CHAPTER III REFRIGERANTS (Part 9)

4.98 36.92 .201 8.5 156.5 165.0 .018 .347 17 18 17.4 2.7 .02711 4.88 36.88 .205 9.0 156.5 165.5 .019 .347 18 19 17.8 3.1 .02714 4.78 36.84 .209 9.5 156.0 165.5 .020 .347 19 20 18.2 3.5 0.02717 4.68 36.80 0.214 10.0 156.0 166.0 0.021 0.346 20 21 18.6 3.9 .02720 4.69 36.76 .218 10.5 156.5 166.0 .022 .346 21 22 19.0 4.3 .02723 4.50 36.72 .222 11.0 155.5 166.5 .023 .346 22 23 19.4 4.7 .02726 4.41 36.68 .227 11.5 155.5 167.0 .025 .346 23 24 19.8 5.1 .02729 4.32 36.64 .231 12.5 154.5 167.0 .026 .346 24 25 20.2 5.6 0.02730. 4.24 36.60 0.236 13.0 154.5 167.5 0.027 0.346 25 26 20.6 5.9 .02735, 4.15 36.56 .241 13.5 154.0 167.5 .028 .346 26 27 21.0 6.3 .02737 4.07 36.53 .246 14.0 154.0 168.0 .029 .346 27 28 21.5 6.8 .02741 4.00 36.48 .250 14.5 154.0 168.5 .030 .346 28 29 21.9 7.2 .02744 3.93 36.44 .254 15.0 153.5 168.5 .031 .346 29 30 22.3 7.6 0.02746 3.86 36.40 0.259 15.5 153.5 169.0 0.032 0.346 30 35 24.6 9.9 .02760 3.52 36.20 .284 18.0 152.5 170.5 .038 .346 35 40 26.9 12.2 .02780 3.22 36.00 .311 21.0 151.0 172 0 .044 346 40 45 29.5 14.8 .02795 2.96 35.80 .338 24.0 150.0 174.0 .049 .346 45 50 32.5 17.8 .02810 2.71 35.60 .369 27.0 148.5 175.5 .055 .346 50 55 35.5 20.8 0.02825 2.49 35.40 0.402 30.0 147.5 177.5 0.061 0.347 55 60 38.7 24.0 .02840 2.28 35.20 .439 33.0 146.0 179.0 .067 .348 60 65 42.2 27.5 .02855 2.10 35.00 .476 36.5 144.5 181.0 .073 .349 65 70 45.8 31.1 .02875 1.94 34.80 .515 39.5 143.5 183.0 .079 .350 70 75 49.7 35.0 .02890 1.79 34.60 .559 43.0 142.0 185.0 .086 .351 75 80 53.9 39.2 0.02910 1.66 34.35 0.602 46.5 140.5 187.0 0.092 0.352 80 85 58.6 43.9 .02930 1.54 34.10 .649 50.0 139.0 189.0 .098 .353 85 86t 59.5 44 8 .0293$ 1 52 34 10 .658 50 5 139 0 189 5 .099 354 set 90 63.3 48.6 .02950 1.42 33.90 .704 53.5 137.5 191.0 .105 .356 90 95 68.4 53.7 .02965 1.32 33.70 .758 57.5 136.0 193.5 .112 .358 95 100 73.7 59.0 0.02990 1.23 33.45 0.813 61.0 134.5 195.5 0.118 0.359 100 105 79.3 64.6 .03005 1.14 33.25 .877 65.0 133.0 198.0 .125 .360 105 110 85.1 70.4 .03030 1.07 33.00 .935 69.0 131.0 200.0 .132 « .362 110 115 91.4 76.7 .03050 0.990 32.80 1.01 73.0 129.5 202.5 .139 .364 11,'-. 120 98.0 83.3 .03075 .926 32.50 1.08 77.0 127.5 204.5 .147 .367 120 125 104.8 90.1 0.03095 0.867 32.30 1.15 81.5 126.0 207.5 0.154 0.369 125 130 112.0 97.3 .03125 .811 32.00 1.23 86.0 124.0 210.0 .161 .371 130 135 119.3 104 6 .03145 .760 31.80 1.32 90.5 122.0 212.5 .169 .375 135 140 126 8 112 1 03175 .716 31 50 1 40 95 0 120 5 215.5 .176 .377 140 andard atmo,»phere (29.82 REFRIGERANTS— TABLES 75 TABLE XXXI.