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486 CHAPTER 21 1955 Guide the rise in the water level at the far end of the return, due to the difference in steam pressure, would be 1 of 28 in. (28 in. head being equal to one pound per square inch), or 3} in.
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564 CHAPTER 23 1955 Guide REFFERENCES * I=B=R Installation Guide No. 5, Baseboard Heating Systems (Institute of Boiler and Radiator Manufacturers, Second Edition, 1953).
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642 CHAPTER 27 1955 Guide must be used in the U-bend to take up the deformation, A.
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666 CHAPTER 29 1955 Guide are not as high as desired, higher pressures can be obtained by use of a steam compressor.2 It is sometimes desirable to install a separate high-pressure line from the boiler plant for steam supply to laundries or other high-pressure equip ment rather than to operate the entire distribution system at higher pres sures.
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720 CHAPTER 31 1955 Guide A.S.H.VJE.
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960 .CHAPTER 42 .1955 Guide plaster is drying out, the range and rate of temperature changes (either; increase or decrease), should be kept low.
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1102 CHAPTER 49 1955 Guide Table 3; Performance Requirements of Water Meters* Sirs In. *4 _____ a........
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1138 CHAPTER 52 1955 Guitj/U ments are recommended.
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72, CHAPTER 4 1956 Guidei The curves in Fig. 4 may be approximated very closely by the empirical formula:1 /- 0.0055T1^1 +(/20,000-e + --10*\Jw* Equation 8 is applicable to all liquids, ahd to gases when the pressure loss is less than 10 percent of the initial pressure.
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146 CHAPTER 7 1956 Guide lectasis, asphyxia and asthma.
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256 CHAPTER 12 1956 Guide Table 1.
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444 CHAPTER 17 1956 Guide ' -j Friction Factors for Pipe Flow, by L.
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822 CHAPTER 35 1956 Guide circulating water as a result of evaporation; that the water suspended in the tower is surrounded by a film of air which is saturated with water vapor and at the temperature of the water surrounded; and that the basic theory of cooling tower operation proposed by Lewis13 and developed by Merkel14 is applicable.
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922 CHAPTER 39 1956 Guide valve handles about one-third of the total capacity and the other about two-thirds.
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