American Society of Heating and Ventilating Engineers Guide, 1930 (VOJf d+BfUdpuOJ t 418 F ig. 1.

American Society of Heating and Ventilating Engineers Guide, 1930 many materials produce better results if dried quickly at comparatively high temperatures than if dried more slowly at lower temperatures.

American Society of Heating and Ventilating Engineers Guide, 1930 Its solubility in water, like all gases, is dependent upon the temperature and partial pressure.

American Society of Heating and Ventilating Engineers Guide, 1930 Table 1.

Copyright, 1931 BY American Society of Heating and Ventilating Engineers AND BY IT Dedicated .

American Society of Heating and Ventilating Engineers Guide, 1931 air is 1.34, based on the values given in Table 1, and when increased by the factor 3 to allow for moving air, the outside surface coefficient is 3 X 1.34 or 4.02 B.t.u. per hour per square foot per degree fahrenheit difference between the surface and the air in contact with it.

American Society of Heating and Ventilating Engineers Guide, 1935- Using the prices shown in Table 5, the cost of the 1,600 ft. of shown in Fig. 11, is S3,193.

American Society oj Heating and Ventilating Engineers Guide, 1935,:.

American Society of Heating and Ventilating Engineers Guide, 1932 Table 1.

American Society of Heating and Ventilating Engineers Guide, 1932 Table 24.

American Society of Heating and Ventilating Engineers Guide, 1932 of Mines and the lower curves show the averages of the pounds of water evaporated per pound of coal under similar and normally good operating conditions.

American Society of Heating and Ventilating Engineers Guide, 1932 Fig. 13.

T able 1.

American Society of Heating and Ventilating Engineers Guide, 1932 10 and 50 fpm, depending on the nature and texture of the sheets.

American Society of Heating and Ventilating Engineers Guide, 1934 Table 2.