CHAPTER III REFRIGERANTS (Part 10)

1.503 85.72 .6657 37.63 147.77 185.40 74 53.48 38.78 .011680 1.476 85.62 .6777 37.97 147.40 185.37 75 54.47 39.77 0.011693 1.448 85 . 52 0.6907 38.32 147.02 185.34 76 55.48 40.78 .011706 1.422 85.42 .7030 38.67 146.64 185.31 77 56.51 41.81 .011719 1.396 85.33 .7163 39.01 146.26 185.27 78 57.56 42.86 .011732 1.371 85.23 .7295 39.36 145.88 185.24 79 58.62 43.92 .011746 1.343 85.13 .7446 39.71 145.50 185.21 80 59.68 44.98 0.011760 1.321 85.03 0.7570 40.05 145.12 185.17 81 60.77 46.07 .011773 1 .297 84.93 .7720 40.39 144.74 185.13 82 61.88 47.18 .011786 1.274 84.84 .7850 40.73 144.36 185.09 83 63.01 48.31 .011800 1.2.53 84.74 .7980 41.08 143.97 185.05 84 64.14 49.44 .011814 1.229 84.04 .8140 41.43 143.58 185.01 85 65.28 50.58 0.011S2S 1.207 84 , 54 0.S2S5 41.78 143.19 184 97 86 1 66.45 51.75 .011841 1.185 84.44 .8440 42.12 142.80 184.92 87 67.64 52.94 .011854 1.164 84.35 .8590 42.46 142.41 184.87 88 68.84 54.14 .011868 1.144 84 .25 .8740 42.80 142.02 184.82 89 70.04 55.34 .011882 1.124 84.15 .8998 43.15 141.62 184.77 90 71.25 56.55 0.011896 1.104 84.05 0.9058 43.50 141.22 184.72 91 72.46 57.76 .011909 1.084 83.96 .9225 43.85 140.82 184.07 92 73.70 59.00 .011923 1.065 83.86 .9390 44.19 140.42 184.61 93 74.98 60.18 .011937 1.047 83.77 .9551 44.53 140.02 184.55 94 76.30 61.60 .011951 1.028 83.67 .9730 44.86 139.62 184.49 95 77.60 62.90 0.011965 1.011 83.57 0.9890 45.20 139.23 184.43 96 79.03 64.33 .011979 .9931 83.47 1.007 45.54 138.83 184.37 97 80.40 65.70 .011993 .9759 83.37 1.025 45.88 138.43 184.31 9S 81.77 67.07 .012008 .9591 83.27 1.043 46.22 138.03 184.25 99 83.14 68.34 .012002 .9425 83.17 1.061 46.56 137.62 184.18 100 84.52 69.82 0.012037 0.9262 83.07 1.080 46.90 137.20 184.10 105 91.85 77.15 .012110 .8498 82.57 1.176. 48.88 135.14 183.72 no 99.76 85.06 .012190 .7804 82.03 1.281 50.26 133.05 183.31 115 108.02 93.32 .012275 .7174 81.46 1.394 51.93 1.30.92 182.85 120 120.93 106.23 .012360 .6598 80.90 1.515 53.58 128.78 182.36 125 126.43 111.73 0.012445 0.6079 80.35 1.645 55.31 126.51 181.82 130 136.48 121.78 .012530 .5595 79.81 1.787 56.85 124.39 181.24 135 147.21 132.51 :012620 .5158 79.23 1.947 58.47 122.15 180.62 140 158.61 143.91 .012720 .4758 78.61 2.102 60.04 119.90 179.94 J Standard ton temperatures. REFRIGERANTS— TABLES 19 TABLE XXXIV. -PROPERTIES OF SUPERHEATED VAPOR OF SULPHUR DIOXIDE— SO. David L. Fiske, Urb ana, 111.