— SATURATED METHYL CHLORIDE (CH3 CI) VAPOR Calculated in English Units by Starr from work of Ohnes and Hoist. ''Fractical Refrigerating Engineers' Pocketbook" Published by Nickerson & Collins Co. Chicago. Temp. Abs. Press. Heat Heat Spec. VoL Density Deg. Lbs. per Content of of Vapor- Cu. Ft. Lbs. per Fahr. Sq. In. Liquid ization per Lb. Cu. Ft. -40 6.96 -34.0 183.3 12.57 0 07955 -35 7 60 -31.5 183.0 11.00 0.0909 —30 9 00 -29 0 182.6 9.70 0.103 -25 10.20 -26 7 182.0 8 60 0.1162 -20 11.80 -24.5 181.4 7.80 0.1282 -15 13 00 -22 3 180.9 7.00 0 1428 -10 15 10 -20 0 180.3 6.25 0 1 600 - 5 16.80 -17.5 180.0 5.60 0 1 785 0 18 00 -15 1 179.2 5 05 0.1980 5 20.70 -12.8 178.3 4.53 0.2207 10 23 00 -10 2 177.8 4.15 0 . 2409 15 24 90 - 8 0 177.03 3.70 0.2702 20 28 50 - 5 6 176.05 3.25 0 . 3076 25 32 00 - 3.2 175.8 2.90 0.3448 30 35.00 - 1.6 174.8 2.71 0.3690 32 36.62 0 0 174.6 2.67 0.3745 40 42 90 + 3.7 173.0 2.25 0.4444 50 46.50 + 8 5 171.0 1.94 0.5154 60 62 00 + 13 2 169.0 1.62 0 9803 65 68.00 15.5 167.85 1.50 0.6666 70 73.10 17 8 166.8 1.39 0.7194 75 80 00 20.2 165.6 1.27 0 7842 80 87.00 22 5 164.2 1.15 0 8695 85 94.30 25 0 163.0 1.05 0.9523 SO 104.00 27.2 161.6 0.995 1.0051 95 110.10 29 6 160.4 0.938 1 0661 100 119.50 31.8 158.8 0.855 1 1695 110 137.50 36.3 156.1 0.77 1.2987 NOTE. — To get gauge pressures 14.7 lbs. are subtracted from tbe absolute pres- sures given in the tables. When the absolute pressure is below 14.7 lb. the absolute pressure is subtracted from 14.7 lbs. and _ this result is multiplied by 2.0355 (for approximate results, 2.0 may be used). This gives the vacvium in inches of mercury below the atmospheric pressure of 14.7 lbs. 76 HOUSEHOLD REFRIGERATION TABLE XXXII.— PROPERTIES OF SATURATED VAPOR OF PROPANE— CaHg Linde Air Products Company Laboratory. Refrigeration Engineering, June 1926. A. S. R. E. Data Book. Temp. Pressure Volu me De isity Heat Content Entrop.v Temp. •F dbove 0° F From 0° F. »F. Abs. Gage Liquid Vapor Liquid Vapor Liquid Latent Vapor Liquid Vapor lb/in,' Ib./in • ft.Vlb. ft.'