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Recent content by kamatr

  1. kamatr

    Code Case 2523

    It is my understanding that the reference to Code Case 2523 is no longet required when using differing systems of units as it is now addressed in the code itself - see Section U-4, 2006 Addenda - 2004 Edition of ASME BPVC VIII Div.1; also the case in the 2007 Edition.
  2. kamatr

    Bracing for nozzle instead of reinforcing pad

    One other important element to remember is that gussets impart out-of-plane loads on the vessel shell and in the main, shell structures do not cope well with out-of-plane loads particularly if the loads are of a dynamic nature (arising from agitatators or similar). There are two failure cases...
  3. kamatr

    FLARE STACK- MECHANICAL CALCULATIONS- EARTHQUAKE AND WIND

    Take a look at "Tubular Steel Structures - Theory and Design" by M.S. Troitsky (published by the James F. Lincoln Arc Welding Foundation, Library of Congress Number - 81-80993)
  4. kamatr

    PD5500 Question

    In Annex C of PD 5500:2000 Symbol "m" is defined as "the index in equation of fatigue design curve (see table C.1)" Formula C-5 is of the form "Sr^m * N = A" where: Sr = Stress Range (N/sq.mm) m = as noted above N = is the design curve fatigue life (cycles) A = is...
  5. kamatr

    CE Certification

    Agree with observations of the previous respondents. A very useful document (available as PDF downloadable) is the "Pressure Equipment - Guidance notes on the UK Regulations (URN 99/1147)" from the UK Department of Trade and Industry (www.dti.gov.uk/strd/strdpubs.htm#pressure) which is...
  6. kamatr

    Metal temperatures in Double Pipe Heat Exchangers

    Just to thank the respondents on suggesting Kern (which I had looked at) and TEMA (which I had forgotten about not having been involved with S&T HE's for quite a while - Section T-4.32 being what I was looking for). Just for information, I was seeking to establish a mean metal temperature of the...
  7. kamatr

    Metal temperatures in Double Pipe Heat Exchangers

    Require assistance in finding a straight forward routine to establish the metal temperature in the inner pipe of a double pipe heat exchanger. Outer pipe/jacket has the heating medium (in this case LP steam) and the inner pipe has the medium to be heated (in this case a hydrocarbon gas).

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