CHAPTER III REFRIGERANTS (Part 8)

1.14 33.23 .877 80.0 139.0 219.0 .151 385 135 140 92 6 77.9 .03032 1.07 32.98 .934 83.6 137.8 221.0 157 .386 140 iaphere<29.82 in. " 14.696 Ibe./aq. in. aba.) REFRIGERANTS— TABLES 71 PROPERTIES OF SATURATED VAPOR OF SEVERAL REFRIGERANTS Starr, Practical Refrigerating Engineers' Pocket Book, Nickerson & Collins Co. TABLE XXin.— ClAHBON BISULPHIDE— CSi TABLE XXIV.— CABBON TETRACHLORIDE, C CU Ttmp Preaure Volume Density Heat Content above 32° K | Vupur \ apor Abjo- Oajte Liquid Latent Vapor" op 11, /Hi ' vac. fl '/Ih rt /U)>, ntu /lb Btu /lb ntu /lb ( P g P' V IJV h + L = H 0 1 10 27,7 53 70 0 0180 -8.00 105 5 150 90 St 1 28 27 32 48 07 0 0208 —7.20 165 0 157 80 10 1 4ti 26 95 43 47 0230 -5 60 104 . 5 15S 90 15 1 67 20 52 38 91 0257 -4 40 104 0 159.00 20 1 89 2(i 07 34 84 0287 -3 00 103 2 100 20 25 2 11 25 63 32.10 0 0324 -1 82 162.9 161 08 30 2 30 25.11 29 49 0339 -0 .50 102 2 101 70 35 2 47 24 89 28 .32 0353 0 00 102 0 102 00 40 3 03 23 75 23 .52 0425 + 2 0.-, 101 2 103.25 •45 3 40 23 00 22 00 0454 2 40 100 7 103 10 SO 3 90 21.95 20 GO 0 0482 4.24 160.0 104.24 55 4 40 20 9S 19 20 0.i21 5. SO 1.59.8 105.0(1 60 4.95 19 84 IS 00 0555 7.20 159.2 100 40 65 5 40 18 93 15 00 .0660 8.50 158 S 107 30 70 5 85 18 03 13 20 0758 9 80 1.58.1 107 90 75 G.50 16 09 11 SO 0S74 10 SO 1.57 5 105,30 80 7.30 15.07 10 40 0.0901 11.70 1.56.9 108.00 85 S 21 13 21 9,80 1020 12 GO 150.2 108 8(1 86f 8 40 12 82 9 15 .1058 12 84 156 1 168 94 90 9 15 11 29 8 30 1204 13 80 153 0 109,40 95 10 00 9 54 7 00 1315 15 00 155 0 170 00 100 11 OS 7 37 7 03 0 1.309 IG 15 1.54 4 170. 55 105 12 30 4 89 G 40 1502 17 40 1.53 S 171.20 110 13 50 2 44 5 SO 1724 18,30 1,53.2 171. ,50 114 r, 14 70 0 no 5 4r. 1834 19 10 152 0 171.70 !ll5 14 80 0 lot 5 40 1851 19 25 152 6 171 85 120 16 10 1 40t 5 loio 1960 20.01 1.52 0 172 01 T-vn Pre«ure \V>lum( \ apor Density Vapor Heat Content above 32° V. Abso- Guee Liquid Latent Vapor '1- 11. /in : v„c rt vib It /lb • Btu /lb. Blu./lb Otu./lb t P gP' V 1/V h + L = H 20 0 40 29 1 09 5 0.014.38 -2 00 94.45 92 45 25 50 2S,8 01 0 01039 -1.2(J 91 00 92.80 30 GO 28 7 .53 0 01886 -0 25 93 70 93 45 32 64 28 6 52 0 01917 0 00 93.00 93.60 40 84 28 2 10 0 02500 + 1 GO 93 20 94 SO 45 0 05 28 0 35 0 0.02857 2.58 92.90 95.48 52 1 07 27.7 34 0 .03113 3.58 92 GO 96. IS 9G 70 55 1 25 27,4 27,0 03703 4.40 92 30 00 1 42 27 0 24.0 04166 5 95 92.20 98. 