554 CHAPTER 21 1957'Giiide Table 1 can be used for pipe sizing by this method.

588 CHAPTER 22 1957 Guide :r Table 1.

648 CHAPTER 24 1957 Guide These quantities of heat are related by the following equations: H = 0.24 W (< -- lo) Ht = 0.24 W , - O H. = Hi -- H, = 0.24 W (ir - 0 jy = d 60 Q ff, = H. + 0.24 d 60 Q (t - t,,). where (1) (2) (3) (4) (5) d = density of air, pounds per cubic foot (0.075 lb per cu ft for Standard Air by definition). ' H, = surplus heat, Btu per hour. ff, = heat required to warm air for ventilation, Btu per hour.

894 CHAPTER 35 1958 Guide chamber, either in series with the sprays or below them.

28 CHAPTER 3 1959 Guide point at which the break in the isotherm through the point in question occurs, is the weight of water per pound of dry air in the vapor phase.'

50 CHAPTER 5 1959 Guide- Table 2____Approximate Unit Conductances for Thermal Convection for Several Flow Systems {Concluded) Heat framfn.

378 CHAPTER 26 1959 Guide Inverted Bucket Traps.

514 CHAPTER 35 1959 Guide The following minimum performance requirements are stipulated: 1.

508 CHAPTER 35 1959 Guide lent cleanout plug should be provided in the case of a .angle return connection.

458 CHAPTER 42 } 962 Guide And Data Book Storage at 0 F or below resulted in minimum changes, even after nine months.

June 17# 1953 / (rtOr'Z' Dr.

Lung Cancer and the Petroleum Industry in Louisiana Marise S.

FILE NAME: Asten Hill (AH) DATE: 1956 Feb 29 DOC#: AH020 DOCUMENT DESCRIPTION: Memo ITMpK !

FILE NAME: Asten Hill (AH) DATE: 1957-1966 DOC#: AH051 DOCUMENT DESCRIPTION: List of Suppliers' Purchase Data aten Hill trandon t .

FILE NAME: New York State & NY Times (NY) DATE: 1952 DOC#: NY002 DOCUMENT DESCRIPTION: Journal Article - The Program of the NY State Occupational Cancer Committee A .