-192 5. A. S. R E. Data Book. Temp. Abe. Pressure 4 lb. /in. » GagePressur&21.7in. vac. (Safn. Temp. - 32 60° F.) Abs. Pressure 6 Ib./inT Gage Pressure 17.7 in. vac. (Sal'n. Temp - 19:37° F.) Abe. Pressure 8 lb./in.> Gage Pressure 13.6 in. vac. (Safn Temp. - S.9«° F.) Abs. Pressure 10 Ib./io.' Gage Pressure 9.6 in. vac. (Safn. Temp. - 1.34° F.) t Volume f..'/lb. V Heat Content Btu./lb. H, Entropy Btu./lb.°F. 5 Volume ft.'/lb. V Heat Content Btu.,1h. H Entropy Btu.,'Ib.°F- 5 Volume ft.'/lb. V Heat Content Btu./lb. H Entropy Btj./Ib.°F. s Volume ft.Vlb. V Heat Content Btu./lb. H Entropy Btu./lb.°F, s (altclCn) -20 -10 0 10 20 30 40 50 60 70 80 90 100 no 120 130 140 150 160 170 180 190 200 18.40 18.83 19.27 19.70 20.14 20.57 21.00 21.42 21.85 22.27 22.70 23 . 12 23.54 23.96 24.39 24.81 25.23 25.65 26.08 26.50 26.92 079.57) 181.5 183.0 184.6 186.1 187.7 189.3 190.9 192.5 194.1 196,7 197.3 198.9 200.5 202.1 203.8 205.2 207 . 1 208.8 210.4 212.1 213.8 0.42487 .42836 .43179 .43516 .43847 0.44161 .44491 .44806 .45116 .45421 0.45722 .46018 .46311 .46600 .46885 0.47167 .47445 .47720 .47991 .48259 0.48523 OlJl) as'u) {0.41 tSt) (9JliO) (.tS2S3) (CiOiSl) 0.510) USt.9S) (.040000) 0^40046 .40432 .40802 0.41159 .41505 .41837 .42161 .42480 0.42795 .43104 .43407 .43705 .43997 0.44283 .44565 .44842 .45116 .45296 0 45651 .45913 .46171 12.75 13.04 13.34 13.63 13.93 14.23 14.52 14.71 15.11 15.40 15.69 15.97 16.26 16.54 16.82 17.09 17.35 17.62 17.88 18.13 18.38 184.3 185.9 187.5 189.1 190.7 192.3 193.9 195.6 197.2" 199.9 200.5 ,202.2 203.8 205.3 207.1 208.8 210.4 212.1 213.7 215.4 217.0 .41850 .42198 .42538 0.42869 .43196 .43517 .43833 .44140 0.44443 .44741 .45035 . .45326 .45613 0.4589(5 .46176 .46451 .46722 .46990 0.47254 .47514 .47769 9.516 9.751 9.983 10.21 10.44 10,66 10.88 11.10 11.32 11.54 11.75 11.97 12.18 12.39 12.61 12.82 13.03 13.24 13 46 13.66 13.88 183.7 185.4 187»1 188.8 190.5 192.2 193.8 195.5 197.1 198.8 20O.4 202.1 203.7 205.4 207:0 208.8 210.3 212.0 213.6 215.3 216.9 0.40871 .41230 .41579 0.41922 .42256 .42582 .42903 .43216 0.43524 .43825 .44123 .44416 .44705 0.44990 ■..45271 .45543 .45820 .46089 0.46353 .46614 ^46871 7.545 7.744 7.939 8.030 8.316 •8.500 8.681 8.860 9.038 9.214 9.389 9.563 9.736 9 908 10.08 10.25 10.42 10.59 10.76 10.93 11.10 183.2 185.0 186.7 