72 CHAPTER 6 1960 Guide DRY BULB TEMPERATURE F * Nets--froth cuflnw and wtaterconfort Ems apply to irisabikusis of ft United State* oofy.

106 CHAPTER 9 1960 Guide Table 2------Variation. in Surface Conductance Coefficient for Vertical Surfaces with Different Temperatures of Surrounding Surface Surroonding Swfstt Tomporatvro 75 f 70 F 69 F 60 F 50 F Convection--Btu per (hr) (sq ft). 6.6 6.6 6.6 6.6 6.6 Radiation--Btu per (hr) (sq ft).. 4.4 8.6 9.6 17.0 24.9 Total--Btu per (hr) (sq ft) ___ 11.0 15.2 16.2 23.6 31.5 tion, is illustrated in Table 2, which applies to a vertical sur face at 80 P, with ambient air at 70 F and with radiation exchange corresponding to an effective emissivity of 0.83.4 In many cases, because the heat resistance of the internal parts of the wall is high compared with the surface resistance, the surface factors are of minor importance.

288 CHAPTER 20 1960 Guide the duet, and perpendicular to the outlet face.

352 CHAPTER 25 1960 Guide . p* static pressure L JI"(r)(D.)

746 CHAPTER 54 1960 Guide Table 1___ Cost Dollars per Too for a Complete System, Including Heating and Cooling Coils, Fan, Duds, Refrigeration Equipment, Temperature Controls, etc.* 12 3 6 Unit Codi 6 78 Total CocT* 9 10 11 Unit Corfi* 12 13 PsfrfgaroHon Root Area Sqft Air Ditfrib* trted Co FI tioo Equip ment per Ton Duct*, Fans, Heat ftefrigero* ing Cods, fton Equip etc. ment Air HantUlng Equipment Total Evaporative Concenters Per Ton Per Sq Ft Floor Per Cfm Per Ton Cooling Towers Per Ton 8,333 12,500 250 16,666 25,000 224 212 33,332 50,000 204 150 50,000 75,000 195 66,664 100,000 192 83,333 125,000 187 100,000 150,000 182 133,328 200,000 165 500 166,666 250,000 158 1.05 0.98 0.95 0.92 0.91 0.90 0.88 0.86 0.84 0-82 6,250 31,200 15,900 20,400 29,200 38,200 46,800 54,600 66,000 79,000 13,100 24,500 35,700 46,000 68,200 90,000 110,000 129,000 168,000 205,000 19,350 35,700 51,600 66,400 97,400 128,200 156,800 183,600 234,000 284,000 775.00 730.00 690.00 664.00 650.00 641.00 628.00 612.00 585.00 568.00 2.32 2.15 2.07 1.99 1.95 1.93 1.88 1.84 1.76 i:7i 1.55 1.43 1.38 1.33 1.30 1.28 1.25 1.23 1.17 1.14 190.00 155.00 120.00 90.00 60.00 52.00 50.00 48.00 46.00 44.00 42.00 40.00 Mg || in 4gpaztmeot iVmc, <zt (or industrial aiirr caoanoddiittiioonniinng* iianvvolving targe areas- Where a multiplicity o hriilllinp tuUele etui ejmtiMBt hem--. tieM OTBti dp BQt appty. t Wb ccn^vnUon of water b suited, add column U T <?

766 CHAPTER 56 1960 Guide termination of the design rate of flow in any particular sec tion of piping.

38 CHAPTER 2 1962 Guide And Data Book S' WER EXHAUST 4 -- CONDITIONED AIR PROM FAR-COIL URtT Fig. 43 ....

58 CHAPTER 4 1962 Guide And Data Boole * 20 pel cent bat 6im added to the o'notable internal gaia to account for (ft* luat of coopfcaioa added with the air-conditioning compressor.

152 CHAPTER 10 1962 Guide And Data Boole Rg. 17 ....

350 CHAPTER 31 1962 Guide And Data Book times required in various rooms used, depending upon the method practiced.

382 CHAPTER 33 1962 Guide And Data Book is the ejector nozzle system.

422 CHAPTER 38 1962 Guide And Data Book accurately calculate the enthalpy of a food product for a com mercial application certain precautions should be followed.

850 CHAPTER 77 1962 Guide And Data fig. 11 ...

m m B 438 CHAPTER 24 1965 Guide And Data .Book Table 128 ;.

528 CHAPTER 27 7 1965 .Guide.