/lb Ib./tl." Ib./It.' Btu./lb. Btu /lb. Btu./lb Btu./lb "F Btu/lb°F t P gP V V liv l/V h + L = H s 5 t -75 0.37 17.0* 0 02660 14.5 37.59 0 0690 -39 5 190 5 151 0 -0 092 0 404 -75 -70 7.37 14.9* 02674 12 9 37.40 0775 -37.0 189 5 152 5 -0.086 400 -70 -65 8.48 12 7* 02688 11 3 37 20 0885 -34.5 188 0 153 5 -0 080 397 -65 -60 9 72 10.1* 02703 9.93 37 00 111 -32.0 187 0 155 0 -0 074 .393 -60 -55 11 1 7.3* 02717 8 70 36.80 115 -29.0 185,5 156 5 -0 067 391 -55 -50 12.6 4.3* 0.02732 7.74 36.60 0 129 -26.5 184.5 158.0 -0 061 0 389 -50 -45 14.4 0 6* 02748 6.89 36 39 145 -24.0 183 0 159 0 -0 055 386 -45 -40 16.2 15 02763 6.13 36 19 163 -21.5 181 5 160 0 -0 049 384 -40 -35 18 1 3 4 02779 5 51 35 99 181 - 19 0 ISO 0 161 0 -0 042 382 -35 -30 20 3 5.6 02795 4 93 35.78 203 -16.0 179 0 163 0 -0 036 380 -30 -25 22 7 8.0 0.02811 4 46 35.58 0.224 -13.3 177.5 164 0 -0 030 0 378 -25 -20 25 4 10 7 02827 4.00 35,37 250 -11 0 176 0 165 0 -0 024 377 -20 -15 28 3 13.6 02844 3.60 35.16 ,278 - 8.0 175 0 167 0 ■ -0 018 .375 -15 -10 31 4 16 7 02860 3 26 34.96 307 - 5,5 173 5 IBS 0 -0 012 374 -10 - 5 34 7 20 0 02878 2.97 34 75 337 - 2.5 172 0 169 5 -0 006 372 - 5 0 38.2 23.5 0 02895 2.71 34.54 0.369 0.0 170 5 170.5 0 000 0.371 0 + 1 39 0 24.3 02899 2.66 34.49 376 0.5 170 5 171 0 001 371 + 1 2' 39 7 25 0 02903 2 61 34 45 383 10 170 5 171 5 .002 .371 2 3 40.5 25.8 02906 2.57 34.41 389 15 170 0 171 5 003 371 3 4 41 3 26 6 02910 2 52 34 37 396 2.0 170 0 172 0 004 371 4 51 42.1 27.4 0 02913 2 48 34 33 0 403 + 3 0 169 5 172 0 +9 006 0.370 St 6 42.9 28.2 02916 2.43 34 29 411 3 5 169 0 172 5 007 .370 6 7 43.7 29.0 02920 2 39 34 25 418 4 0 168 5 172 5 008 370 7 S 44.5 29 8 02924 2.35 34.20 426 4 5 168 5 173 0 009 370 8 9 45.3 30 6 02927 2 31 34 16 433 5.0 168 0 173 0 010 370 9 10 46.1 31.4 0 02931 2.27 34 12 0.441 5.6 168 0 173 5 0 012 0 370 10 11 47.0 32 3 02935 2 23 34 07 448 6.0 168 0 174 0 013 370 11 12 47.9 33.2 02939 2.19 34 03 4.56 6 5 167 5 174 0 014 .370 12 13 48 8 34.1 02943 2 15 33 98 465 7.5 167 0 174 5 015 370 13 14 49 7 3a 0 02946 2 11 33 94 474 8.0 166 5 174.5 016 370 14 IS 50 6 35 9 0 02950 2 07 33 90 0 483 8.5 166.5 175 0 0 018 0.369 IS 16 51 C 36 9 02954 2 04 33 85 491- 9,0 1(')6 0 175 0 019 369 16 17 52 5 37 8 02959 2 00 33 80 500 9,5 166 0 175.5 .020 369 17 18 53 5 38 8 02963 1 97 33 75 .509 10 0 165 5 175 5 021 369 18 19 54.5 30.8 02966 1.93 33.71 518 10.5 165 5 176 0 022 369 19 20 55.5 40 8 0 02970 1.90 33.67 0.526 11.0 165.0 176 0 0 024 0 368 20 25 00 9 46 2 02991 1 74 33 43 .575 14,0 163 5 177.5 030 ,368 25 30 66 3 51 6 03012 1 60 33.20 625 17.0 162 0 179 0 .035 366 30 35 72 0 57 3 03033 1 48 32 97 .676 20.0 160 5 180,5 041 .366 35 40 78 0 63 3 03055 1 37 32 73 730 23.0 1.59.0 182 0 047 366 40 45 84 6 69 9 0 03078 1.27 32 49 0.787 26.0 157,5 183.5 0 053 0 365 45 50 91 8 77 1 03102 1 18 32 24 .847 29 0 1.56 0 185 0 059 .365 50 55 99 3 84 6 03125 1 10 32 00 909 32.0 1,54 5 186 5 .065 365 55 60 107 1 92.4 031.50 1 01 31.75 990 35.0 153 0 188 0 070 .364 60 65 115 4 100 7 03174 0.945 31.50 1 06 38.0 151 5 189.5 .076 .364 65 70 124 0 109 3 0 03201 0.883 31.24 1.13 41.0 149 5 190 5 0 082 0.364 70 75 133 2 118 5 03229 825 30 97 1 21 44.0 148 0 192 0 088 364 75 80 142 8 128 1 03257 .770 30.70 1 30 47.5 140 0 193 5 093 .364 80 85 153 1 138 4 03287 722 30.42 1 39 50.5 144 5 195 0 099 .364 85 66 1 155 3 140 5 03292 717 30 38 1 40 51.0 144 0 195 0 100 364 set 90 164 0 149 0 0 03317 0.673 30.15 1 49 54.0 142,5 196.5 0 105 0 364 90 95 175 0 160 0 03348 .632 29.87 1,58 57.0 140 5 197 5 111 364 95 100 187 0 172 0 03381 591 29 58 1 69 60.5 138 5 199.0 116 ,363 100 105 200 0 185 0 03416 553 29 27 1 81 63.5 136 5 200 0 122 363 105 110 212 0 197 0 03453 520 28.96 1 92 67.0 134 0 201 0 128 363 110 115 226 0 211 0 0 03493 0.4S8 28.03 2 05 70.5 131 5 202 0 0.134 0 363 115 120 240 0 225 0 03534 459 28.30 2 18 73 5 129 0 202 5 .140 .363 120 125 254 0 239 0 03.575 432 27 97 2 31 77.0 126 5 203 5 .145 361 125 B (29.82 iu. - 14,696 Ibs./sq. in. abs.) REFRIGERANTS— TABLES n TABLE XXXIII. -PROPERTIES OF SATURATED VAPOR OF SULPHUR DIOXIDE— SO2 L avid L . Fiske, Urba la. III. —1925. A. S . R. E . Data Book. Tem Pressure Volume Deosity Heat Content Above— 40' Aba. Gage Liquid Vapor Liquid Vapor lb. /ft.' Liquid Latcntt Vapor "V. lb./in.» lb. /in.' ft.Vlb. ft.Vlb. lb./ft.> Btu./lb. Btu./lb. Btu./lb. i P gp 0 V I/O i/v h + £ = H -40 3 . 136 23.54* 0.010440 22.42 95.79 0.04460 0.00 178.61 178.61 -35 3.693 22.41* .010486 19.23 95.36 .05200 1.45 177.82 179.27 -30 4.331 21.10* .0105.32 16.56 94.94 .06039 2.93 176.97 179.90 -25 5.058 19.03* 0.010580 14.31 94.52 0.00988 4.44 176.06 180.50 -20 5.883 17.93* .010627 12.42 94.10 .08119 5. 98 175.09 181.07 -15 6.814 10.05* .010674 10.81 93.68 .09250 7.56 174.06 181.62 -10 7.863 13.01* .010721 9.44 93.27 .1025 9.16 172.97 182.13 - 5 9.0.38 11.52* .010770 8.28 92.85 .1208 10.79 171.83 182.62 0 10.35 8.85* 0.010820 7.280 92.42 0.1374 12.44 170.63 183.07 1 10.63 8 . 