188.4 190.1 191.8 193.5 195.2 196.9 198.6 200.3 202.0 203.7 205.4 207.1 208.8 210.5 212.2 213.8 215.4 217.0 Temp. °F. 20 30 ,40 50 60 70 80 90 100 110 120 130 140 150 160 170 180 190 200 210 220 230 240 250 Abs, Pressure 15 lb., 'in.' Gage Pressure 0.30 lb.,in.' (Sat'n. Temp. 14.43° F.) Abs. Pressure 20 lb. An.' Gage Pressure 5 30 Ib./in,' (Safn. Temp. 26.44° F.) Abs. Pressure 25 lb. /in.' Gage Pressure 10.30 lb. /in.' (Safn. Temp. 36.33° F.) Aba. Pressure 30 lb /in,' Gage Pressure 15.30 lb/in.' (Sat'n. Temp. 44.75° F ) (o.UO) 5.192 5.333 5.470 5.604 5.734 5.862 5.988 6.112 6.233 6.353 6.471 6.588 6.705 6.821 6.937 7.052 7.167 7.282 7.396 usun 185.4 187.3 189.2 191.0 192.8 195.6 196.4 198.2 199.9 201.6 203.3 205.6 206.7 208.4 210.1 211.8 213.5 215.2 216.9 (0.30091) 0.39270 .39672 .40054 .40424 .40777 0.41116 .41443 .41765 .42076 .42383 0.42682 .42976 .43264 .43548 .43825 0.44097 .44366 .44630 .44889 (3.S7S) USi.se) icassm (S.IBS) Ossjse) (0.S775O («.«/4) USS.iS) (0.S7169) 4.035 4.145 4.251 4.354 4.454 4.552 4.648 4.742 4.834 4.925 5.015 5.104 5.193 5.281 5.369 5.456 5.542 5.629 5.715 187.8 189.8 191.8 193.7 195.6 197.5 199.3 201.1 202 9 204.7 206.5 208.2 209.9 211.6 213.3 215.0 216.7 218.4 220.1 0.38959 .39346 .39719 0.40080 .40429 .40758 .41093 .41415 0.41726 .42027 .42322 .42613 .42898 0.43176 .43449 .43716 .43977 .44234 0.44488 3.181 3.273 3.363 3.451 3.536 3.618 3.696 3.772 3.848 3.923 3.998 4.073 4.145 4.216 4.287 4.358 4.428 .4.498 4.567 4.637 4.706 186.1 188.4 190.6 192.7 194.7 196.7 198.6 200.5 202.4 204.2 206.0 207.8 209.6 211.4 213.2 215.0 216.7 218.4 220.1 221.8 223.5 0.37927 ,38372 .38795 0.39198 .39582 .39945 .40291 .40625 0.40949 .41261 .41568 .41866 .42156 0.42439 .42717 .42988 .43253 .43413 0.43769 .44023 .44275 2.747 2.830 2.907 2.980 3.052 3.122 3.189 3.254 3.318 3.381 3.443 3.504 3.565 3.625 3.685 3.744 3.803 3.861 3.919 3.977 4.035 i89.3 191.6 193.8 195.9 197 .9 199.9 201 8 203.7 205.6 207.5 209.3 211.1 212.9 214.7 216.5 218.3 220.1 221.9 223.6 225.3 227.0 0.37969 0 38428 .38848 .39236 .39603 .39955 0.40293 .40619 40935 .41241 .41539 0 41S29 .42112 M2387 .42657 .42921 0.43180 .43438 .43691 .43942 .44188 260 Note: V is Volume of Superheated Vapor, ft.'/lb.; H is Heat Content, Btu./lb., and S is Entropy, Btu./lb. °F. 8U HOUSEHOLD REFRIGERATION TABLE XXXIV.— PROPERTIES OF SUPERHEATED VAPOR OF SULPHUR DIOXIDE— S02.