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Heat Transfer Laboratory Technical Reports

Research and Teaching Output of the MIT Community

Heat Transfer Laboratory Technical Reports

 

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  • Film boiling on the inside of vertical tubes with upward flow of the fluid at low qualities 
    Dougall, R. S.; Rohsenow, Warren M. (Cambridge, Mass. : Dept. of Mechanical Engineering, Massachusetts Institute of Technology, [1963], 1963)
    Flow regimes, local heat transfer coefficients, and temperature distributions along the wall have been studied for film boiling inside a vertical tube with upward flow of a saturated liquid. The area of interest has been ...
  • The mechanism of void formation in initially subcooled systems 
    Griffith, P.; Snyder, George A. (Cambridge, Mass., M.I.T. Dept. of Mechanical Engineering, [1963], 1963)
    When an initially subcooled, water filled system undergoes a transient in heat flux or pressure such that bubbles form, the most important variable which determines the volume of the resulting void is the number of bubbles ...
  • The mechanism of void formation in initially subcooled systems 
    Griffith, P.; Snyder, George A. (Cambridge, Mass., M.I.T. Dept. of Mechanical Engineering, [1963], 1963)
    When an initially subcooled, water filled system undergoes a transient in heat flux or pressure such that bubbles form, the most important variable which determines the volume of the resulting void is the number of bubbles ...
  • Model of critical heat flux in subcooled flow boiling 
    Fiori, Mario P.; Bergles A. E. (Cambridge, Mass. : M.I.T. Dept. of Mechanical Engineering, [1968], 1968)
    The physical phenomenon occurring before and at the critical heat flux (CHF) for subcooled flow boiling has been investigated. The first phase of this study established the basic nature of the flow structure at CHF. A ...
  • The influence of return bends on the downstream pressure drop and condensation heat transfer in tubes 
    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 ...
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