15 05 1 00 26 7 21 5 04651 6 .50 91 70 98 2U 70 1 85 26.2 19.5 0.05128 8.20 91 40 99.00 75 2.15 25 . 5 17 5 0,5714 8. 50 91.05 99 , 53 SO 2.40 25.0 10 0 .00345 9.80 90.07 99.87 85 2 70 24 4 14 5 00890 10.60 90 04 100 04 86}* 2 78 24 2 14 2 07037 10 80 90 04 100 83 90 3 12 23,5 13 0 07092 11,00 90.02 101 02 95 3.60 22 6 11.0 0 0909 12,40 89 70 102.10 100 4 00 21,8 10.0 .1000 13,4(1 89 41) 102 . SO 105 4 42 20 9 9 0 nil 14 00 S9 20 103.80 110 4.S9 20,1 8 5 1176 15 80 SS 70 104.50 115 5.35 19.1 8 0 12.50 10 95 88 30 105.25 120 5.95 17.8 7 5 0.1333 18.00 87 9O:lO5.90l 125 0,50 16.7 7 0 1428 18.90 87 . 50 106.40 107.0.5; 130 7 20 15 2 G 3 1587 19.95 87.10 135 7 90 13.9 5 5 1818 20.99 86 70 107.69 140 8 05 12 3 4 8 2006 21 40 86 32 107.78 170 14 70 0 2.8 0 3571 20 90 83 00 109 90 TABLE XXV.— CHLOROFORM— CH Cls TABLE XXVII.— NITROUS OXIDE— N2O t P «P* V 1/V h L .V* 20 0 08 29 76 ,50,00 0.02012 -4 00 121 00 117 fiO 25 1.00 27 83 44, (K) .0227 -2.5 120 20 117 70 32 1.15 27 . ,58 ,38 10 02626 0 00 120 00 120 00 ,50 2 03 25 79 23 65 04232 4 19 118 87 123 00 68 3 15 23.51 IS 50 10.50 06.505 8 40 117 14 125 54 86t 4 80 20 15 0 0952 12 63 115 38 128 0) 104 7.52 14 61 7 14 1403 16 SO 113 03 130.49 122 10 30 8 96 5 (h; 1979 20 13 111 83 131 90 140.5 14 70 0 00 4 95 2200 23 70 109 00 132 70 TABLE XXVI.— ETHYL ETHERS— (C2H6)20 t P gP V 1/V h L H' 0 1 3 27 . 28 38 0 0.0203 -18 00 171 0 1,53 (K) 5} 15 26 87 35 0 0285 -15 00 170 8 155 80 10 1.8 2G 26 32 5 .03.52 -12.00 170.4 1,'.8.43 15 ■2.2 25 , 40 30 0 0332 -9.50 170 2 101.70 20 2.5 24.84 27.0 .0372 -6.50 170.0 103 ,50 25 2.9 24 03 24 3 0.0417 -4.00 169.6 165.60 30 3 4 23. (X) 21 4 ,0408 -1.50 169.4 167.90 35 3.9 22 00 19 3 0518 + 1.40 168.8 170.20 40 4.4 21 09 17.0 .0588 4.00 168 4 172.40 45 4.9 19 97 15 0 .0666 6.60 168.0 174.60 SO 5.5 18.72 13 2 0 0757 9.57 167.6 177.17 70 8.8 12 05 7.S . 1280 20 04 165.4 185 44 75 9 8 10 02 7 0 .1430 23.40 1134 8 188 20 80 10 9 7 , 33 6 2 1020 20.40 101 2 190 (ill 85 12.2 5.09 5 5 1800 29.00 103 S 192 Ml 86- { 12 3 4 62 5 4 1880 29.50 163 5 193' 00 90 13.4 2.72 5.1 0.1960 31.50 163 0 194 . 50 95 14 7 0.