—(Cot,tiiiucd) Temp. Abe. PreMUlc 40 Ib.Am.' Gage Pressure 25 .TO lb. /in.' (Safn. Temp. S8.83° F.) Abs. Pressure SO lb/in.' Gage Pressure S.S.SO Ib./ip.' (Sat'n, Temp. 70.40° F.) Abs. Pressure 60 lb. /in.' Gage Pressure 4.'i 30 Ib./in,' (Sat'n. Temp. 80,29° F.) Abs. Pressure 70 lb./in.« Gage Pressure 5.1.30 Ib./in.' (Safn. Temp. 88.97° F.) t Volume ft.'/lb. V Heat Content Btu./Ib. H Entropy Btu./lb.-F. s' Volume tt.'/lb. V Heat Content Btu./lb. H F.ntropy ntu./lb.°F s Volume fl.'/lb. V Heat Content Btu./lh. H Entropy Rtu-/lb.°F 5 Volume tt.'/lb, V Heat Content ntu./ib, H Entiopy Btu./lb.°F. 5 iaisatn) 60 70 80 90 100 110 120 130 140 150 160 170 180 190 200 210 220 230 240 250 260 270 280 290 300 a 970) 1.980 2.064 2.121 2 185 2 246 2.304 2.360 2.413 2.465 2.515 2.565 2.614 2.662 2.709 2.755 2.800 2.845 2.889 2.933 2,977 3.021 (.iss.eo) 185.9 188.7 191.3 193.6 196.1 198.3 200.4 202.5 204.6 206.5 208.5 210.4 212,3 214.2 216.0 217.9 219.7 221.5 223.3 225.1 227.0 10.36470) 0.36544 .37064 .37544 .37992 .38415 0.38810 .39183 .39541 ,39881 .40209 0.40525 .40831 ,41127 ,41416 ,41694 0.41966 .42233 ,42494 ,42751 .43007 0,43262 VS77-) U8S.-iS) (.OSSSiS) itSI44) iiss.iey i0.3S27i} ii.ies) (IS4.77) (0.S47S9) 1.668 1.723 1.775 1.825 1.872 1.917 1.961 2.003 2,044 2.084 2.123 2.161 2.199 2.237 2.274 2.311 2.347 2.383 2 418 2.454 2.489 188.4 191,2 193,9 196.4 198.8 201.1 203.3 2Q5.4 207.5 209.6 211.6 213.4 215.4 217 3 219.2 221.1 223.0 224.9 226 7 228.5 230.3 .36366 . .36887 .37369 0.37815 .38234 .38627 .38998 .39353 0,39691 .40015 ,40327 .40628 .40919 0.41200 .41477 .41748 .42015 .42275 0 42535 .42791 .43045 1.288 1.346 1.403 1.459 1.514 1.563 1.608 1.650 1.689 1.726 1.751 1 785 1.819 1.853 1 .885 1,917 1.948 1.979 2 010 2,040 2 070 191.4 194.3 197.0 199.5 201.9 204.2 206.5 '208.6 210.7 212.8 214.8 •216.8 218.7 220 7 2'22.6 2'24.5 226.4 228.2 230.1 232.0 233.8 0.36403 0. 36906 .37375 .37810 .38217 ,38603 0.38963 .39310 .39639 ,39956 ,40260 0 40554 .40839 .41118 .41391 .41657 0.41917 .42175 .42431 .42685 0 4'2935 1.181 1.228 1.272 1.313 1.352 1.389 1.424 1.457 1.489 1.521 1.551 1.580 1.608 1.636 1 .664 1.691 1.718 1.745 1.771 1.798 1.824 187.6 191.6 194.8 197.6 220. 3 ■202.9 205.3 207.6 209.9 212.0 214.1 216,1 218.1 220 . 1 •222 . 1 2-24.1 •226.0 •227.9 ■229.8 231.7. 