Document aBgLLR02vx97qwbZ4aLXmaQLR

306 CHAPTER 20 1965 Guide And Data.Book Refrigerant Tables and GHarts raK[e 5 .... Refrigerant 13 (Monochtorotrifluoromethane) Properties of Liquid end Saturated Vapor* 307 . Premire-EnthaJpy Diagram for Refrigerant 13 Table 6 .... Refrigerant 13 (Monochlorotriftuoromethane) Properties of Superheated Vapor* : mp t. (At Pat) ' >180 -160 -140 -120 - 80 - Q0 - 40 - 20 0 20 40 60 80 too 1 120 160 Abs Pretsx/rK } pd Gaga Pnom 27.88 fa. Voc (5af Tamp -J 84.37 Ft. ft , , Abs Pressure 1*5 pd Gage Pressure 26.87 fa. Voc * (Serf ramp -J75.96F) y ;h ' Abe Pressure 2 pd . Gage Pressure 25A5 fa.'Voc (Sol ramp --169.62 F) ft . Abs Pressure 2-5 pd Gaga Pressure 23.83 fa. Voc (Sof Temp --164.47 F) h * Abs Pressure 3 pd Goga Pressure 23.81 fa. Vac (So* lamp -- td0.lt Ft y :h (28.05) 30.51 84.78 (40.23) (0.1705) 40.70 0.1722 43.02 : .1797 45.38 47.80 ' .1940 (19.22) 20.35 23.15 (41.18) (0.1658) 42:95 0.1719 45.33 .179347.76 -:1864 (14.70) (41.80) (0.1625) (11.95) (42.30) (0.1601) (10.088) 16.22 42.88 0.1662 12.14 42.81 0.1618 10.00 :'45.28 -.1736 - 45.22 :.1693 10.82 17.33 47.70 .1807 13.85 47.66 .1764 11.52 (42.73) (0.1581) 42.74 45.17 ' .1656 47.62 .1728 38.93 40.98 43.05 45.11 52.78 68.00 60.71 .2078 .2143 .2207 .2270 25.93 27.81 28.68 30.06 62.75 55.83 67.98 60.69 0.1933 .2000 .2130 .2192 19.42 20.46 - 21.49 22.63 62.72 56.81 67.96 60.67 0)1876 .1944 .2010' .2076 .2139; 14.69 16.52 16.35 17.18 18.00 - 50.15 62.69 66.28 57.93 60.65 0.1834 .1902 .1968 .2032 .2095 12.22 13.92 13.61 14:31 15.00 50.12 52.66 65.26 67.91 60.63 0.1799 .1866 .1997 '47.15 49.23 51.28 62.35 65.40 63.48 69.24 72.22 75.26 0.2331 .2392 .2449 .2510 .2569 : 31.43 32.81 34.18 35.64 36.91 63.47 69.23 72.21 76.25 0.2252 .2315 .2375 .2432 .2491 23.56 24.58 25.61 28.65 27.68 63.45 69.21 73.19 76.24 0.2200 .2201 .2320 .2379 .2436. IS.84 19.66 20.49 21.31 22.14 63.43 66.28 69.20 72.18 76.23 0.2156 .2217 ..2277 .2335 .2393 15.69 16.37 17.07 17.75 18:44 63.42 66.27 69.19 72.17 75.23 0.2121 .2182 - .2243 -.2360 67.46 59.50 61.56 63.62 65.67 78.36 81.53 88.04 91.37 .2680 .2734 .2788 .2843 39.66 41.03 42.40 -43.77 78.35 81.52 84.76 88.03 91.36 0.2547 .2603 .2657' .2710 .2764 28.71 29.74 80.77 31.79 32.82 78.34 81.61 88.02 91.36 0.2492 .2548 .2602. .2657 .2711 22.96 23.79 24.62 25.44 26.20 78.34 81.50 84.73 88.02 91.35 0.2450 .2504 -.2560 ..22666184 19.13 19.82 20.50 21.19 21.88 78.33 81.60 84.72 88.01 0.2414 .2471 .2579 Temp.-'. (At Sat) -100 0 100 200 Abs Pressure 4 pd - ' Abs Pressure 6 pd. Abi Pressure'8'pri ' ' Abs Pressure 10 pd - Gaga Press. 21.76 fa. Voc Gage Press. 17.70 fa. Voc Goga Frets. 36] fa.' Voc Goga Prett 9-56 fa. Voc -iSatTemp -152.91 Ft {Satjemp -- 7 42.06 F) (SofTemp --133.80 F) (Scf Temp --127.03 FJ Abs Pressute'15'pd Goga Pressure 0.3 pd {Sal Temp -- 113-92 f\- (7.722) .(43.60) (0.1550) (5.296) (44.57) (0.1509) (4.055) (46.47) (0.1481) (3.296) (46.12) (0.1459) (2.259) .(47.45) (0.1423) 45.07 0.1599 44.84 0.1517 8.612 47.54 ' .1673 : 6.705 47-87 .1591' ' 4.251 47.20 0.i033 8.376 47.02 0.1486 9.149 9.671 10.19 10.72 11.23 60.05 62.61 55.22 57.88 60.60 .1810 . 6.421 .1877 ! 6.772 .1942 ` 7.124 :2005 7.471 62.60 67.80 60.53 .1732 .1799 .1864 .1927 4.795 6.062 6.325 6.589 62:38 57.72 60.46 0.1605 .1674 .1742 :1807 .1871 3.819 4.034 4.248 4.460 49.64 62.27 57.64 60.39 0.1560 .1628 .1694 -.1763 .1827 2.368 2:518 3.665 2.811 2.955 49.29' ` 61.98 . 54.69' 67.43 60.21 0.1476 .1547 1 .1616 .1683 .1748 11.75 12.27 12.78 13.29 13.81 - 63.89 66.24 69.16 72.16 75.20 14.34 ' 14.85 * 15.37 15.88 16.41 16.92 17.43 78:31 81.48 87.99 94.73* 98.17. 0.2066 .2128 .2187 .2245 1 .2303 ! 8.515 9.204 0.2361 -.2416 .2470 .2525 : 12578 0.2830 -2882 * 9.549 '10.58 10.93 ill`,27' jll.62; 63.33 75.16 78.27. 01.31 94.70 98.16. .2110 "6.375 .2169 .2226 6.896 75.12 7.155 78.23 .2338 81.40 .2447 .2501 8.192 - 91.28 .2055 -.2113 .2170 0.2220 .2390 .2445 5.092 6.611 6.719 6.925 6.341 6.548 .2603 8.707 98.12 .2548 6.961 63.20' 66.08 69.02 72.0175.07 0.1889 .1951 .2010 .2069 .2127 78.19 81.37. 87.90 91.25 0.2184 .2241 .2295 .2348 .2401 0.2468 98.10 .2505 3.098 3.241 3.381 3.520 3.662 63.05' 0.1810 65.93 - .1872 . 68.89 .1932 71.90' 74.97' - .2050 3.801' 3.940 4.218 4.356 ' 78.10 81.29' ' 84.63 87.83' 91.18 0.2106 4.495 ! 94.68' 0.2376 4.634 "Reprinted inm Industrial and BngineeriaqChtmitti-it, VoL 44, Junuij 1922, p. 1SS. Copyright 1922 by the Aaoiau Chemical Society, *nd reprinted by pcmiuaio& of too copyright owner.