Document 4QzppNNRBrM4Eny32y0dnBMNG

342 CHAPTER 20 1965 Guide And Data Book Table 22 .... Refrigerant 7.17 Properties of Superheated Vapor* (Concluded) Temp f f (At Set) 120 140 190 200 Abs Fr(wrt 190.0 pt) Goge Prtinr* 175.3 pd (Sol reap 93.13 F) . Abs Pressure 200.0 pd Gope Pressure 185.3 pd [Set reap 96.34 P) Abs Pressure 210.0 pd Goge Pressure 195.3 pd (Sat reap 99.43 f) Abs Presssue 220.0 ps - . - Abs Pi emu0 230.0 psi Goge Pressure 205.3 pd Gage Pressure 215.3 ptj (Sal Teap 102.42 F) (Sat reap 105^0 F) b .b *b * -- * b . (1.1802) (632.7) (1.1756) .(1.431) (633.0) (1.1713) (1.867) (633.2) (1.1671) (1-307) (633.4) (1.1631) 1.709 660.5 .2396 - 643.4 1.612 650.9 1.656 658.1 1.698 665.0 .1947 1.480 .2077 1.524 .2200 . 1.666 .2317 1.608 641.6 649.1656.4 663.6 .1996 .2121 .2240 1.400 1.443 1.485 1.526 639.4 647.3 654.8 662.0 J1917 .2167 1.870 1.449 645.4 1.1700 .1840 .2095 2.005 698.7 .3612 .2912 1.740 . 671.8 1.780 678.4 1.820 1.897 697.7 1.2429 .2537 .2641 .2840 1.648 1.687 1.725 1.799 670.4' 677.1 690.2 696.6 1.2354 1.564 .2464 1.601 .2569 . 1.638 .2672 1.675 .2771 1.710 669.0 675.8 682.6 689.1 695.5 1.2281 .2394 .2604 .2704 1.487' 1.524 1.594 1.629 667.6 674.5 687.9 694.4 1.2213 .2325 .2538 .2640 704.9 : 723.3 ' 2.274 741.3 1.3007 .3099 .3189 .8278 1.935 703.9 1.972 710.1- 2.009 2.046 . 722.4: 1.2935 .3029 .3120 .3209 .3296 1.836 . 1.872 1.942 1.977 .3534 - 2.154 740:5 .8467 - 2.046 702.9 709.2 721.5 727.6 733.7 739.8 1.2867 1.745 .2961 1.780 .3053 1.814 .3143 1.848 .3231 1.881 1.3317 ` 1.914 .3402 1.947 701.9 708.2 714.4 720.6 726.8 732.9 739.0 1.2801 1.663' .2896 , 1.696' .2989 1.729 .8079 1.762' 1.3255- - 1.826 ' .8340 1.857 700.9 713.5 719.8 732.1 738.3 1.2738 .2927 .3018 .3107 1.3195 .3281 (At Sat) 120 140 - 170. 180 100 220 240 260 - 270 - Abs Pressure 240.0 pd Abs Pressure 250.0 pd Abs Pressure 200.0 pd Go9* Pressure 225.3 pa Goge Pressure 235.3 pd Goge Pressure 245.3 pd (Sat reap 108.09 F\ . [Set Tamp )I0.S0F) ' . [Set Tamp 113.42 FI Abs Pressure 280.0 pd - Abs Preswre 300.0 pd Gage Pressure 265.3 psf Goge Pressure 283J pd. (Sol reap 118.45 F) [Set Tamp 12321 F) (1.253) .(633.6) (1.1502) 1.261 635.8 1.302 643.6- .1764 1.342 651.3 .1898 . 1.380 658.8 .2025 (633.8) (1.1555) 1.240 64i.5 1.1690 1.278 - 649.6 - .1827 1.316 657.2 .1966 (1.155) 1.182 1.220 1.257 (633.9) (1.1518) . (1.072) 639.5 1.1617 1.078 647.8 .1757 1.115 655.6 . .1689 . l.lSli (634.0) (1.1449) 635.4 1.1473644.0 .1621652.2 .. .1759. (0.999) 1.058 (634.0) (1.1383) 648.7 .1632 - 1.416 1.487 . 1.621 1.554 680.0 - .2369 693.3 .2577 1.486 692.2 .2517 ' 1.292 - 1.326 1.859 1.891 1.422 663.1 670.4 . 677.5 684.4 691.1 1.2014 -.2132 .2245 . .2354 .2458 1.184 1.317 . 1.249 1.279 1.309 660.1 667.6 674.9 6S1.9 688.9 1T18S8 1.091 :2Qll -1.128 .2127. .3.153 * .2239 .2346 1.211 6S6.9' 1.1767 664.7 672.2 .2014 1.651 1.714 725.1 : 7ii:7 .3049 . 1.640 724.3- .2993 : 1.453 . 1.514 1.672 697.7' 704.3 710.7 717.1 723.4 1.2560 .2658 .2754 ' .2847 .2938 . 1.339 1.367 1.896 1.424 - 1.451 695.6702.3 708.8 715.3 721.8 1.2449' 1.239 .2560 . 1.267' .2647- 1.294 .