233.5 0,35443 0,36020 .3654,5^ .37028 .37478 .37897 0.38291 .38662 .39014 .39348 .39670 0.39978 .40275 .40564 .40843 ,41120 0,41389 .41653 ,41912 .42167 0.42418 Temp. Abs. Pressure 80 lb. /in » Gage Pressure 65.10 lb. /in.' (Safn. Temp. 96.88° F.) Abs. Pressure 100 lb"/in.' Gage Pressure 83.30 lb/in.' (Safn. Temp. 110.15° F.) Abs. Pressure 120 lb. /in.' Gage Pressure 10,V30 lb./in.» (Sat'n, Temp, 121.52° F.) Abs. Pressure 140 Ib./in.' Gage Pressure 125.30 Ib./in.' (Safn. Temp, 131.04° F.) iattafit) 100 110 120 130 140 150 160 170 ISO 190 200 210 220 230 240 250 260 270 280 290 300 310 320 330 340. i0.9S09y 0.993 1.040 1.084 1.125 1.163 1.199 1.232 1.263 1.292 1 320 1.347 1.374 1.400 1.426 1.451 1,476 1 500 1.524 1.547 1.570 1.593 ilSi.SS) 185.6 189.1 192.5 195.7 198 6 201.3 203.9 206.4 208.7 211.0 213.3 215.5 217.5 219 6 221 6 223 6 225.6 227.6 229.5 231.5 233.4 (0.34557) 0.34571 ,35214 .35797 ,36330 ,36819 0.37270 .37692 -.38093 .38461 .38813 0.39150 .39471 .39780 .40079 .40369 0.40651 .40926 .41195 .41459 .41719 0 41974 (0.77«o) (ISSM) W.sseoj) {0.e4SO} OSi.I9) 10.33954) 0J45I) US1.04) iO.Sl3SS) 0.8190 .8575 .8928 0.9255 .9561 .9848 1.012 1.03S 1.062 1.086 1.109 1 131 1.152 1.173 1 . 194 1 213 1 .232 1.251 1.268 1.284 1.299 187,3 191.0 194.6 197.9 200.9 203.7 206 4 209.0 211.5 213.8 216.1 218.4 220.5 222.6 224.7 226.8 228. S 230.8 2.'?2 8 234.8 236,7 0.34296 .34942 .35528 0.36061 .36558 .37009 .37431 .37829 0.38203 ,38550 .38892 .39214 .39524 0.39824 .40114 .40397 .40673 .40944 0.41207 .41464 ,41716 0.7085 0.7403 .7700 .7972 ,8'228 .8470 0 8699 .8916 .9124 .9324 .9515 0.9700 .9.S'<0 l.f)06 1 .023 1.040 1.0.56 1.072 1.088 1.104 1.120 190.1 193.9 197.4 200.6 203.7 206 7 209.4 212.0 214.5 217.0 219.3 221 5 223.7 225.9 ■228.0 230.1 233.2 2,34.3 ■236.3 2.38.3 ■240.3 0.34264 0.34904 .35484 .36012 .36494 .36936 0.37348 .37737 .38104 .38451 .38785 0.39106 .39416 ,39713 40002 ,40284 0.40,5.58 ,40.825 0.5734 0.6055 .6345 .6613 ,6861 ,7092 0: 7.309 ,7513 ,7707 .7892 .8070 0.8241 .8405 .8564 .8720 ,8970 0,9017 9161 185 i 189.7 193 6 196.3 200.8 ■204.0 •207.1 210 0 212.7 215.4 217.9 220 3 222 6 224.9 227.1 229.3 231.5 2,33.6 2.35.7 237.7 239.7 0.33089 0 33777 .34442 .35041 .35588 ,36088 0.36548 ..36976 .37379 ..37758 ..38118 0.38461 .38789 .39105 .39408 .39701 0.39985 .40261 ,40.529 ,40791 0.41049 .41,ns5 i: .9302 .41338 1 .9441 0.41.T.S3 0.9,579 Note: V is Volume of Superheated Vapo» ft.'