HEATING VENTILATINC AIR CONDITIONING GUIDE 1943 , at a constant level slightly lower than the outlets of the atomizers them selves and is drawn constantly to the atomizer by aspiration when com pressed air is supplied.

HEATING VENTILATING AIR CONDITIONING GUIDE 1943 and economical operation, all automatically-fired gas burners ;should be equipped with pressure regulators on the gas supply line.

HEATING VENTILATING AIR CONDITIONING GUIDE 1943 governed by the amount of pressure which can be spared in overcoming resistance to flow of a given volume of water per unit of time.

HEATING VENTILATING AIR CONDITIONING GUIDE 1943 RICE, Robert B.

HEATING VENTILATING AIR CONDITIONING GUIDE 1943 President________ 1st Vice-President2nd Vice-Presidents Treasurer__ ______ Secretary__________ _A.

HEATING VENTILATING AIR CONDITIONING GUIDE 1944 Table 9.

>M HEATING VENTILATING AIR CONDITIONING GUIDE 1944 CHAPTER I.

HEATINC VENTILATING AIR CONDITIONING GUIDE 1944 METHOD OF DESIGNING FORCED-AIR HEATING SYSTEMS6 1.

HEATING VENTILATING AIR CONDITIONING CUIDE 1944 Heat in air exhausted from oven at 422 F per pound fuel burned = 0.333 X 123.9 X (Sm - Sn) = 41.3 (91 - 8.6) = 3,400 Btu.

2 Chapter 1 Table 1.

Chapter 14_________________ ' 1945 Guide' 34 lb.

- 414 Chapter 22 194S Guide the other hand, remote type room unite contain less mechanical ma chinery, avoid the operating cost penalty of an air-cooled condenser, as in the case of the self-contained, air-cooled room units, and seldom require heavy wiring to handle the fan load.

436 ____________ ;Chapter 23________________________________ 1945 Guide COMPARISON OF METHODS OF DEHUmSStCATION 7 ~ Almost all summer comfort air conditioning, as well as much industrial and commercial air conditioning, requires both, of the functions of sensible and latent heat removal from air.

432 Chapter 23 1945 Guide the main'brine reservoir for. re-pumping.

508 Chapter 26 1945 Guide A section of a typical counter-flow tower is shown-in-Fig.- 4:--If- the reduction in water rate due to evaporation within the volume is neglected, the energy balance for this differential section of the exchanger volume may be written as: ., L c dt = G dh "- -_ (2) The potential for net energy transfer due to heat and mass transfer from the water to the mixture in contact with it may be expressed with reasonable accuracy as the difference between the enthalpy of saturated air at the water temperature, An, and the enthalpy of the main stream air vapor mixture7, Aa.