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  1. dbachovchin

    relatively thick orifice

    I want to calculate pressure drop across a small (0.038 in), non-sharp-edged relatively thick (0.060 in) orifice. Flow is not choked, but Reynold number is high. There are big pipes on both sides. Using Perry, discharge coefficient is 0.61. This corresponds to 2.7 velocity heads. If...
  2. dbachovchin

    Orifice DP radial into high velocity stream

    I have a very high velocity gas stream inside a pipe. The pipe has several small holes in it, with a higher pressure gas on the outside. I need to calculate the pressure drop into the pipe. I know the equations for contaction and expansion loss, but how do I assess the loss due to direction...
  3. dbachovchin

    Combined heat and mass transfer

    The Dittus Boelter and Sieder Tate relations may be used for heat transfer coefficients. Analogous forms with Sh and Sc instead of Nu and PR may be used for mass transfer. Does the resulting expression meed to be corrected or modified if their is simultaneous heat transfer? i.e. Is there a...
  4. dbachovchin

    Tubing roughness

    Where can I find a comprehensive list of pipe and tube roughnesses for fluid flow pressure loss calculation? Lists in standard texts are very short.

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