/lb.; H is Heat Content. Btu./lb.. aud-S is Entrop]'. Btu./lb. °F. REFRIGERANTS— TABLES 81 82 HOUSEHOLD REFRIGERATION 'S 'V ^ IC o ' ^ 2 P c; c- j CO c^ o ■* r>. >o 01 -^ ^ ^ ■'J' »o Cl « lO O Cl C-l or-; I <N Cl O— I -H . r^ o — o o t^ci O •-< ^ Cl Cl (NO CO O I '£2 CO" CT" c: Cl O lO £^ d $ ££J2 3" c S" t." W !^ K ^ ^ C C c: rt c! £oaji ii,^ •ro oo CCl COiO ,=5 • O O t. CO o o o .t: I + O 00 f CO -^ 1^ M cc Cl « '■Zai a. x u Cj II 2 £a Wo t; H .Sg REFRIGERANTS— TABLES 83 TABLE XXXVI.— SOLUBILITY OF AMMONIA IN WATER. Siebel — Compend of Mechanical Refrigeration. Nicksrson & Collins Co., Chicago. Temp. Content Lb. NhJ Vol.NHi Lb.NHj VoI.NHj "F. Lb.H.O voi.n.o °v. Lb.HiO Vol.HiO 320 0.899 1180 122.0 0.284 373 35.6 .853 1120 125.6 .274 3.59 39.2 .809 1062 129.2 .265 348 42.8 .765 1005 132.8 .2.56 336 46.4 .724 951 136.4 .247 324 soo 0.684 898 140.0 0.2.38 312 .53.6 .646 848 143.6 .229 301 .57.2 .611 802 147.2 .220 289 60.8 .578 759 150.8 .211 277 64.4 .546 717 154.4 .202 265 68.0 0.518 683 158.0 0.194 2.54 71.6 .490 643 161.6 .186 244 75.2 .467 613 165.2 .178 234 78.8 .446 .585 168.8 .170 223 82.4 .426 559 172.4 .162 212 86.0 0.408 536 1760 0.1,54 202 89.2 .393 516 179.6 .146 192 93.2 .378 496 183.2 .138 181 96.8 .363 478 186.8 .130 170 100.4 .350 459 190.4 .122 160 104.0 0.338 444 194.0 0.114 149 107.6 .326 428 197.fi .106 139 111.2 .315 414 201.2 .098 128 114.8 .303 399 204.8 .090 118 118.4 .294 386 208.4 .082 107 1 (212.0 0.074 97) PreM. Abe. Lb./in.> 32»F. es^F. 1040 F. 212° F. 1 Lb. NH. Lb.HtO VoI.NH, Vol.HjO Lb. NHi Lb.HiO VoI.NH. Vol.H^O Lb. NHi Lb.HiO VoI.NH. VoLHiO Gm.NH, Lb.HK) Vol.NHi Lb.HiO 14.67 15.44 16.41 17.37 18.34 19.30 20.27 21.23 22.19 23.16 24.13 25.09 26.06 27.02 27.99 28.95 30.88 32.81 37.74 36.67 38.60 40.53 0.899 0.937 0,980 1.029 1.077 1.126 1.177 1.236 1.283 1.336 1.388 1.442 1.496 1..549 1.603 1.656 1.758 1.861 1.966 2.020 1.180 1.231 1.287 1.351 1.414 1.478 1..546 1.615 1.685 1.754 1.823 1.894 1.965 2.034 2.105 2.175 2.309 2.444 2.582 2.718 0.518 .535 .5.56 .574 .594 0.613 .632 .651 .669 .685 0.704 .722 .741 .761 .780 0.801 .842 .881 .919 .955 0.992 0.683 .703 .730 .754 .781 0.805 .830 .855 .878 .894 0.924 .948 .973 .999 1.023 1.052 1.106 1.1.57 1.207 1.254 1.302 0.338 .349 .363 .378 .391 0.404 .414 .425 .434 .445 0.454 .463 .472 .479 .486 0.493 .511 .530 .547 .565 0.579 ..594 0.443 .458 .476 .496 .513 0.531 .543 .559 .570 .584 0.596 -.609 .619 .629 .638 0.647 .671 .696 .718 .742 0.764 .780 0.074 .078 .083 .088 .092 0.096 .101 .106 .110 .115 0.120 .125 .130 .135 0.097 .102 .109 .115 .120 0.126 .132 .139 .140 .151 0.157 .164 .170 .177 1 For convenience the bodies of the above tables give the ammonia content of ;he saturated solutions at the various temperatures and pressures in both pounds of am- monia per pound of water and volumes of ammonia per volume of water. — Editor A. S. R. E. Data Book. TABLE XXXVIl.— HEAT OF ASSOCIATION OF AMMONIA. MoHicr-.S(n rr'tf I Rcfrigcrat ni) E OinctT ,' Ha nd Hna k. ^ ickerson A'Collirn Co.. Vhicano. ^ ^ ^ ^ ., K K s a X X X 33 X X B 33 i: Z z z z 2 z Z z z Z Z .£} Xi .a j3 .a ^S J3 L* M Si j3 Si Sl ft? JS a 3 X 2 X 3 B 3 X 3 S 3 X 3 X 3 X 3 S 3 X 3 X 3 ''• a <i a eg Z =0 a a » A S) 7. CQ z n z 03 03 n 347 s 329 in 307 l.'i 284 20 2,V) ?.s 232 30 203 3S 17.i 40 142 4S 100 so 70 5S :!4 1 344 ti 323 11 303 1« 279 21 2.54 2li 220 31 19S 3li 108 41 135 40 99 h\ .S2 50 27 2 .■J40 7 321 12 29« 17 274 22 24 S 27 221 32 192 3; 102 42 128 47 92 Wi. 36 57 20 :i 337 X 316 r.( 294 1,S 269 2.1 243 2,S 215 33 180 3M \i>^ 43 121 48 85 .S3 49 58 14 4 333 H 311 14 2S0 19 204 24 23S 29 209 .14 180 39 149 44 113 49 77 .M 41 59 7 00 to 100-01 at of Association of Ammonia," gives the heat of 18 of variouB strengths. The iotcX heat liberated i lutioiis of various strengthB ia the heat 0/ associatic See tables of Properties of Anhytirous Ammonii and disasaociatioD of one pound of n up respectively when a pound of ami tho latent heat of vipuristiti 84 HOUSEHOLD REFRIGERATION ^ u V CQ ^ ^_, UJ < ^ t* o s ^ o S .o> § H-, < c ft:; < o •^ a ,° a < s fe Us u o > X X o X fin 4; w J O m < fe H H ^ '^ * ft f W ~ §1 1 Oj re <- J, 2 I ■- s < " 1-00 t^O 0 M r^rOlOt^O lAx P^IOOOOOOO O 0>ih loO «»5 MClNlHWIHIHI-Cl-IMI-IWlHI-il-ll-l !? iH u-)Tt»ot^O 'to Ti-t^o ■*" toiDOoo or^OvO •^00 <n lo O 0 - ^ fO^Ot^Oi-i POO 0\ <^ lOOO M Tj-cO cs vO tH lO O Tfoo M M O CM» t^O voLO-^rO" M w O O CM» 00 t^ t^>0 to to ■<!• ^ iOO>0 fO'^O" OvMO 0>0 " fO^OOOOO t^OO 1-1 >O00 Tl-O t^ t^ 0> 0 i-i t^ tovO 0> w rO I^ O fOO 0>«>0 O -^OvfOI^WO M O O O\00 t~.vO lOTl-'trO'N M M 0 O O>00 00 <^^0 >0 lo 1/1 tJ- MNWMI-lMI-ll-IIHlHMIHMIHI-l n OO lo O M \0 O^O 0 rOO 00 M O 0 OO t^ t-'O ro-O O >0 t^ to