(K1 4 8 .2130 .34 OC 162 2 196 20I 100 10 0 1 3t 4.5 2220 36 .50 161 5 197 50 Te.np. Pressure Volume Density Heat Latent Abso- G.ige Liquid Vapor Liquid Vapor °F Ib./in.i lb,/in.= tt.'/lb. ft.'/lb. Ib./tt.' lb,/ft.' Btu.,,b. ( P gP' V ■ V 1/v' 1/V L -130 14 2 0 5 0.01232 5.940 81.17 0.165 162.3 -121 19.6 4 9 .01248 4.370 80.13 23 168. 9 - 112 26,8 12 0 .01264 3.200 79.11 .30 165.0 -103 35,5 20 S .01280 2.480 78 . 12 .40 162.3 -94 47,3 32.6 .01290 1.8S0 77.16 .53 158.9 -85 59.6 44.9 0.01312 1.510 76 22 0.66 155.0 -76 75.0 60.3 .01314 1 . 220 76.10 0.82 150.7 -67 92.3 77.6 .01370 0.9990 72.67 1.00 148.9 -.58 113 0 98 3 .01408 .8270 71.02 1.20 145.8 -49 135.0 120 3 .01440 .0900 09.44 1.40 142.5 -40 160.0 -145.3 0.01472 0.6000 67 93 1.65 139.1 -31 190 0 175 3 .01.504 . 5120 00.49 1.95 135.0 — 22 223 . 0 208.3 .01530 .4430 05.10 2 25 132.3 -13 257.0 242.3 .01,508 3950 63,77 2 50 129.0 -4 295.0 280.3 .01000 .3470 02 50 2.85 125 2 }+5 333.0 318 3 0 01632 0 3080 61 27 3 25 121 4 14 375.0 360.3 .01680 .2690 59 , 52 3 70 116.8 23 422.0 405.3 .01728 .2340 57,87 4 25 111.9 32 471.0 456 3 .01776 .2017 56.30 4 95 107 5 41 528.0 513.3 .01845 1744 54 19 5.70 103.2 SO 592.0 577.3 0.01920 0.1496 52.08 6.65 95.8 59 663.0 648.3 .02010 .1276 45,60 7.80 88 2 68 745 0 730.3 .02140 1076 46 , 73 9.30 73.6 77 832 0 817 3 .112300 . 0890 43 , 48 11 20 66 9 t86 930 0 915 3 02560 0726 39 06 13 80 51 1 95 1035 0 1020.3 0.0313G 0.0634 31 88 18.70 24.4 96 1055 0 1040.3 .03498 .0537 28. 58 23.50 13:2 97 1065 0 1040.3 .04080 .0408 24 51 24 50 0 0 72 HOUSEHOLD REFRIGERATION TABLE XXVIII.- PROPERTIES OF SATURATED VAPOR OF ETHANE— CjHe (H. D. Edwards) Pressure \ Specific Volume Density | Heat Content Above — 40° Temp. Abs. Gage Liquid Vapor Liquid Vapor Temp op "F lb./in.5 Ib./in.s ft.Vlb. ft.Vlb. Ib./ft.s Ib./ft.s Latert t. P- g.p. V V 1/v 1/V Btu./ib.;L= t. -150 7.0 15.6 0.02849 16.7 35.10 0.060 242 -150 -145 8.0 13.6 0.02865 14.1 34.90 0.071 240 -145 -140 9.7 10.1 0.02888 12.1 34.63 0.083 238 -140 -135 11.2 * 7.1 0.02901 10.5 34.47 0.095 236 -135 -130 13.2 * 3.0 0.02924 8.85 34.20 0.113 235 -130 -125 15.5 0.8 0.02939 1.69 34.02 0.130 233 -125 -120 18.2 3.5 0.02961 6.89 33.77 0.145 231 -120 -115 21.4 6.7 0.02976 5.88 33.60 0.170 229 -115 -110 24.8 10.1 0.03001 5.27 33 . 32 0.190 227 -110 -105 28.5 13.8 0.03018 4.55 33.13 0.220 225 -105 -100 3-'. 