788 CHAPTER 36 1950Guide Table 5.

984 CHAPTER 48 1950 Guide Table 3.

90 CHAPTER 4 1951- Guide'Sj Coefficients for these taps have been adopted by the International Standard^.

328 CHAPTER 13 1951 Guide this is what is ordinarily meant when the heating value of a fuel is specified.

336 CHAPTER 13 1951 Guide forming a cone, the top of which should be level with the middle of the firing door.

536 CHAPTER 23 1951 Guide Convection Transfer Convection values of heat transfer are not easily established.

538 CHAPTER 23 1951 Guide Example 2.

604 CHAPTER 27 1951 Guide ness than that determined by the use of Fig. 6.

632 CHAPTER 30 1951 Guide on desks and may result in a sensation of draft.

688 CHAPTER 31 1951 Guide h0 -- friction loss under actual (operating) conditions, any consistent unite. he -- pressure loss due to sudden contraction, feet of fluid flowing. h0 = pressure loss due to sudden enlargement, feet of fluid flowing. hi = friction loss, feet of fluid flowing.

994 CHAPTER 47 1951 Guide class, are usually air conditioned.

656 CHAPTER 30 1952 Guide prevent the primary or inducedair stream from striking furniture and obstaclea, and producing objectionable drafts. .

738 CHAPTER 33 1952 Guide range is extended appreciably beyond that of the conventional cyclone.

886 CHAPTER 40 1952 Guide Sound Control 887 Fiq. 8.

968 CHAPTER 45 1952 Guide ical corrosion.