27 * .010830 7.099 92.33 .1408 12.79 170.38 183.17 2 10.91 7.34* .010810 6.923 92.25 .14.14 13.12 170.13 183.25 3 11.20 7.11* .0108.50 6.751 92.16 .1481 13.45 169.88 183.33 4 11.50 6..W* .010800 6.584 92.06 .1591 13.78 169.63 183.41 St 11.81 5.87* 0.010870 6.421 92.00 0,1558 14.11 169.38 183.49 6 12.12 5.24* .0108.80 6.266 91.91 .1596 14.45 169.12 183.57 7 12.43 4.61* .010890 6.114 '91 .83 .1628 14.79 168.86 183.65 '8 12.75 3.96* .010900 5.007 91.74 .1670 15.13 168.60 183.73 9 13.08 3.29* .010910 5.822 91.66 .1717 15.46 168.34 183.80 10 13.42 2.59* 0.010920 5.682 91.58 0.1760 15.80 168.07 183.87 11 13.77 1.88* .010930 5.548 91.49 .1803 16.14 167.80 183.94 12 14.12 1.17* .010940 5.417 91.41 .1846 16.48 167.53 184.01 13 14.48 0.44* .0109.50 5.289 91.33 .1890 16.81 167.26 184.07 14 14.84 .14 .010960 5.164 91.24 .1936 17.15 166.97 184.14 15 15.21 .51 0.010971 5.042 91.16 0.19S3 17.49 166.72 184.21 16 15.59 .89 .010981 4.926 91.07 .2030 17.84 166.44 184.28 17 15.98 1.28 .010992 4.812 90.98 .2078 18.18 166.16 184.34 18 16.37 1.67 .011003 4.701 90.89 .2127 18.52 165.88 184.40 19 16.77 2.07 .011014 4.593 90.80 .2177 18.86 165.60 184.46 20 17.18 2.48 0.011025 4.487 90.71 0.2228 19.20 165.32 184.52 21 17.60 2.90' .011036 4.386 90.62 .2280 10.55 165.03 184.58 22 18.03 3.33 .011047 4.287 90.53 .2332 19.90 164.74 184.64 23 18.46 3.76 .011058 4.190 90.44 .2387 20.24 164.45 184.69 24 18.89 4.19 .011070 4.096 90.33 .2441 20.58 164.16 184.74 25 19.34 4.64 0.011082 3.994 90.24 0.2404 20.92 163.87 184.79 26 19.80 5.10 .011093 3.915 90.15 .2559 21.26 163.58 184.84 27 20.26 5.56 .011104 3. 829 90.06 .2611 21.61 163.28 184.89 28 20.73 6.03 .011116 3.744 89.96 .2671 21.96 162.98 184.94 29 21.21 6.51 .011128 3.662 89.86 .2731 22.30 162.68 184.93 30 21.70 7.00 0.011140 3.581 89.76 0.2800 22.64 162.38 185.02 31 22.20 7.50 .011152 3.503 89.67 .2854 22.98 162.08 185.0«> 32 22.71 8.01 .011164 3.437 89.58 .2909 23.33 161.77 185.10 33 23.23 S.53 .011176 3.. 3.55 89.48 .2980 23.68 161.46 185.14 34 23.75 9.05 .0111.88 3.283 89.39 .3046 24.03 161.15 185.18 35 24.28 9.58 0.011200 3.212 89.29 0.3113 24.38 160.84 185.22 36 24.82 10.12 .011212 3.144 ,89.18 .3181 24.72 160.53 185.25 37 25.39 10.69 .011224 3.078 S9.09 .3249 25.07 160.21 185.28 38 25.95 11.25 .011236 3.013 89.00 .3319 25.42 159.89 185.31 39 26.52 11.82 .011248 2.949 ,88.90 .3391 25.77 159.57 185.34 40 27.10 12.40 D. 011260 2.887 88.81 0.3464 26.12 159.25 185.37 41 27.69 12.99 .011272 2.827 88.71 .3538 26.47 158.93 185.40 42 28.29 13.59 .011284 2.769 88.62 .3611 26.81 158.61 