4 17.7 0.0305 4.13 32.8 0.242 224 -100 -95 36.4 21.7 0.0307 3.57 32.6 0.280 222 -95 -90 41.0 26 . 3 0.0.309 3.23 32.4 0.310 220 -90 -85 46.0 31.3 0.0311 2.86 32.2 0.350 218 -85 -80 51.2 30 . 5 0.0313 2.56 31.9 0.390 216 -80 -75 56.8 42.1 0.0315 2.35 31.7 0.425 214 -75 -70 63.0 48 . 3 0.0318 2.10 31.5 0.477 212 -70 -65 70.3 55 . 6 0.0320 1.94 31.3 0.515 210 -65 -60 78.2 63.5 0.0322 1.75 31.0 0.570 208 -60 -55 80.6 75.9 0.0325 1.63 30.8 0.615 206 -55 -50 95.9 81 .2 0.0327 1.50 30.5 0.666 204 -50 -■15 105.0 90.3 0.0330 1.39 30.3 0.720 201 -45 -40 114.5 99.8 0.0333 1.28 30.0 0.780 199 -40 -35 124.5 109.8 0.0336 1.18 29.8 0.845 196 -35 -30 135.0 120.3 0.0339 1.13 29.5 0.875 194 -30 -25 146.7 132.0 0.0342 1.05 29.2 0.950 192 -25 -20 159.5 144. S 0.0345 0.976 28.9 1.03 190 -20 -15 172 157 0.0350 0 . 855 28 . 6 1.17 187 -15 -10 187 172 0.0353 0.819 28 . 3 1.22 185 -10 -5 202 187 0.0357 0.730 28.0 1.37 182 -5 0 219 204 0.0361 0.689 27.7 1.45 179 0 +5 236 221 0 . 0365 0.629 27.4 1.59 176 +5 10 254 230 0.0370 0..581 27.0 1.72 174 +10 +15 272 257 0.0375 0.538 26.7 1.86 171 +15 +20 292 277 0.0379 0 . 495 26.3 2.02 168 +20 +25 307 292 0.0385 0,457 26.0 2 19 165 +25 +oO 335 320 0.0390 0.422 25.6 2.37 162 +30 +35 358 34 .S 0.0.397 0.389 25.2 2.57 158 +35 +40 383 3(18 0.0403 0 . 360 24.8 2.78 155 +40 +45 405 390 0 . 04 1 0 0.330 24.4 3 . 03 150 +45 +50 428 413 0.0417 0.305 24.0 3.28 146 +50 +55 453 438 0.0426 0.279 23 . 5 3.58 141 +55 +60 481 466 0.0435 0.256 23.0 3.90 136 +60 +65 511 496 0.0444 0.238 22 5 4.20 130 +65 +70 543 528 0.0461 0.214 21 '7 4.67 124 +70 +75 584 569 0.0478 0.182 20.9 5.50 115 +75 +80 625 610 0.0.508 0.163 19.7 6.14 107 +80 +85 672 6.=; 7 0.0.549 0.128 18.2 7.80 78 +85 +89 . 8 718 703 0.0775 0.0775 12.9 12.9 0 +89.8 * Inches of mercury below one standard atmosphere (29.92 in. =14. 697 Ibs./sq. in. abs.) Note: — References: Vapor Pressures. From 7 to 32 Ibs./sq. in. abs. by Maass & Wright, J. Am. Chem. Sec, 43, p. 1098. 1921. From 31 to 347 Ibs./sq. in. abs. by Kuenen and Robson. Phil. Mag, (6) 3, p. 149. 