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Vapors for heat engines, including considerations relating to the use of fluids other than steam for power generation; a study of desirable vacuum limits in simple condensing engines: methods for computing efficiencies of vapor cycles with limited expansion and superheat; a volume-temperature equation for dry steam, and new temperature-entropy diagrams for various engineering vapors (1912)

Ennis, William D. (William Duane), b. 1877 · New York, D. Van Nostrand Company · leaf 38

An illustration from Vapors for heat engines, including considerations relating to the use of fluids other than steam for power generation; a study of desirable vacuum limits in simple condensing engines: methods for computing efficiencies of vapor cycles with limited expansion and superheat; a volume-temperature equation for dry steam, and new temperature-entropy diagrams for various engineering vapors, 1912, leaf 38
246X 312.35= 77.0 1960 Carbon bisulphide. . 0.260X 176.19= 45.9 1520 Carbon chloride 0. 238 X 118. 95 = 28.3 1190 Steam 0.279X1143.53 = 319.0 4000 (b) Initially Dry Vapor, 302° to 110°Steam... 0.231X1101.66= 255.0 3570 (c) Vapors with Superheat at 600° F. Steam 0.272X1257.5 =342 4150 Alcohol 0.278X… … Fig. 3.—Turbine Characteristics with Frictionless Buckets (a) (6) Jet velocity ab, ab ab Peripheral velocity ac, ed ac, ac, ed, ed Absolute exit velocity ec, ec ec, ec Rotative components of ] . .. . ... , ,.. , . absolute exit velocities} cf> cf (negatlve) <*/(negative) tities of heat…

Heat-engines · Vapors

Internet Archive · Library of Congress · Public Domain Mark 1.0. Free to use for anything.

More pictures from Vapors for heat engines, including considerations relating to the use of fluids other than steam for power generation; a study of desirable vacuum limits in simple condensing engines: methods for computing efficiencies of vapor cycles with limited expansion and superheat; a volume-temperature equation for dry steam, and new temperature-entropy diagrams for various engineering vapors

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