. 7 933.7 9 32. 6 931.6 930.6 929 .6 928 .6 927 .7 926 .7 925 .8 9 24 .9 9 24 .0 923 .0 922 .2 921 .3 920 .5 1150 .4 1150.8 11 52. 0 1153.1 11 54 .2 1155.3 1156.3 1157 .2 1158.1 1159.0 1159.8 1160.6 1161.3 11 62. 0 11 62. 7 1163 .4 11 64. 1 11 64. 7 1165 .4 1166.0 1166.5 1167.1 1167.6 1168 .2 1168.7 1169 .2 1169.7 1170 .2 1170.7 1171.1 1171.6 11 72. 0 11 72. 4 11 72. 9 1173.3 1173.7 11 74. 1 11 74. 4 11 74. 8 1175 .2 1175.6 26 .80 26 .29 24 .75 23 .39 22 .17 21 .08 20 .089 19.1 92 18.375 17. 627 16.938 16.303 15.715 15.170 14. 663 14. 189 13. 746 13.330 12. 940 12. 5 72 12. 226 11.898 11.588 11 .29 4 11.015 10.750 10 .49 8 10 .25 8 10. 029 9.810 9.601 9 .40 1 9 .20 9 9. 025 8. 848 8.678 8.515 8.359 8 .20 8 8.0 62 7. 922 (continued) Chapter. P 14. 696 15.0 16.0 17.0 18.0 19.0 20 .0 21 .0 22 .0 23 .0 24 .0 25 .0 26 .0 27 .0 28 .0 29 .0 30.0 31.0 32. 0 33.0 34. 0 35.0 36.0 37.0 38.0 39.0 40 .0 41 .0 42 . 0 43 .0 44 .0 45 .0 46 .0 47 .0 48 .0 49 .0 50.0 51.0 52. 0 53.0 54. 0 0.0 0.3 1.3 2. 3 3.3 4. 3 5.3 6.3 7.3 8.3 9.3 10.3 11.3 12. 3 13.3 14. 3 15.3 16.3 17.3 18.3 19.3 20 .3 21 .3 22 .3 23 .3 24 .3 25 .3 26 .3 27 .3 28 .3 29 .3 30.3 31.3 32. 3 33.3 34. 3 35.3 36.3 37.3 38.3 39.3 21 2.00 21 3.03 21 6. 32 219 .44 22 2 .41 22 5 . 24 22 7.96 23 0.57 23 3.07 23 5 .49 23 7. 82 240 .07 24 2 .25 24 4.36 24 6 .41 24 8 .40 25 0.33 25 2 .22 25 4. 05 25 5. 84 25 7.58 25 9 .28 26 0.95 26 2.57 26 4. 16 26 5. 72 267 .25 26 8. 74 27 0 .21 27 1. 64 27 3.05 27 4. 44 27 5.80 27 7.13 27 8 .45 27 9. 74 28 1.01 28 2 .26 28 3 .49 28 4. 70 28 5.90 180.07 181.11 1 84. 42 187.56 190.56 193. 42 196.16 198.79 20 1.33 20 3.78 20 6. 14 20 8. 42 210. 62 2 12. 75 21 4. 83 21 6.86 21 8. 82 220 .73 22 2.59 22 4. 41 22 6.18 22 7.91 22 9.60 23 1 .26 23 2.89 23 4. 48 23 6.03 23 7.55 23 9. 04 24 0.51 24 1.95 24 3.36 24 4.75 24 6. 12 247 .47 24 8.79 25 0.09 25 1.37 25 2.63 25 3.87 25 5.09 970.3 969.7 967.6 965.5 963.6 961.9 960.1 958 .4 956.8 955 .2 953.7 9 52. 1 950.7 949 .3 947 .9 946 .5 945 .3 944 .0 9 42 . 8 941 .6 940 .3 939 .2 938.0 936.9 935.8 9 34. 7 933.7 9 32. 6 931.6 930.6 929 .6 928 .6 927 .7 926 .7 925 .8 9 24 .9 9 24 .0 923 .0 922 .2 921 .3 920 .5 1150 .4 1150.8 11 52. 0 1153.1 11 54 .2 1155.3 1156.3 1157 .2 1158.1 1159.0 1159.8 1160.6 1161.3 11 62. 0 11 62. 7 1163 .4 11 64. 1 11 64. 7 1165 .4 1166.0 1166.5 1167.1 1167.6 1168 .2 1168.7 1169 .2 1169.7 1170 .2 1170.7 1171.1 1171.6 11 72. 0 11 72. 4 11 72. 9 1173.3 1173.7 11 74. 1 11 74. 4 11 74. 8 1175 .2 1175.6 26 .80 26 .29 24 .75 23 .39 22 .17 21 .08 20 .089 19.1 92 18.375 17. 627 16.938 16.303 15.715 15.170 14. 663 14. 189 13. 746 13.330 12. 940 12. 5 72 12. 226 11.898 11.588 11 .29 4 11.015 10.750 10 .49 8 10 .25 8 10. 029 9.810 9.601 9 .40 1 9 .20 9 9. 025 8. 848 8.678 8.515 8.359 8 .20 8 8.0 62 7. 922 (continued) Chapter. (continued) TEMP ( _F) ENTROPY (1) BTU/(LB.)