424 CHAPTER 17 1952 Guide opening of windows, abnormal heating of the building, poor design of heat ing system, sun effect, and other variations.

428 CHAPTER 17 1952 Guide "deg below 65 F.

674 CHAPTER 31 1952 Guide -lengths and mean'velocities of flow as a circular duct of the same hydraulic diameter.

1070 1952 Guide Page JOHNS-MANVILLE, 22 East 40th St., Hew York 16, N.

106 CHAPTER 5 1953 Guide ; PERIODIC AND TRANSIENT HEAT FLOW The foregoing data and examples dealt with steady-state heat transfer (not varying with time).

102 CHAPTER 5 1953 Guide Rz, and into the water stream through the convection,resistance,, Rx.

346 CHAPTER 14 , 1953 Guide Table 8.

August 26, 1955 Mr* Hugh U, Jackson, dinner Industrial Health Program Johns-MinvUle Corporation 22 East 40th Street Hew York 16, New York Dear Hught The enclosed letter la self-explanatory* We did not feel that we could reply la eorreapoBde&ee to Mr, Kane, aad there* fore invited him to the Institute for a conference.

V) March 8, 1957 Ivan Sabourin, E*q c/o Hots!

90 CHAPTER 5 1954 Guide in the eddy or turbident region the major fraction of the transfer occurs by eddy mixing.

CHAPTER 19 1954 Guides 458 an.i *-'**> ?"

860 CHAPTER 37 1954 Guide Table. 9.

994 CHAPTER 45 1954 Guide Design of Dilution Systems !

EDGE INDEX for HEATING VENTILATING AIR CONDITIONING GUIDE 1954 Chapter No.

226 CHAPTER 11 1955 GuideJl| are indicative of what might be expected in this connection, but it should^ be noted that Table 3 is based on a no-wind condition, and therefore notif?