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#1
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| The image that contains the equations can be found over at http://members.shaw.ca/ckcc/tmp/equations.gif. It doesn't look like a pure physics equation, but I figured I might have some luck in here. Thanks for your time and courtesy! |
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#2
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| "Steve Lee" <[Only registered users see links. ]> wrote in message news:[Only registered users see links. ]... You're right. It *doesn't* look like a pure physics equation, but it *does* look like the kind of ad hoc expression that might be developed by an engineer, especially the alternate expressions for k in (2) that depend on the relative values of H/W and sqrt(3). Also, the variables used are all consistent with variables used in fluid flow: Q is often used for a flow rate, the Greek letter eta (the "n"-like letter) for viscosity, T for temperature, v for velocity, the Greek letter gamma (the "y"-like letter) for specific weight, H for hydrostatic head (height), W for weight, T for temperature or kinetic energy or time or torque, k for various constants, A for cross-sectional area, and d is a symbol for a difference. This collection of variables would seem to apply to flow of a viscous liquid through a conduit. I can't help you much beyond that as I am a chemist, not an engineer. HTH Tom Davidson Richmond, VA |
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#3
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| Dear Steve Lee: "Steve Lee" <[Only registered users see links. ]> wrote in message news:[Only registered users see links. ]... tadchem has the right of it. Through sheer intuition and years of abuse at the "hands" of engineers, he has correctly identified empirical relations for heat transfer. The Q_dot is the giveaway, and it is "heat flow" (units of watt or its ilk). I would guess some sort of convective heat transfer from a surface "H" high, by "L" wide. Will it be necessary for me to dig my Heat Transfer book out, and name the relation, or at least its progenitor? David A. Smith |
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#4
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| "N:dlzc D:aol T:com (dlzc)" <N: dlzc1 D:cox T:[Only registered users see links. ]> wrote in message news:ebhQc.1624$xk.634@fed1read01... <snip> Thank you, David. I was stalled over why the 'dT' term would have been there, but then I have never had to calculate characteristics of heat exchangers before. Tom Davidson Richmond, VA |
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#5
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| Hi Tom, "tadchem" <[Only registered users see links. ]> wrote in message news:[Only registered users see links. ]... dig It is poorly presented. This is usually "deltaT" or "/\T", representing the difference between bulk fluid and.exchanger "root" temperature (if I recall corrrectly). It should not have been presented in the "universally recognized" differential form, even though no other "d_" term was present. Leave it to an engineer... David A. Smith |
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#6
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| I understood that dT referred to w temperature *difference* rather than a *differential.* I was just a bit slow in completing the relation: [viscosity] + [temperature difference] => [convection] Thanks again. Tom Davidson Richmond, VA |
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#7
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| equations , image , represents |
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