470 CHAPTER20 1953 Guide' Fig. 4.
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732 CHAPTER 33 1953 Guide time.
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834 CHAPTER 37 1953 Guide evaporation with the vapors leaving slightly superheated.
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966 CHAPTER 45 1953 Guide Table 1.
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r~ 'rr-tn e Industrial Hygiene Digest 5 *5 5 2 FEBRUARY, 1950 (VoL 14, No. 2) !
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Confidential Approved.
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96 CHAPTER 5 1954 Guide: Heat Transfer radiation which exists.
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354 CHAPTER 14 1954 Guide The operating efficiency of a gas appliance can then be computed with sufficient precision by application of Equation 18.
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368 CHAPTER 15. 1954 Guidfe V4 W installations.
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374 CHAPTER 15 1954 Guide In most localities it may be installed in basements without being enclosed.
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564 CHAPTER 24 1954 Guide 15 are marked Part 1 to Part 4 and, as will be evident by following the dashed line on Pthaertch1.artS, taarertiunsgedfraosmfotlhloewdse:pth of cover (2.5 in.), proceed vertically to the line representing pipe spacing on centers (12 in.), and then horizontally to the first ordi natPeaorft P8.arMt 2o.ve parallel to the nearest upward sloping line, indicating "2 in. & over" cover, to intersect the ordinate representing ) in. pipe, and then proceed hori zonPtaarlltySt.oPthroecefiersdt poardrainllaetletoof Panadrt a3l.ong the nearest downward sloping line to an intersection with the ordinate representing the panel output (34 Btu per sq ft), and then move horizontally to the right hand scale of Part 3 and read a required average waPtearrtie4m.peFrraotumrethine twheatceorilteomf 1p0e6raFt.ure 106 F just found in Part 3, proceed hori zontally into Part 4 to intersect the line representing insulation between the slab and fill.
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844 CHAPTER 37 1954 Guide nized that, heat storage devices may be used with any of these systems involving either a single or a dual heat source.
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934 CHAPTER 42 1954 Guide 0 plaster is drying out, the range and rate of temperature changes (either increase or decrease), should be kept low.
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f938 CHAPTER 42 1954 Guide experience shows that such high heat, requirement may result in excessive operating cost.
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1038 CHAPTER 47 1954 Guide and a humidity Hi will cool, following this cooling line toward poin'tb^f Air leaving with a humidity Hs will consequently have cooled to t., the wet-bulb temperature of the air throughout the dryer being t,,.
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