Page:Journal of the American Society of Mechanical Engineers, Volume 33.pdf/681

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APPENDIX No. 4

DERIVATION OF FORMULA [6] GIVING THE EQUATION OF THE ADIABATIC SATURATION LINE

86Assuming 1 lb. of pure air having the temperature containing lb. of moisture with the corresponding dew point hand vapor pressure having a resultant adiabatic saturation temperature of , assume also a moisture increment under adiabatic conditions resulting in a temperature increment of . This moisture increment is evidently evaporated at a vapor pressure corresponding to temperature and superheated to temperature . The temperature of the liquid is evidently constant at temperature , from principle C. The total heat of the vapor in the increment is , where is the total heat of steam corresponding to temperature and vapor pressure , and is the heat required to superheat from saturation temperature to dry-bulb temperature . The heat of the liquid evaporated, however, is corresponding to temperature of saturation .

87 The total heat interchange required to evaporate under these conditions is therefore

[40]

The change in sensible heat of 1 lb. of air and lb. of water vapor due to the temperature increment is

[41]

Since the change is adiabatic these values may be related by the equation

[42]

[43]

in which and </math>t_1</math> are variables corresponding to the variable while is a variable related to by the different equation. A constant corresponding to is while , may be taken approximately as a mean between its values at and at and as a mean between its values at and at . The temperature of saturation is , and is the corresponding moisture content at saturation.

88It is not necessary, however, to solve this equation in this form as this relationship may be simplified.

[44]

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