Continue to Site

Eng-Tips is the largest engineering community on the Internet

Intelligent Work Forums for Engineering Professionals

  • Congratulations waross on being selected by the Eng-Tips community for having the most helpful posts in the forums last week. Way to Go!

Recent content by starrproe

  1. starrproe

    External Pressure Calculations interpretation.

    rsaeed, You may please refer following message from PVElite regarding your query on addition of static head for extrenal design calculations.
  2. starrproe

    Circ. Stress at Horn of Saddle

    jte, It is turning out that I will also need to work on a vessel with 3 saddles in some time. Can you please share as to what approach did you use for anaylsing vessel on 3 saddles.Somebody from my office suggested using STAADPRO.Since I have no experience dealing with such vessels,can you...
  3. starrproe

    External Pressure Calculations interpretation.

    rsaeed, My views on your queries: Refer UG-32(a), UG-33(a) & UG-33(a)(1)(a). Probably PV-ELite is misunderstanding "plus heads" as adding liquid static head, which is incorrect.Code intends to denote concave sides of heads as "plus heads" and convex sides as "minus heads". Static head of...
  4. starrproe

    UCS 79 % extreme fibre elongation

    rsaeed, By default, PV-Elite assumes 1.3 times allowable stress at ambient temperarue as the allowable stress during hydrotest. This is the case with youur calculation as well.(Press F1 on your keyboard after selecting "Hydrotest is 90% yield." in Design Constraints header to see it yourself.)...
  5. starrproe

    UCS 79 % extreme fibre elongation

    rsaeed, Your ellipsoidal head dimensions are - ID = 3500mm Min. Thickness = 61.5mm Nominal thickness = 75mm Procedure for calculating fibre elongation is - Centreline diameter = 3500+2*(Min. Thickness/2) = 3500+2*61.5/2 = 3561.5mm Centreline radius...
  6. starrproe

    Reinforcement pad split in half

    vesselfab, Can you please share broad outlines of requirements for spliced RF pads? I dont have A09 of Code. Starrproe
  7. starrproe

    Estimating static pressure loss for air-cooled heat excahnger

    jone, Thanks for the text.. speco / srfish,, Thanks for your valuable suggestions. Starrproe
  8. starrproe

    Estimating static pressure loss for air-cooled heat excahnger

    Hi All, I am working on rerating some existing air-coolers for higher duty.Initial calculations suggest that by increasing the air-flow(using new fans), while retaining existing bundle, the required process parametres can be acheived. However, since I also need to check suitability of existing...
  9. starrproe

    Reinforcement for closely spaced openings

    My query is for an existing column where I need to introduce a new manway. The location for new manway is in vicinity to an existing 6" nozzle, such that limits of reinforcement of the two openings interact and it represents closely spaced openings per UG-42 of ASME-VIII-1. When I run the...
  10. starrproe

    Difference between SSC, SCC and HIC?

    Hi All, This question may sound a bit stupid to the experts here in this forum, but I just can't resist myself asking you guys as the issue has been bogging me for quite some time. What is the main difference between the corosion mechanisms - Stress Corosion Cracking(SCC), Sulfice stres...
  11. starrproe

    Nozzle reinforcement query - area available in shell

    I am adding a new 16" nozzle to an existing process column: 1. Column dimensions - 8840mm ID x 47000mm T/L to T/L 2. Design pressure and temperature - 3.5 Kg/cm^2(g), 367C 3. Shell and Nozzle neck MoC - SA 516-70 4. Provided shell course thickness - 27mm Required shell thickness due to int /...
  12. starrproe

    Non-pressure Welds to Section VIII Div I Vessel

    metengr, Can you please direct me to relevant section of Code (ASME-VIII-1) which says that PWHT will not be required for the attachment welds? Regards, Starrproe
  13. starrproe

    Nozzles on a blind flange

    jte, Thanks for your response... I am sorry if my statement has caused you some confusion, but actually I wanted to know whether I can have any size of reducing slip-on flange,especially with openings greater than those allowed per Columns 2,4 & 6 of Table F6 (e.g. NPS 24 x 16). Will such a...
  14. starrproe

    Nozzles on a blind flange

    jte, I have come across a case where I need to provide a 16" opening in blind flange of 24" manway.(I can't use a 24x16 concentric reducer due to process constraints.) I am planning to go for a 24x16 reducing type slip-on flange.Of course, the reducing outlet would need a hub as specified in...
  15. starrproe

    Using Manway as Nozzle

    We have a 24" manway with standard flanges per ANSI B16.5 in a 8840mm dia. process column.Our Process engineers want to do some modification, for which they need to use this manway as an inlet nozzle by cutting a 16" opening in the blind flange and connecting it with a 16" line. However, this...

Part and Inventory Search