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Recent content by harvey13

  1. harvey13

    Duct Diameter ID/OD Convention?

    Thanks for the input. I think that this discussion highlights that the duct diameter should always be specified as I.D. or O.D. Arewin
  2. harvey13

    Duct Diameter ID/OD Convention?

    I've thought about this a little more and I think that industrial pipes (mainly dust collection) are assumed to be O.D. The dimensions of standard rolled angle/flange rings are listed by diameter, and the I.D. of these rings are 1/8" or 3/16" larger than the nominal dimeter of the pipe, i.e. a...
  3. harvey13

    Duct Diameter ID/OD Convention?

    Thanks Chris, The second half was just me running on too long, but also to make it clear that I know that ductwork can be just about any dimension. I would assume that industrial duct would be the same.
  4. harvey13

    Duct Diameter ID/OD Convention?

    We are having a discussion about duct diameters, and so I have a short question about Ductwork. Is there a generally accepted convention that understands that listing the size of a duct, automatically identifies the ID or OD of the duct? If so, which one? Is the convention the same for HVAC...
  5. harvey13

    Cooling Tower distribution piping pressure

    Sorry about the "vanishing", but I was out of the office w/o internet connection. I was asking about the water distribution basins in the tower, but we can let this thread die. Thanks for your help. Harvey13
  6. harvey13

    Cooling Tower distribution piping pressure

    What is a recommended pressure in the distribution header of a packaged cooling tower with 6-8 cells? The flow is balanced at each cell by a manual butterfly valve. I've been told to use 30 psig, but that seems like a lot of pump HP to waste. Will there be problems if I design the header...
  7. harvey13

    Non-Newtonian Pressure Drop (revisited)

    Gne77 I’ve been away from “my” computer for over a month, and since I’m old, I couldn’t remember by password and I wasn’t able to respond until today, so a belated thanks for the clarification. In the example from the 7JUL post I have a question. You have the “First Part” written as: (3 *...
  8. harvey13

    Non-Newtonian Pressure Drop (revisited)

    777gne I have tried to follow your conversation with Latexman, but there are too many gaps for me in the development of this equation and the thread from last year. Latexman had a different variation of your equation that I think was due to the units of the proportionality coefficient. I...
  9. harvey13

    Industrial Ventilation Program

    A client has asked if there is a computer program for Industrial Ventilation. The client is primarily interested in dust collection systems. A typical system has several hoods (different types) branch ducts, elbows, tees, main duct, collector, fan, etc. Can anyone recommend a program.
  10. harvey13

    Journal brg/pin design for Draw Bar mech

    Recommendations for journal bearing & pin design: mat'l, pin surface finish & hardness, design contact pressure, lubrication. The draw bar linkage mechanism has very high loads >500,000 lbs and moves very slowly so that velocity and angular travel <30deg between the pins and bushings is very...
  11. harvey13

    Example Calculations - Flow & Pressure Drops, etc.

    Would like suggestions for text or workbook, etc. with sample industrial ventilation problems.
  12. harvey13

    guyed stack design

    Is there a 'standard' for the design of guyed stacks published by some organization?&nbsp;&nbsp;I am familar with wind pressures (25-33 lbs/sqft - 100mph) and wind loads (pressure x projeted area).&nbsp;&nbsp;I am less familar with accepted methods of calculating critical buckling loads...

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