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TECHNICAL PAPERS

Isentropic Compressible Flow for Non-Ideal Gas Models for a Venturi

[+] Author and Article Information
Kenneth C. Cornelius, Kartik Srinivas

Department of Mechanical and Materials Engineering, 3640 Colonel Glenn Hwy., Wright State University, Dayton, Ohio 45435-0001

Phone: (937) 775-5091, Fax: (937) 775-5009

J. Fluids Eng 126(2), 238-244 (May 03, 2004) (7 pages) doi:10.1115/1.1677499 History: Received March 20, 2002; Revised September 15, 2003; Online May 03, 2004
Copyright © 2004 by ASME
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References

Halmi,  D., 1974, “Metering Performance Investigation and Substantiation of the “Universal Venturi Tube” (U.V.T.),” ASME J. Fluids Eng., 96, pp. 124–131, 132–138.
Miller, R. W., 1996, Flow Measurement Engineering Handbook, 3rd Edition, McGraw Hill, NY, pp. 2.15–2.21, 2.110–2.112, 13.3–13.33, I1–I13.
Thompson,  P. A., and Sullivan,  D. A., 1978, “Exact and Approximate Equations for Real-Fluid Isentropic Flow,” ASME J. Fluids Eng., 100, pp. 413–418.
Sullivan,  D. A., 1981, “Historical Review of Real-Fluid Isentropic Flow Models,” ASME J. Fluids Eng., 103, pp. 258–267.
Fox, R. W., and McDonald, A. T., 1998, Introduction to Fluid Mechanics, 5th Edition, John Wiley and Sons, Inc., NY, pp. 353–357.
White, F. M., 1991, Viscous Fluid Flow. McGraw Hill, NY, pp. 42–48, 406–422.
Morel,  T., 1975, “Comprehensive Design of Axisymmetric Wind Tunnel Contractions,” ASME J. Fluids Eng., 97(2), pp. 225–233.
Saad, M., 1992, Compressible Fluid Flow, 2nd edition, Prentice-Hall, NJ, pp. 87–116.
Cengel, Y. A., and Boles, M. A., 2002, Thermodynamics an Engineering Approach, 4th edition, McGraw Hill, NY, pp. 664–690, 867–869.
Howell, J. R., and Buckius, R. O., 1992, Fundamentals of Engineering Thermodynamics, 2nd edition, McGraw Hill, NY, pp. 622–628.
Bird, R. B., Stewart, W. E., and Lightfoot, E. N., 1966, Transport Phenomena, 2nd Edition, John Wiley & Sons, Inc., NY, pp. 469–473.
Martin,  J. J., and Hou,  Y. C., 1955, “Development of an Equation of State for Gases,” AIChE J., 1:142, pp. 142–151.
Downing, A., and Knight, K., 1971, “The Thermodynamic Properties of Refrigerant R-22,” DuPont Technical Bulletin RT-52.
McLinden,  M. O., Gallagher,  J. S., and Weber,  L. A., 1989, “Measurement and Formulation of the Thermodynamic Properties of R-134a and 123,” ASHRAE Trans., 95(2), pp. 263–283.
Bivens, D. B., and Yokozeki, A., 1996, “A Blend of R125/R143a/R134a With Mass Percentages of 44%/52%/4%, R-404a,” Intl. Conference on Ozone Protection Technologies, Washington, DC, also“The Thermodynamic Properties of SUVA HP62 Refrigerant R-404a,” DuPont Technical Bulletin T-HP62.
Lemmon,  E. W., Jacobsen,  R. T., Penoncello,  S. G., and Friend,  D. S., 2000, “Thermodynamic Properties of Air and Mixtures of Nitrogen, Argon, and Oxygen from 60 to 2000 K at Pressures to 2000 MPa,” J. Phys. Chem., 29(3), pp. 12–32.

Figures

Grahic Jump Location
Venturi meter at the entrance of a plenum
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P versus T for refrigerants and air
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P versus ρ for refrigerants and air
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z versus T for refrigerants and air
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Exponent k versus ρ for refrigerants
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Φm versus (δP/PT) real versus ideal comparison for refrigerants
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Mach versus (δP/PT) real versus ideal for refrigerants and air
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P versus v diagram for air with constant isentrope lines
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Exponent values and z versus P along isentrope for air

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