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Browsing Heat Transfer Laboratory Technical Reports by Issue Date

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Browsing Heat Transfer Laboratory Technical Reports by Issue Date

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  • Hill, Wayne S.; Rohsenow, Warren M. (Cambridge, Mass. : Heat Transfer Laboratory, Dept. of Mechanical Engineering, Massachusetts Institute of Technology, [1982], 1982)
    Dispersed flow film boiling is characterized by liquid-phase droplets entrained in a continuous vapor-phase flow. In a previous work at MIT, a model of dispersed flow heat transfer was developed, called the Local Conditions ...
  • Hull, Lawrence M.; Rohsenow, Warren M. (Cambridge, Mass. : Heat Transfer Laboratory, Dept. of Mechanical Engineering, Massachusetts Istitute of Technology, [1982], 1982)
    Dispersed flow film boiling consists of a dispersion of droplets which are carried over a very hot surface by their vapor. This process occurs in cryogenic equipment and wet steam turbines. It is also of interest in the ...
  • Yoder, Graydon L.; Rohsenow, Warren M. (Cambridge, Mass. : Heat Transfer Laboratory, Dept. of Mechanical Engineering, Massachusetts Institute of Technology, [1980], 1980)
    Dispersed flow consists of small liquid droplets entrained in a flowing vapor. This flow regime can occur in cryogenic equipment, in steam generators, and during nuclear reactor loss of coolant accidents. A theoretical ...
  • Kendall, Gail E.; Rohsenow, Warren M. (Cambridge, Mass. : Heat Transfer Laboratory, Dept. of Mechanical Engineering, Massachusetts Institute of Technology, [1978], 1978)
    Heat transfer to drops impacting on a hot surface is examined in context of dispersions of flowing, boiling fluids. The liquid contribution to heat transfer from a hot tube to a two-phase dispersion is formulated in terms ...
  • Plummer, David N. (Cambridge, Mass. : Heat Transfer Laboratory, Department of Mechanical Engineering, Massachusetts Institute of Technology, 1974, 1974)
  • Griffith, P.; Lau, Chun Woon.; Hon, Pou Cheong.; Pearson, John Franklin. (Cambridge : Heat Transfer Laboratory, [1973], 1973)
    A method of calculating the pressure drop in inclined and vertical oil-gas wells is proposed. The data used to establish the method is from a variety of sources but is largely from air and water flowing in systems close ...
  • Iloeje, Onwuamaeze C.; Plummer, David N.; Rohsenow, Warren M. (Cambridge, Mass. : M.I.T. Heat Transfer Laboratory, [1972], 1972)
    The mechanism of collapse of forced cnnvection annular vertical flow film boiling, with liquid core, is investigated using liquid nitrogen at low pressures. The report includes the effect of heat flux from the buss bar. ...
  • Lorenz, J. J.; Mikic, B. B.; Rohsenow, Warren M. (Cambridge, Mass. : M.I.T. Engineering Projects Laboratory, [1972], 1972)
    A unified model relating surface variables to the nucleate pool boiling characteristics was developed. A simple vapor trapping mechanism was postulated and a geometrical model constructed for idealized conical cavities ...
  • Bar-Cohen Avram; Bergles A. E. (Cambridge, Mass. : M.I.T. Heat Transfer Laboratory, [1971], 1971)
    A combined experimental and analytical investigation of boiling and condensation in a liquid-filled enclosure, with water and Freon- 113 as the working fluids, is described. The operating characteristics of a boiling system, ...
  • Murphy, Richard Walter; Bergles A. E. (Cambridge, Mass. : M.I.T. Heat Transfer Laboratory, [1971], 1971)
    A study was conducted of heat transfer and hydrodynamic behavior for subcooled flow boiling of Freon-113, one of a group of fluorocarbons suitable for use in cooling of high-power-density electronic components. Problems ...
  • Traviss, Donald P.; Baron, Anton G.; Rohsenow, Warren M. (Cambridge, Mass. : M.I.T. Heat Transfer Laboratory, [1971], 1971)
    High vapor velocity condensation inside a tube was studied analytically. The von Karman universal velocity distribution was applied to the condensate flow, pressure drops were calculated using the Lockhart- Martinelli ...
  • Traviss, Donald P.; Rohsenow, Warren M. (Cambridge, Mass. : M.I.T. Heat Transfer Laboratory, [1971], 1971)
    The influence of return bends on the downstream pressure drop and heat transfer coefficient of condensing refrigerant R-12 was studied experimentally. Flow patterns in glass return bends of 1/2 to 1 in. radius and 0.315 ...
  • Roca, Richard T.; Mikic, B. B. (Cambridge, Mass. : M.I.T. Dept. of Mechanical Engineering, [1971], 1971)
    The contact conductance at an interface can be determined by knowing the material and surface properties and the interfacial pressure distribution. This pressure distribution can be influenced strongly by the roughness of ...
  • Bergles A. E.; Brown, G. S.; Lee, R. A.; Simonds, Richard R.; Snider, Warren Dean. (Cambridge, Mass. : M.I.T. Heat Transfer Laboratory, [1970], 1970)
    This report summarizes a three-year program concerned with obtaining basic design information for tubes having a random roughness on the inside wall (RID) and tubing having continuous internal fins (Forge Fin). Test apparatus ...
  • Gould, Herbert Hirsch; Mikic, B. B. (Cambridge, Mass. : M.I.T. Engineering Projects Laboratory, [1970], 1970)
    When two plates are bolted (or riveted) together these will be in contact in the immediate vicinity of the bolt heads and separated beyond it. The pressure distribution and size of the contact zone is of considerable ...
  • McMillan, Robert; Mikic, B. B. (Cambridge, Mass. : M.I.T. Engineering Projects Laboratory, [1970], 1970)
    This work considers the effect of roughness and waviness on interfacial pressure distributions and interfacial contact resistance. It is shown that for moderate roughness the contour area could be substantially different ...
  • Bae, Soonhoon; Maulbetsch, John S.; Rohsenow, Warren M. (Cambridge, Mass. : M.I.T. Heat Transfer Laboratory, [1970], 1970)
    High vapor velocity condensation inside a tube was studied theoretically. The heat transfer coefficients were calculated by the momentum and heat transfer analogy. The Von Karman universal velocity distribution was applied ...
  • Bae, Soonhoon; Maulbetsch, John S.; Rohsenow, Warren M. (Cambridge, Mass. : M.I.T. Heat Transfer Laboratory, [1969], 1969)
    High vapor velocity condensation inside a tube was studied theoretically. The heat transfer coefficients were calculated by the momentum and heat transfer analogy. The Von Karman universal velocity distribution was applied ...
  • Eryou, N. Dennis; Glicksman, Leon R. (Cambridge, Mass. : M.I.T. Engineering Projects Laboratory, [1969], 1969)
    One dimensional temperature profiles and heat fluxes within a slab of molten glass were measured experimentally. The glass slab was contained in a platinum foil lined ceramic tray inside a high temperature furnace. An ...
  • Hynek, Scott Josef; Rohsenow, Warren M.; Bergles A. E. (Cambridge, Mass. : M.I.T. Dept. of Mechanical Engineering, [1969], 1969)
    This report presents the latest results of an investigation of the characteristics of dispersed flow film boiling. Heat transfer data are presented for vertical upflow of nitrogen in an electrically heated tube, 0.4 in. ...
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