<

Results 1 to 10 of 10

Thread: Design Pressure ( Full Liquid )

Hybrid View

Previous Post Previous Post   Next Post Next Post
  1. #1

    Join Date
    Nov 2009
    Location
    Kuala Lumpur
    Posts
    22
    You have to include static pressure of the liquid filling the entire vessel in installed position. Assume the PV is a vertical cylinder.

    Static pressure = [liquid column height]x[liquid density]x[gravity]
    "The client is always right - except when he is wrong"

  2. Design Pressure ( Full Liquid )

    Thank's for your reply
    1.That equation is suitable for Horizontal PV ??
    2, Pllease explain for that equation [liquid column height] ,??
    3.then Static pressure as base reference for PV design pressure ??




    Static pressure = [liquid column height]x[liquid density]x[gravity]


    Thank,s

  3.    Sponsored Links



    -

  4. #3

    Join Date
    Nov 2009
    Location
    Kuala Lumpur
    Posts
    22
    What I meant was, without looking at any dwgs, I assumed your PV was a vertical cylinder.

    The same equation applies for any container carrying liquid.

    Liquid column height is the height of the liquid medium contained in the PV. For the sake of putting numbers, say:
    Topmost point of vessel : 2.000m
    Lowest point of vessel : 1.000m
    Liquid column height = 2.000m - 1.000m = 1.000m

    Apply equation (assume gravity = 9.81N/kg);
    Static pressure = [1.000m]x[1000kg/m3]x[9.81N/kg] = 9.81e3 N/m2 or Pa(g)
    Finally equal to 9.81kPa(g) or 0.0981Bar(g)

    This is as much as I can advise without looking at any dwgs or diagrams
    "The client is always right - except when he is wrong"

  5. #4
    Strictly speaking, this is not pressure vessel as the pressure is so so low. As long as the wall of vessel can meet the structure requirement, the vessel will work. As the pressure so low, you do not have to follow ASME BPV Code.

  6. #5

    Join Date
    Nov 2009
    Location
    Kuala Lumpur
    Posts
    22
    Quote Originally Posted by chunlin View Post
    Strictly speaking, this is not pressure vessel as the pressure is so so low. As long as the wall of vessel can meet the structure requirement, the vessel will work. As the pressure so low, you do not have to follow ASME BPV Code.
    I agree. Perhaps the owner specified that way for certain reasons, i.e. size of the vessel, etc. Anyway, good luck adiarahman08.
    "The client is always right - except when he is wrong"

  7.    Spons.


  8. #6
    or you can find in PV Handbook by Megyesy.. that Static head = 0.433 psi x Head (in feet).. example that if your vertical vessel is about 10 feet. than 0.433 x 10 feet = 4.33 psi.

  9. hai
    tha tank height is 15m
    Tank dia is 15m
    design specifgravity is 1.114
    design pressure is full liquid + 0.015bar

    how to calculate the design pressure in kpa

    please

  10. #8

    Join Date
    May 2009
    Location
    Jubail Saudi Arabia
    Posts
    193
    Quote Originally Posted by robertantoreni View Post
    hai
    tha tank height is 15m
    Tank dia is 15m
    design specifgravity is 1.114
    design pressure is full liquid + 0.015bar

    how to calculate the design pressure in kpa

    please
    oh! my god.. are you an engineer?....really?

Similar Threads

  1. Replies: 36
    Last Post: 02-19-2019, 03:13 AM
  2. Flowing Tubing Pressure in Liquid Loaded Natural Gas Wells
    By Davu in forum Oil And Gas Production
    Replies: 1
    Last Post: 09-04-2013, 09:05 PM
  3. how can i reduce pressure in a liquid ?
    By dhnsekaran in forum Oil And Gas Process
    Replies: 4
    Last Post: 07-23-2010, 07:46 PM
  4. Article: how can i reduce pressure in a liquid ?
    By dhnsekaran in forum Home Articles
    Replies: 0
    Last Post: 07-08-2010, 05:49 PM

Tags for this Thread

Bookmarks

Posting Permissions

  • You may not post new threads
  • You may not post replies
  • You may not post attachments
  • You may not edit your posts
  •  
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40