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Recent content by PhilEduard

  1. PhilEduard

    Weld Strength Reduction Factor

    Hi Davefitz, Thank you so much for your tip and information. I really do appreciate your time on this. Regards, Phil
  2. PhilEduard

    Weld Strength Reduction Factor

    All, Power piping does not consider weld srength reduction factor W (Wc in Caesar II) but process pipng does and B31.3 addresses a situation where at temp. more than 1500 deg F., W should be obtain by the Designers themselves. Does anyone knows where this figure would come normally? Thanks...
  3. PhilEduard

    High pressure steam supporting?

    Hi Tim, Let me say something here in my opinion. First of all supporting any pipe at elbows are often discourage by stress engineers simply becuase more often the method to locally analyze the stresses at this point is not readily available.There has been no module in Caesar II and perhaps any...
  4. PhilEduard

    maximum shear load -pipe shoe and support

    Journeyman1972 Using teflon slide plates on pipe shoe evolves normally from pipe stress analysis. A system for example, consists of piping and equipment as pumps, vessels, etc., and of course you have pipe supports. Pipe supports are of different in nature say it could slide, it could be...
  5. PhilEduard

    Heat Exchanger Nozzle Allowable

    A great help John. Nice to feel you're always around. Thanks a lot and regards. Phil
  6. PhilEduard

    Heat Exchanger Nozzle Allowable

    So far I did have Stress Handbook by Helguero though I've not used it for a long time (a lot are not applicable anymore). And there was not a shell and tube type Heat Exchanger included but an air cooled type even then that current Caesar II module includes only the air cooled type. For a 24" to...
  7. PhilEduard

    Gas Density - Nitrogen

    Hi there Harvey, We'll sure you are absolutely right. My pressur is in gauge and I need to add 14.7 to make it absolute. I'll surely download your software and I'll visit your software homepage too. Thanks a lot for your quick help. Regards, Phil
  8. PhilEduard

    Gas Density - Nitrogen

    Hi there guys, I know this is the right forum for this question and I believe too mostly are working on process engineering. This question could be very simple for you but it took me a while to figure it out simply becuase of the metric unit I'm not use to. I have a system running on compressed...
  9. PhilEduard

    Pressure Thrust

    I thank you all guys for refreshing me on this subject. It's been a while (35 years) since I grauated my college and it's interesting to meet incidentally pressure thrust on piping system other than 90 degree. I have confirmed all your mentoring from the hydraulic books. Funny because I asked a...
  10. PhilEduard

    Pressure Thrust

    rconner, thank you so much for a quick reply. More power to you. Phil
  11. PhilEduard

    Pressure Thrust

    I thought quickly this could be easy but it seems to give me a bit of confusion. Where you realized a pressure thrust exist, you simply multiply the inside crossectional area of the pipe with its operating pressure and, that is if the change in direction is 90 degree. How do you evaluate this...
  12. PhilEduard

    Strange forces on restraints

    Scalabres, You need to join or you can be a visitor I think in the forum at COADE: http://www.coade.com/support_discussion.asp. And, simply copy and paste your problem in there. Phil
  13. PhilEduard

    Strange forces on restraints

    Scalabres, For the benifit of other who might encounter this same problem in the future, could you post this thread on COADE Caesar forum? This issue is more suited in that forum. Thanks. Phil
  14. PhilEduard

    Bending or Bending + Torsion

    Thanks Greg. After seeing a nice photo of the actual design I agree you are right. Thanks a lot.
  15. PhilEduard

    Bending or Bending + Torsion

    Hi all, I am evaluating an extended trunnion at the bottom of pipe. Imagine a horizontal pipe and sticking 270 degree (below the pipe) is a trunnion which is also a pipe and the length is about 2 feet from the center of the carrier pipe. To prevent the carrier pipe from moving (the pipe in...

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