Continue to Site

Eng-Tips is the largest engineering community on the Internet

Intelligent Work Forums for Engineering Professionals

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

Search results for query: *

  1. SyedZainAli

    PV elite Effective force bearing width calculations

    Dear Engineers, For lug types with a bottom plate and no continuous rings (Simple geometry with no gussets and gusseted geometry with top plate in Lug Type), enter the distance between gussets plus two times the gusset plate thickness. For lug types with continuous top and bottom rings...
  2. SyedZainAli

    Floating tubesheet thickness

    hello guys, as per UHX14.2, the two tubesheets ( fixed and floating) shall have the same thickness and material. however in my case the design temperatures at stationery side is different (i.e. 500 deg. C) from what i am having at floating end (288 deg. C) and the tube length is 18000 mm from...
  3. SyedZainAli

    RT of the nozzle below NPS 6 size

    Is it possible to perform RT for the steam pipes size NPS 2 that are drawn from header in a fired boiler deisgned on Section 1
  4. SyedZainAli

    How to calculate the pump surge pressure?

    Dear All, I am right now looking for some pumps attached in parallel to a header I want to calculate the surge in startup of pump to cater the hammering in the header
  5. SyedZainAli

    Ligament hole in a header comes on circumfrential headers

    Dear All, I am right now working on design and detail engineering of a header having tube ligaments on its already UG-53 has been used what if one of my ligament hole comes on a circumferential/longitudinal seam (All of the seams are 100 % radiographed) What will be the code requirement that...
  6. SyedZainAli

    Simultanious calculations for TEMA and UHX for tubesheet in PV Elite

    hello guys, I want to know is there any method to perform the calculations as per TEMA and UHX for tubesheet in PV-Elite as this we can do in COMPRESS. With Best Regards Zain
  7. SyedZainAli

    Air cooled Heat Exchagers

    Can any one share sample mechanical design calculations for Air cooled Heat Exchanger for gaining knowledge in this field
  8. SyedZainAli

    AWS A 2.4

    Dear Members, Good day, I want to ask that where it has been mentioned in ASME BPVC codes to follow AWS A 2.4 for the welding symbols on drawing for any stamped vessel Best Regards Zain
  9. SyedZainAli

    Stress concentration factors while calculating WRC-297 in PV-Elite

    Dear All, I want to ask as While calculating WRC-297 calculations on PV Elite, Pv- Elite considers 2 Stress concentration factors mainly 1) Shell Stress Concentration factors (default value 1.2) and 2) Nozzle Stress Concentration factor ( default value 2.25) my question is that what values...
  10. SyedZainAli

    Percentage fiber elongation in Div 2 as per table 6.1 A

    Guys, How are you all, I was yesterday designing a vessel having a transition cone, and while I was checking the calculation I came to know that compress takes the value of t in the fiber elongation calculations for cones and transition other than nominal thickness considered i am attaching the...
  11. SyedZainAli

    UHX 14.5.9 Step (9)

    This is wrt ASME S8D1 edition 2013 para UHX-14.5.9(b) which deals with checking the tubes for buckling stress in case of a floating head heat exchanger. Can anybody explain the reasoning/logic behind this para which is relevant for floating head shell and tube heat exchangers? As this para is...
  12. SyedZainAli

    How can we design a flange used as Quick opening closure having slotted bolt holes

    Dear All I am working on a design project that comprises of a quick opening closure having slotted bolt holes and instead of having stud bolts it has Eye bolts eye side of the bolt is attached to the shell so that we can instantly open all bolts i am having trouble in designing such type of the...
  13. SyedZainAli

    TEMA A.23 TUBE LONGITUDINAL STRESS - PERIPHERY OF BUNDLE

    Dear All I am designing an S&T heat Exchanger of type BEM and i am having the Following Error on compress "TEMA A.23: Tube longitudinal compressive stress is excessive (Operating)." what are the possible ways to eradicate this error My Design conditions are Shell side: Design Pressure : 77...
  14. SyedZainAli

    TEMA A.23 TUBE LONGITUDINAL STRESS - PERIPHERY OF BUNDLE

    Dear All I am designing an S&T heat Exchanger of type BEM and i am having the Following Error on compress "TEMA A.23: Tube longitudinal compressive stress is excessive (Operating)." what are the possible ways to eradicate this error My Design conditions are Shell side: Design Pressure : 77...
  15. SyedZainAli

    Allowable Stress Values for Lifting Pressure Vessel through Lifting Lug

    Dear Tom Barsh As Mentioned in the Help topic In Compress "As well there is an option to reset all the allowable stress values based on the vessel material yield stress of the component to which the lift lug is attached. This is useful if the lug material is the same as the vessel component...
  16. SyedZainAli

    API 620 Storage tank Design Calculations

    Hello Everybody Can anyone share me the Sample Design Calculation For Designing Storage tanks according to API 620 Code I shall be very thankful to you Regards Zain
  17. SyedZainAli

    Weight value, W, used in equation tw = W/(2*pi*Rm*St*Ks*Ec)

    I want to ask the Question that when ever we design vertical vessel on compress having support lugs this error occurs "Weight value, W, used in equation tw = W/(2*pi*Rm*St*Ks*Ec) for cylinder and transition components does not include weight of liquid above top of vessel. kindly ellaborate the...
  18. SyedZainAli

    Weight value, W, used in equation tw = W/(2*pi*Rm*St*Ks*Ec) for cylind

    I want to ask the Question that when ever we design vertical vessel on compress having support lugs this error occurs "Weight value, W, used in equation tw = W/(2*pi*Rm*St*Ks*Ec) for cylinder and transition components does not include weight of liquid above top of vessel. kindly ellaborate the...

Part and Inventory Search