Now showing items 1-4 of 4

    • Entrance effects in a developing slug flow 

      Moissis, Raphael; Griffith, P. (Cambridge, Mass. : Massachusetts Institute of Technology, Division of Industrial Cooperation, [1960], 1960)
      The kinetics of a Taylor bubble, as it rises behind a series of other bubbles in a gas-liquid slug flow, have been determined. The rise velocity of a bubble is expressed as a function of separation distance from the bubble ...
    • Heat transfer and pressure drop in tape generated swirl flow 

      Lopina, Robert F.; Bergles A. E. (Cambridge, Mass. : M.I.T. Dept. of Mechanical Engineering, [1967], 1967)
      The heat transfer and pressure drop characteristics of water in tape generated swirl flow were investigated. The test sections were electrically heated small diameter nickel tubes with tight fitting full length Inconel ...
    • The Momentum flux in two-phase flow 

      Andeen, Gerry B.; Griffith, P. (Cambridge, Mass. : M.I.T. Division of Sponsored Research, [1965], 1965)
      The average momentum flux at a section of a pipe with twophase upflow has been measured by the impulse technique. Steamwater and air-water mixtures were tested in one-inch and onehalf inch nominal pipes. Homogeneous ...
    • Two phase pressure drop in inclined and vertical pipes 

      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 ...