-2742 .2834 1.346 693.5 700.3 706.9 720.0 1.2344 .2447 ..2546 .2738 1.775 t 1.805 737.5 743.6 .3224 1.690 .8308 1.729 736.7 .8168 742.9' .8253 1.630 1.658 1.3027 736.0 .3115 742.2 .3200 1.478 728.1 1.2924 1.872 1.505 734.4 .3013 1.397 1.532 740.7 .8099- 1.422 726.5 1.2827 732.9 .2917 739.2 Table 23 .. . Refrigerant 744-(Carbon.Dioxide) Properties of Solid,,Liquid, and Saturated Vapor* Pressure Voiuae Dandtf . Ib/eu ' frrfbcrfpf** ft/lb f) - Btu/ib ' Entropy** ' . Bfu/(/b) (* . reap ' Pressure Vobnue Density ib/eu Enthalpy** ft/lb ft :8tv/tb Entropy** Btv/Vb) <fl ptia psig Vapor biA/ -147 -U0 2.14 25.56* 36.80 3.19 23.41* 34.60 99.60 -130 -110 6.85 u.n S' -109.4 .- 14.70 17.80 22.14 >7.65 .84.05 11.87* 9.13 . -.98.23 0.92* 6.86 97.66 0.02 6.69 97.56 4.72 7.67 2-80 . 06.90 19.39 2.82 90.16 85: -41.67 - 80 ;S0.70 .- 75 61.75 - TO 74.90 - 69.9 >75.1 27.00. 2.07 ' 95.78 -36.03 1.70 47.08 60.23 1.17 . 60.43. r.11. ..94.43 - 69:9 - 68 -.68 -- 64 62 =75.1' 78.69 82.42 88.29 90.49 60.43 -'63.93 67.75 . 71.72- 76.82 1.1670 1.109S 1.0S90 1.0100 0.9650 . 73.05 . 72.83 . 72.67 > - 58 S - 54 1} - 52 94.75 99.15 103.69 108.40 113.25 80.08 84.48 89.0393.73 98.68 0.9260 72.25 71.99 .8530 . 71.79 .8190 71.63 .780. 71.23 - 48 - 44 - to 123.45 134.81 145.87 102.60 108.78 114.13 119.64 131.20 0.7300' 70.97 .7200 70.7) 70.47 .6660 70.18 .6380 . 89.83 .6113 69.69 Uqwid Vapor liquid' Vapor A/ A */ - -123.3 128.2 -0.3214 44).4832 - .3163 .4691 -116.0 132.1 - .2988 . .4218 -113.1 ` 133.3 -".2904 .4145 -113.9. 123.4 -- 106.5 . : 136.3 -0.3898 -.2815 -.2730 -0.4124 -.4062 . . .2981 '.2902 ,, .3822- -104.5.- - 135.6 0.2742 -102.3 ' - 125.8 - .2810 - i .3665- - .2561- - .2494 :: .3508 . - 97.8 136.0. - .2433. .: .3508 - 11.9 ' - 10.1 - 9.1 136.3 138.6 138.7 - .0290 .3475 - .0243. . .3444 - 0.3429 - 6.4 - 6.6 - 4.6 - 3.6 - 3.7 - 1.8 - 0.9 0.0 - .0153 137.2 - .0131 137.6 137.7 .137.8 137.9 - .0048 0.0000 .3383 . .3368 .3285 ' ptia psig Vapor liquid Uqtdd Vapor Uqtdd Vapor i/v: b/ A*. . */ * -38 -32 -28 -24 . -20 158.15 171.17 184.97 199.57 316.03 143.48 156.60 170.80 184.90 200.35 0.5650 :5310 .4845 ' .4500 .4165 69.11 67.93 67.34 68.78 1.9 -6.67.4 9.3 138.1 0.000 0.3358 138.4 138.6 .0168 -16 231.33 216.65 0.2885 68.18 11.9 138.8 0.0253 0.8130 -12 348.62 332.86 .3590 66.67 12.9. 133.8 .0293 - 8 286.62 251.96 .3245 64.94 16.0 138.9 - 4 285.70 271.03 -.3118 64.31 .16.9 0 305.79 291.09 . .2906 63.63 16.6 .138.9 .0419 326.8- .312.1 8 348.9- 334.2 . !:.!?: 372.1 396.4 357.4 381.7 , - 431.8 ; 407.1 0.2708 .2520 .2350 :219S .2048 83.01 '61.61 . 60.90 ,-60.17 20.8 22.9 26.0 27.8 138.9 0.0462 0.3006 . 138.7 138.6 . .0591 S; 24 '443.4' 23 .28 . 478.3 ' 3S 505.3. 635.7 40 667.3 433.7 461.6 490.6 21.0 653.6 0.1910 -.1782 .1662 .1650 .1442 69.33 - 81.8 66.68 ' 34.3 67.77 88.8 66.93 39.8 66.99 41.8 138.3 138.0 137.7 127.3 -136.8 0.0634 .0730 - .0778 .0831 .0872 0.2885 44 600.4 665.7 0.1342 65.04 44.4 48 634.9 620.3 .uso 64.00 47.1 S3 .1163 62.99 49.9 60 708.3 693.6 .1080 61.92 63.8 80 747.4 732.7 .0995 50.78 66.7 138.1 0.0923 0.2745 134.6 133.4 132.2 .1026 .1030 .1128 61 783.1 0.0930 49.48 68.8 130.7 0.1193 0.2563 68 830.6 816.9 .0842 48.10 62.0 128.9 .1260 72 874.9 .0760 46.60 65.6 120.6 .1316 78 931.1 906.4 .0680 44.64 69.6 .122.9 .1390 064.8 42.19 74.0 119.0 .1460 87.8 1073.1 1057.4 .0345 28.96 97.1 97.1 .1880 * India of matnij Mow one ousted ttmc^faae. ** Bosod oa 0 far the atursted Dqtdd st --40 F. Refrigerant Tables and Charts 343 8^ visd-iunssw n-