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32 pounds of air contains one pound of O.] [Footnote 25: Per pound of C in the CO.] [Footnote 26: Ratio by volume of O to N in air.] [Footnote 27: Available hydrogen.] [Footnote 28: See Table 31, page 151.] [Footnote 29: This formula is equivalent to (10) given in chapter on combustion. 34.56 = theoretical air required for combustion of one pound of H (see Table 31).] [Footnote 30: For degree of accuracy of this formula, see Transactions, A. S. M. E., Volume XXI, 1900, page 94.] [Footnote 31: For loss per pound of coal multiply by per cent of carbon in coal by ultimate analysis.] [Footnote 32: For loss per pound of coal multiply by per cent of carbon in coal by ultimate analysis.] [Footnote 33: The Panther Creek District forms a part of what is known as the Southern Field; in the matter of hardness, however, these coals are more nearly akin to Lehigh coals.] [Footnote 34: Sometimes called Western Middle or Northern Schuylkill Field.] [Footnote 35: Geographically, the Shamokin District is part of the Western Middle Mahanoy Field, but the coals found in this section resemble more closely those of the Wyoming Field.] [Footnote 36: See page 161.] [Footnote 37: U. S. Geological Survey.] [Footnote 38: See "Steam Boiler Economy", page 47, First Edition.] [Footnote 39: To agree with Pfaundler's formula the end ordinates should be given half values in determining T", _i. e._, T" = ((Temp. at B + Temp. at C) / 2 + Temp. all other ordinates) / N] [Footnote 40: B. t. u. calculated.] [Footnote 41: Average of two samples.] [Footnote 42: Assuming bagasse temperature = 80 degrees Fahrenheit and exit gas temperature = 500 degrees Fahrenheit.] [Footnote 43: Dr. Henry C. Sherman. Columbia University.] [Footnote 44: Includes N.] [Footnote 45: Includes silt.] [Footnote 46: Net efficiency = gross efficiency less 2 per cent for steam used in atomizing oil. Heat value of oil = 18500 B. t. u. One ton of coal weighs 2000 pounds. One barrel of oil weighs 336 pounds. One gallon of oil weighs 8 pounds.] [Footnote 47: Average of 20 samples.] [Footnote 48: Includes H and CH_{4}.] [Footnote 49: B. t. u. approximate. For method of calculation, see page 175.] [Footnote 50: Temperatures are average over one cycle of operation and may vary widely as to maximum and minimum.] [Footnote 51: Dependant upon length of kiln.] [Footnote 52: Results secured by this method will be approximately
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