1902. From 162 to 734 Ibs./sq. in. abs. A. Hainlen, Lieb. Ann. 282, p. 229, 1894. Liquid and Vapor Densities. From — 162^° F_ to — 101° F. experimental data on liquid by Maass & Wright, J. Am. Chem. Soc, l3, p. 1104, 1921. Remainder of liquid and all of 'apor data as well as latent heats, calculated by The Laboratory of The Linde Air Products Co., Buffalo, N. Y. Probable accuracy of Density, Liquids, 1%; Vapor, 3'^: Latent Heats, 10%. REFRIGERANTS— TABLES 73 TABLE XXIX. -PROPERTIES OF SATURATED VAPOR OF ETHYL CHLORIDE C2H5CI. Hodsdon, igi^. Refrigerating World, Aug., (.1922). Henning, Oltnes, Regnuult and others; compiled by Starr. Practical Refrigerating Engineers' Hand Book, Nick- erson & Collins Co., Chicago, 1922. Tem Pressure Vok me Density Heat Content Above- 32°F. Abs. Gage Liquid Vapor Liquid Vapor Liquid Latent Vapor °F. lb. /in.' Ib./in.J ft.=/lb. ft.'/lb. lb./ft.> Ib./ft.« Btu./lb. Btu./lb. Btu./lb. t P gP V V l/» 1/V A + L = H -22 2.20 -12.5 0.01657 34.4 60.35 0.0291 -23.1 181.3 158.2 -13 2.85 -11.85 .01669 26.95 59.92 .0371 -19.2 179.9 160.7 - 4 3.66 -11.04 .OI6S2 21.33 59.45 .0469 -15.4 178.5 163.1 + t5 4.65 -10.05 .01695 17.06 59.00 .0586 -11.6 177.0 165.4 14 5.85 - 8.85 .01708 13.77 58.55 .0726 - 7.7 175.5 167.8 23 7.28 - 7.42 0.01721 11.21 68.10 0.0892 - 3.8 174.0 170.2 32 8.99 - 5.71 .01735 9.21 57.64 .1086 0.0 172.5 172.5 41 11.01 - 3.69 .01749 7.62 57.18 .1311 + 3.8 170.9 174.7 50 13.37 - 1.33 .01763 6.36 56.72 .1573 7.7 169.3 177.0 59 16.11 + 1.41 .01777 5.34 56.27 .1873 11.6 167.7 179.3 68 19.29 4.50 0.01792 4.51 55.80 0.2215 15.4 166.0 181.4 77 22.94 8.24 .01807 3.84 55.34 .2604 19.2 164.3 183.5 t86 27.10 12.40 .01822 3.29 54.88 .3043 23.1 162.6 185.7 95 31.82 17.12 .01838 2.83 54.41 .3536 26.9 160.8 187.7 104 37.17 22.47 0.01854 2.44 53.94 0.4090 30.8 159.0 189.9 113 43.16 28.46 .01870 2.13 53.47 .4704 34.6 157.2 191.8 122 49.88 35.18 .01887 1.86 53.00 .5382 38.5 155.3 193.8 131 57.36 42.66 .01904 1.63 52.52 .6135 42.3 153.3 195.6 -22 2.13 -12.57 0.0163 34.2 61.5 0.029 -23.1 193.0 170.0 -13 2.80 -11.90 .0164 26.5 61.0 .038 -19.2 192.0 172.5 - 4 3.63 -11.07 .0164 20.9 60.6 .048 -15.4 191.0 175.5 + t5 4.63 -10.07 .0167 16.7 60.1 .061 -11.5 190.0 178.5 14 5.84 - 8.86 .0169 13.5 59.7 .074 - 7.7 188.5 181.0 23 7.28 - 7.42 0.0109 11.0 59.2 0.091 3.85 187.5 183.5 32 9.00 - 5.70 .0170 9.1 58.8 .110 0 186.0 186.0 41 11.00 - 3.70 .0172 7.6 58.3 .132 + 3.85 184.5 188.0 50 13.55 - 1.15 .0174 6.25 57.9 .160 7.7 182.5 190.0 54.5 14.70 0.00 .0175 5.6 57.6 0.179 9.52 181.5 191.5 59 16.10 + 1.40 