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  1. CMA010

    Distillation Column relief load for simultenous loss of feed and ovhd cooling/reflux.

    Make a flash curve of the bottoms product and make corresponding reboiler duty and relief rate calcs for each vapourisation step. For a narrow boiling mixture I wouldn't bother tho'.
  2. CMA010

    Distillation Column relief load for simultenous loss of feed and ovhd cooling/reflux.

    What is optimistic about the assumption of the normal bottoms composition during relief? Doesn't the manual heat balance method result in normal reboiler duty / latent heat of top tray liquid for your case?
  3. CMA010

    Fractionation column blocked discharge psv sizing case

    Difficult to say without more details
  4. CMA010

    Criteria for use of PSV / TSV???

    The "relief Systems Handbook" of Parry gives criteria for thermal relief. Furthermore there are some articles that give guidance ("What you should know about liquid thermal expansion", HP November 2008, and "Decide whether to use thermal relief valves", CEP December 1993).
  5. CMA010

    Normal & Emergency Vent Query

    If you're doing a project for AstraZeneca you should use their standard as long as it is more stringent than applicable industry standards / design codes.
  6. CMA010

    Open or closed bonnet?

    Closed Bonnet.
  7. CMA010

    API 521 Vapor Discharge Capacity Equation

    From you question you seemed to have the concepts mixed up. I'm sure in the standard a statement is made (or was made) that the vapour relief required is equal to the total rate of heat absorption divided by the latent heat of vapourisation, or W = Q/dH.
  8. CMA010

    API 521 Vapor Discharge Capacity Equation

    Equation A-7 is for vessels which do not contain liquid while W = Q/dH is for vessels which do. The A-7 equation is still part of the latest version (2008).
  9. CMA010

    Equation to calculate the back pressure for a PSV discharged to atmosphere

    Using API STD 521 (§ 7.3.1.3.3) yields a built-up back pressure of ± 0.17 bar and 0.6 Mach at the outlet.
  10. CMA010

    Which SRV capacity should be used for piping calculation?

    Note that according ISO 4126 the actual capacity should be used.
  11. CMA010

    Max vacuum allowable for tank & PV-vent

    Design code usually specifies the maximum allowable pressure and vacuum, at least the European standards do (EN 14015 or the old BS 2654)
  12. CMA010

    Flare capacity problem

    Instrumented Protective Function
  13. CMA010

    Flare capacity problem

    Flare reducing IPF's?
  14. CMA010

    Resistance to Flow Method for Rupture Disks in Two-Phase Flow Service

    No you can't use the method for vapour flow for a two-phase flow. However, you can try to use the method for two-phase flow given in API 521, § 7.3.1.3.5
  15. CMA010

    Managing Relief Valve Calibrations

    Normally you do not have to change the P&ID's as the P&ID's only state the functional tag number and not the equipment specific numbers. If you swap the PRV's the numbers on the P&ID's do not change but in your maintenance system (e.g. SAP) the functional location and history is updated.
  16. CMA010

    ASME Area vs API Area

    Using the API area and the API Kd (from API standard 520) should give approximately the same capacity as the ASME area and the ASME certified K. Which assumed K did you use?
  17. CMA010

    API 2000 - Inbreathing flow: which one?

    For new tanks 4.3.2.3.3 should always be used. For existing tanks (designed and installed before the Sixth edition was effective) the annex or 4.3.2.3.3 can be used. Protego can provide more background as they were involved in the sixth edition.
  18. CMA010

    DIERS applicability for two phase flow

    What pressures and fluids are you talking about? It looks like you have a supercritical relief (reported as two phase by simulators?)

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