650 CHAPTER 30 1953 Guide In cold weather no refrigerant is required iu the cooling coil,, and in hot weather no heating medium is circulated in the heating coil.

828 CHAPTER 37 ' 1953 Guide': S nized that heat storage devices'may be used with-any of these systems, involving either a single or a duabheat source.

1048 CHAPTER 49 1953 Guide FRICTION LOSS IN HEAD IN LBS.

1120 1953 Guide ME'I'fcRS, Flow Williams Oil-O-Matic Div., Eureka .UHnrn^ Flnginopring hn liSSLiiM .

130 CHAPTER 6 1954 Guide '* Physiological Response of Subjects Exposed to High Effective Temperatures and Elevated Mean Radiant Temperatures, by C.

PLAINTIFF'S EXHIBIT Industrial Hygiene Digest INDUSTRIAL HEALTH NEWS LITERATURE ABSTRACTS MEDICAL ENGINEERING CHEMICAL TOXICOLOGICAL LEGAL > daciaiona and tianda MAY, 1954 (Vol. 18, No. 5) '3MED ':bces J-JN I 1954 S^N/STRIAL HYGIENE FOUNDATION MELLON INSTITUTE 4400 FIFTH AVENUE PITTSBURGH 13.

612 CHAPTER 27 1954 Guide not heavier than extra-strong, assumes a maximum safe value of fiber stress of 16,000 psi.

706 CHAPTER 32 1954 Guide appreciable, as in elbows of good design, it is customary to include the dynamic loss with the friction loss, thereby facilitating design calculations.

910 CHAPTER 41 ' 1954 Guide Table 3. ..

1026 CHAPTER 47 1954 Guide Periods of Drying1 A typical drying time curve for a wet solid is shown in Fig. 2.

402 CHAPTER 16 1955 Guide return piping preventing return of condensation; (c) valve closed in return line; (d) connection of bottom of water column into a very active section or thin waterway; and (e) improper connections between boilers in battery permitting boiler with excess pressure to push returning condensation into boiler with lower pressure. 4.

576 CHAPTER 24 1955 Guide Table 2.

858 CHAPTER 37 1955 Guide of refrigerant entering the evaporator remains unchanged, but the leaving enthalpy increases and, hence, the refrigerating effect increases.

1052 CHAPTER 47 1955 Guide < Fiber saturation point is the moisture content of cellular materials (wood, etc.) at which the cell walls are completely saturated while the cavities are liquid-free.

68 CHAPTER 4 1956 Guide Replacing v by its equal g/gcp (where p is density in pounds weight per cubic foot) and rearranging, Equation 3 becomes -- dV* + - dp + dz + -- [Jdu + pdv -- Jdq + dW] = 0 2g p g (4) In the case of flow through a pipe, no outside work is performed so that dW = 0.