0.0176 5.35 .57.3 0.187 11.5 180.5 192.5 68 19.26 4.56 .0176 4.55 56.9 .220 15.4 179.5 194.0 77 22.90 8.20 .0177 3.90 56.5 .256 19.2 176.5 196.0 t86 27.05 12.35 .0178 3.35 56.0 .299 23.1 174.0 197.5 95 31.77 17.07 .0180 2.89 55.6 .345 27.0 172.0 199.0 104 37.11 22.41 0.0182 2.57 55.1 0.374 30.8 169.0 200.0 Gage pressures table supplied by Editor A. S. {Standard ton temperatures. R. E. Data Book. 74 HOUSEHOLD REFRIGERATION TABLE XXX.— PROPERTIES OF SATURATED VAPOR OF ISOBUTANE— C4H10 Lindc Air Products Company Laboratory. Refrigeration Engineering, June 1926 A. S. R. E. Data Book. Temp. PreMure Volume DenBity Heat Content Entropy From O' F. Temp. -F. Above 0" F. °F. Aba. Gsn Liquid Vapor Liquid Vapor Liquid Latent Vapor Liquid Vapor Ib.An." Ib./in.' ft.'/lb. ft.'/lb. lb./Jt.» lb./tt.> Btu./lb Btu./lb. Btu./lb. Btu./lb.'>F Btu./lb.»F t P gP c V 1/v 1/V h + L = H « 5 t -20 7.50 14.6 0.02610 11.00 38.36 0.0952 -9.0 166.5 156.5 -0.020 0.356 -20 -16 8.30 13. 0 .02620 9.60 38.16 .101 -7.0 164.0 157.0 -0.016 .354 -15 -10 9.28 11. 0 .02635 8.91 37.95 .112 -4.6 163.0 158.6 -0.010 .353 -10 - 6 10.4 8.8 .02645 7.99 37.80 .126 -2.5 162.0 159.6 -0.008 .351 - 5 0 11.6 6.3* 0.02660 7.17 37.60 0.139 0.0 160.5 160.6 0.000 0.350 0 + 1 11.9 5. 7* .02663 7.02 37.56 .142 0.5 160.5 161.0 .001 .350 + 1 2 12.2 5.1* .02667 6.87 37.60 .146 + 1.0 160.0 161.0 .002 .350 2 3 12.5 4, 6* .02670 6.72 37.46 .149 1.5 160.0 161.5 .003 .350 3 4 12.8 4.0* .02672 6.57 37.43 .152 2.0 159.5 161.5 .004 .350 4 5t 13.1 3.3» 0.02675 6.41 37.40 0.156 2.5 159.5 162.0 0.005 0.348 St 6 13.3 2.7* .02677 6.28 37.35 .159 3.0 159.0 162.0 .006 .349 6 7 13.6 2.1* .02680 6.15 37.31 .163 3.5 159.0 162.6 .007 .349 7 8 13.9 1.5* .02683 6.02 37.27 .166 4.0 158.5 162.5 .009 .349 8 9 14.2 0.9* .02686 6.88 37.23 .170 4.5 158.5 163.0 .010 .349 9 10 14.6 0.2* 0.02690 6.76 37.20 0.174 5.0 158.6 163.6 0.011 0.348 10 11 14.8 0.1 .02692 5.65 37.16 .177 5.5 158.0 163.5 .012 .348 11 12 15.2 0.5 .02695 6.52 37.11 .181 6.0 158.0 164.0 .013 .348 12 13 15.6 0.9 .02698 5.41 37.07 .185 6.5 157.5 164.0 .014 .348 13 14 15.9 1.2 .02700 6.30 37.04 .190 7.0 157.5 164.5 .015 .348 14 15 16.3 1.6 0.02705 5.18 37.00 0.193 7.5 157.0 164.5 0.016 0.347 15 16 16.7 2.0 .02706 6.08 36.96 .197 8.0 157.0 165.0 .017 .347 16 17 17.0 2.3 .02709