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  1. dskjockey1

    Heat Exchanger Tubes

    Does anyone have a suggestion on how to simulate tubes when analyzing a tube sheet on a shell and tube TEMA type heat exchanger? I would rather not model each tube individually. I have thought of adding a hinge restraint to each tube hole but I am not sure that would simulate tubes properly on a...
  2. dskjockey1

    Pressure Vessel Nozzle w/ Moments

    I am new to using simulation and trying to analyze a nozzle in a 2:1 head configuration. The end of the nozzle is subjected to various forces and moments due to piping. There is no issues with modeling the forces but I am not sure how to apply the moments. Currently I have treated them as...
  3. dskjockey1

    UG-101 Proof Test

    Does a proof tested part per UG-101 ever expire in the eyes of the ASME Code? Does it ever expire for Alberta CRN registration? This would be a proof tested cover of a heat exchanger. Thanks!
  4. dskjockey1

    Joint Efficiencies for Nozzles

    See UG-37(a), Definition of "E" and "E1"
  5. dskjockey1

    ANSI/ASME Flanges

    Can I machine off the RF of a standard ANSI B16.5 flange without affecting the pressure rating of that flange? How about machining off 1/3 of the RF height? Thanks!
  6. dskjockey1

    Appendix 2 and Multi Chamber Vessels

    If I have a heat exchanger with a tubesheet sandwiched between two body flanges (one flange subjected to 100 psig shell side design conditions, one flange subjected to 800 psig tube side design conditions). Does Appendix 2 require me to design both body flanges to the worse case Wm1 and Wm2 of...
  7. dskjockey1

    Interpretation: VIII-1-89-227

    Does the same rule apply if I have wld pipe such as SA-312 304 Wld? Or is this only for Smls pipe shells?
  8. dskjockey1

    Interpretation: VIII-1-89-227

    According to this interpretation if I have smls pipe and a bolted joint at each end welded to the shell with a full penetration corner joint a JE = 1 is permitted. What if my weld attachments on both ends are loose type flanges (slip on flange / double fillet)? Can I still use a circumferential...
  9. dskjockey1

    Joint Efficiencies for Nozzles

    Yes I did. You are correct when you spot RT smls pipe you can claim a JE = 1. But per UW-11(a)(2) when full RT per code (not 100% all BW) is called for on a vessel, nozzles which have weld neck flanges attached to them that are < 10" NPS do not need to be radiographed in order for the vessel to...
  10. dskjockey1

    Joint Efficiencies for Nozzles

    E = 1 even though the nozzle weld will not be subjected to any RT? Remember, the shell may be radiographed but the nozzle does not have to be RT examined per code.
  11. dskjockey1

    Joint Efficiencies for Nozzles

    UW-11(a)(2) states that radiography is not required for Cat B and C butt welds in communicating chambers that do not exceed 10 NPS. If I have a vessel with Full Per Code RT and nozzles which are 6"-RFWN nozzles, can I take credit for a JE = 1 in my calculations for these nozzles even though...
  12. dskjockey1

    Spot RT and ERW Pipe

    This has probably been asked before but. If I perform spot RT on a circumferential joints of ERW (SA-53B) pipe is my longitudinal JE = 1 or .85? Thanks!
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