185.42 43 28.90 14.20 .011296 2.712 88.52 .3687 27.16 158.28 185.44 44 29.52 14.82 .011308 2.656 88.43 .3765 27.51 157.95 185.46 45 30.15 15.45 9.011320 2.601 88.34 0.3844 27.86 157.62 185.48 ' 46 30.79 16.09 .011.332 2.548 88.24 .3925 28.21 157.29 185.50 47 31.44 16.74 .011344 2.497 88.15 .4005 28.56 156.96 185.52 48 32.10 17.40 .011356 2.446 88.05 .4088 28.92 156.62 185.54 49 32.77 18.07 .011368 2.397 87.96 .4172 29.27 156.28 185.55 50 33.45 18.75 D. 01 1380 2.348 87.87 0.4259 29.61 155.95 185.56 ' 51 34.15 19.45 .011392 2.302 87.78 .4345 29.96 155.61 185.57 52 34.86 20.16 .011404 2.256 87.67 .4433 30.31 155.27 185.58 53 35.58 20.88 .011416 2.2U 87.60 .4523 30.66 154 93 185.59 54 36.31 21.61 .011428 2.167 S7.51 .4615 31.00 1.54.. 59 185.59 • Inches of mercur>' below one standard atmosphere r29 92 in.) 14.fi9tf lb. nb^ t For Internal Latent heat see Re. Eng. Vol. II. No G.; p. 235. (Dec 1924 j S Standard ton temperatures. 78 HOUSEHOLD REFRIGERATION TABLE XXXIII.— PROPERTIES OF SATURATED VAPOR OF SULPHUR 'DIOXlBE—S02—(.CanH7iued) Tern. Pressure Vok me Density Heat Content Above — iO" "F. Abs. Ib./in.' Gage lb./in.> I.iquul ft.Vlb. V.ip.,r ft.Mb. Liquid Ib./ft.J Vujior Ib./ft.i Liquid Btu./lb. Latent Btu./lb. Vapor Btu./lb. t 55 P 8P 22.35 V V 1/v 1/V h + L = H 37.05 0.011440 2.124 87.41 0.4708 31.36 154.24 185. 6« 56 37.80 23.10 .011452 2.083 87.31 .4801 31.72 153.89 185.61 57 38 56 23.86 .011464 2.043 87.22 .4894 32.08 153.54 185.62 5S 39.33 24.63 .011476 2.003 87.13 .4992 32.42 153 . 19 185.61 59 40 , 12 25.42 .011488 1.964 87.04 .5092 32.76 152.84 185.60 60 40.93 26.23 0.011500 1.926 86.95 0.5194 33.10 152.49 185.59 61 41.75 27.05 .011512 1.889 86.86 .5294 33.44 152.14 185.58 62 42.58 27.88 .011524 1.853 86.77 .5396 33.79 151.78 185.57 63 43.42 28.72 .011.530 1.816 86.68 .5507 34.14 151.42 185.56 64 44.27 29.57 .011548 1.7S3 86.59 ^5609 34.49 151.06 185.55 65 45.13 30.43 0.011500 1,749 86.50 o'5717 34.84 150.70 185.54 66 46.00 31.30 .011.572 1.716 86.41 .5827 .35 . 19 150.34 185.53 67 46.88 32.18 .011.585 1.683 86.32 .5943 35.54 149.98 185.52 68 47,78 33.08 .011598 1 .6.-.2 86.22 .60.54 35.88 149.62 185.50 69 48.69 33.99 .011611 1.621 86.12 .6170 36.23 149.25 185.48 70 49.02 34.92 0.011626 1.590 86.02 0.6290 36.58 148.88 185.46 71 50.57 35.87 .011639 1.557 85.92 .6423 36.93 148.51 185.44 72 51.54 36.84 .011652 1.532 85.82 .6527 37.28 148.14 185.42 73 52.51 37.81 .011660