Refine
Estimated Years 1950-1959Clear
21,856 results foundRefine Search
404 CHAPTER 16 1954 Guide Commercial Standard US-51 is a method of rating oil-burning floor furnaces by test
Document image
refid# nq3VxBEoy2VQ5nJ1Q7KeXLd81 page
742 CHAPTER 33 1954 Guided Fans ,-W4X 743 No - SW, SI No 2 * 5W, SI No 3 - SW, SI No 3-OW, DI No 4 - SW, SI Counter-Clockwist Top Horizontal Clockwise Top Horizontal Clockwise Bottom Horizontal Counter-Clockwise Bottom Horizontal No 7 - SW, SI No 7 - DW, DI Fig. 6. .N8-SW,SI.
Document image
refid# NEX64Lb76g8V1v95YOz4ywMnE1 page
996 CHAPTER 45 1954 Guide heat, effective temperature, and body heat balance.
Document image
refid# Rjdy3mDXgzYjYkwMBx7KkqKon1 page
1122 .
Document image
refid# peONm4kQ8ELYxgKR9b8QMM2gw1 page
518 CHAPTER 21 1955 Guide to2in.
Document image
refid# ebRznM8XD5XYqzenxxxj1KGq1 page
596 CHAPTER 25 . : -1955 Guide BOILER CAPACITY FOR STEAM UNIT HEATERS The capacity of the boiler should be based on the rated capacity of the unit heaters at the lowest entering air temperature and highest fan speed that will occur, plus an allowance for pipe line losses; It is unwise to in stall a single unit heater as the sole load on any boiler, particularly if the unit heater motor is started and stopped by thermostatic control.
Document image
refid# BvGzMQGKjL3YBGoo9NKG1zV7o1 page
6'28* ( CHAPTER 27 1955 Guide; TjfBtE?
Document image
refid# pZdeBzkQND9KV4xVqGDv0V6a1 page
656 CHAPTER 28 1955 Guide manufacturers to suit their products, and others by applicators and users.
Document image
refid# rpv4Z0LGG2K7KNDLVbyaoZV4V1 page
704 For a long slot CHAPTER 31 1955 Guide (8a) where Qz = total volume flow rate at distance X from face of outlet, cubic, feet per minute.
Document image
refid# rp9p5Dj423v4VYoGv3M3Z6pKa1 page
838 CHAPTER 36 1955 Guide where U = overall coefficient of heat transfer, Btu per (hour) (square foot external surface) (Fahrenheit degree mean temperature difference between air and fluid within the coil). f, -- film coefficient ofheat transfer between the internal surface of the coil and the fluid flowing within the coil, Btu per (hour) (square foot internal sur face) (Fahrenheit degree mean temperature difference between that surface and the average fluid temperature). /,, = film coefficient of heat transfer between air and the external surface of the coil, Btu per (hour) (square foot external surface) (Fahrenheit degree mean temperature difference between the mass' of air and the external surface). k -- conductivity of material from which the bare pipe is constructed, Btu per (hour) (square foot) (Fahrenheit degree per inch thickness).
Document image
refid# mmYxYqNG0YzkNXmx5x3Db51Xb1 page
934 CHAPTER 41 1955 Guide^ i- r preciable velocity has not yet been mastered, although it is a subject of ' current investigation.
Document image
refid# jgREO8n2ZY4K0JNgapbRme7MR1 page
1010 CHAPTER 45 1955 Gwa'p '' Table , 1.--- Temperatures and Humidities Applicable to Industrial Aisi?
Document image
refid# v1Nom9LZg3m66jJqEgDeammjZ1 page
14 CHAPTER 2 1956 Guide 1!
Document image
refid# e1vGkBGY7pJKmyD8rxajZ0ka41 page
264 CHAPTER 12 1956 Guide necessary to make an allowance for floor heat loss from rooms located over the basement.
Document image
refid# G5B3Gd8mdQoOL41Q00N6V7yYV1 page
I/Sl jbhns-Manviiia u c ef VEinternal Correspondence' To: File, LEGAL DEPARTMENT i From: W.
Document imageDocument imageDocument image
refid# GX28b4L40yK9wX34EYeoBX2q3 pages