(_R) ENTHALPY (1) (BTU/LB.) DENSITY (LB./CU. FT.) VOLUME (CU. FT./LB.) PRESSURE TEMP ( _F) Vapor s g Liquid s f Vapor h g Liquid h f Liquid I/v f Vapor V g psigpsia −59 −58 −57 −56 −55 − 54 −53 − 52 −51 −50 49 48 47 46 45 44 43 − 42 41 40 −39 −38 −37 −36 −35 − 34 −33 − 32 −31 −30 29 28 27 26 25 24 23 22 21 20 −19 −18 −17 −16 −15 − 14 5. 74 5.93 6.13 6.33 6. 54 6.75 6.97 7 .20 7 .43 7.67 7.91 8.16 8. 42 8.68 8.95 9 .23 9.51 9.81 10.10 10 .41 10. 72 11. 04 11.37 11.71 12. 05 12. 41 12. 77 13. 14 13. 52 13.90 14. 30 14. 71 15. 12 15.55 15.98 16 . 24 16.88 17. 34 17.81 18.30 18.79 19.30 19.81 20 . 34 20 .88 21 .43 18 .2 (2) 17.8 (2) 17 .4 (2) 17.0 (2) 16.6 (2) 16 .2 (2) 15.7 (2) 15.3 (2) 14. 8 (2) 14. 3 (2) 13.8 (2) 13.3 (2) 12. 8 (2) 12. 2 (2) 11.7 (2) 11.1 (2) 10.6 (2) 10.0 (2) 9.3 (2) 8.7 (2) 8.1 (2) 7 .4 (2) 6.8 (2) 6.1 (2) 5 .4 (2) 4. 7 (2) 3.9 (2) 3 .2 (2) 2. 4 (2) 1.6 (2) 0.8 (2) 0.0 0 .4 0.8 1.3 1.7 2. 2 2. 6 3.1 3.6 4. 1 4. 6 5.1 5.6 6 .2 6.7 43 .37 42 . 05 40 .79 39.56 38.38 37 . 24 36.15 35.09 34. 06 33.08 32. 12 31 .20 30.31 29 .45 28 . 62 27. 82 27. 04 26 .29 25 .56 24 .86 24 .18 23 .53 22 .89 22 .27 21 .68 21 .10 20 . 54 20 .00 19 .48 18.97 18 .48 18.00 17. 54 17.09 16.66 16 . 24 15.83 15 .43 15.05 14. 68 14. 32 13.97 13. 62 13 .29 12. 97 12. 66 43 .87 43 .83 43 .78 43 . 74 43.70 43 .66 43 . 62 43 .58 43 . 54 43 .49 43 .45 43 .41 43 .37 43 .33 43 .28 43 . 24 43 .20 43 .16 43 . 12 43 .08 43 . 04 42 . 99 42 . 95 42 . 90 42 . 86 42 . 82 42 . 78 42 . 73 42 . 69 42 . 65 42 . 61 42 . 57 42 . 54 42 . 48 42 . 44 42 . 40 42 . 35 42 . 31 42 . 26 42 . 22 42 . 18 42 . 13 42 . 09 42 . 04 42 . 00 41 .96 20 .1 −19.1 −18.0 −17.0 −15.9 − 14. 8 −13.8 − 12. 7 −11.7 −10.6 −9.6 −8.5 −7 .4 −6 .4 −5.3 4. 3 −3 .2 2. 1 −1.1 0.0 1.1 2. 1 3 .2 4. 3 5.3 6 .4 7 .4 8.5 9.6 10.7 11.7 12. 8 13.9 14. 9 16.0 17.1 18.1 19 .2 20.3 21 .4 22 .4 23 .5 24 .6 25 .6 26 .7 27 .8 590.0 590 .4 590.8 591 .2 591.6 5 92. 1 5 92. 4 5 92. 9 593 .2 593.7 5 94. 0 5 94. 4 5 94. 9 595 .2 595.6 596.0 596 .4 596.8 597 .2 597.6 598.0 598.3 598.7 599.1 599.5 599.9 600 .2 600.6 601.0 601 .4 601.7 6 02. 1 6 02. 5 6 02. 8 603 .2 603.6 603.9 6 04. 3 6 04. 6 605.0 605.3 605.7 606.1 606 .4 606.7 607.1 −0. 049 0 −. 046 4 −. 043 8 −. 04 12 −.0386 −0.0360 −.03 34 −.0307 −. 028 1 −. 025 6 −0. 023 0 −. 020 4 −.0179 −.0153 −.0 127 −0.01 02 −.0076 −.0051 −.0 025 .0000 0.0 025 .0051 .0076 .0101 .0 126 0.0151 .0176 . 020 1 . 022 6 . 025 0 0. 027 5 .0300 .0 325 .0350 .03 74 0.0399 .0 42 3 . 044 8 . 04 72 . 049 7 0.0 521 .0 545 .0570 .05 94 .0618 .06 42 1 .47 41 1 .47 13 1 .46 86 1 .46 58 1 .46 31 1 .46 04 1 .45 77 1 .45 51 1 .4 5 24 1 .44 97 1 .44 71 1 .44 45 1 .44 19 1 .43 93 1 .43 68 1 .43 42 1 .43 17 1. 42 9 2 1. 42 6 7 1. 42 4 2 1. 42 1 7 1 .41 93 1 .41 69 1 .41 44 1 .4 120 1 .40 96 1 .40 72 1 .40 48 1 .4 025 1 .40 01 1.3978 1.3955 1.39 32 1.3909 1.3886 1.3863 1.3 840 1.3818 1.3796 1.37 74 1.37 52 1.3 729 1.3708 1.3686 1.36 64 1.36 42 (continued) Chapter