Chemical Engineering Industrial Academy
Chemical Engineering Industrial Academy
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The Design of Stiffening Rings | External Pressure Vessel l Introduction | Part-1
In this video chemical engineering industrial academy will explain
STIFFENERS RING DESIGN ANALYSIS
In the design of stiffening rings, there is no direct procedure or formula to size or design the rings. Instead, the specific size and type of ring are first specified, and then they are analyzed for their moment of inertia and resistance against lateral buckling. If these parameters satisfy the design criteria, the rings' design is then optimized and finalized.
Why there is the need of Stiffening Rings?
If the actual external pressure exceeds the maximum pressure, the vessel can withstand, then the options for reinforcement, include increasing the vessel's thickness, increasing the shell thickness, solely to meet external pressure requirements, may not always be cost-effective or 2nd option is altering its geometry. Geometry of the vessels means the length to diameter ratio and shape of the vessel.
And also, vessel's diameter and length cannot be changed easily, once designed, due to couple of reasons, the obvious reasons may be,
• The designed capacity,
• Position and orientation in plant layout,
• Constraints in instrumentations and operations,
• Cost effectiveness,
• Integration with other equipment, and
• Local machining and fabrication facility constraints for a typical vessel,
and also couple of other reasons may be.
So, what is the solution?
One practical solution is there, that the distance between lines of supports can be changed, or adjusted. This is an alternative solution for strengthening the vessel against external pressure, to utilize external or internal stiffening rings or a combination of them.
But how this works?
Notice here that, reducing the distance between support lines, by adding stiffening ring, enhances the stability of the vessel's shell, the effect is similar to a shorter simply supported beam, that can withstand greater external loads, it is exactly what the stiffening ring do with external pressure vessel.
The required thickness of a shell with a given diameter, under a specified external pressure, can normally be reduced by shortening the shell’s effective length in between the support lines. The length can be reduced by providing stiffening rings at various intervals.
Added Advantages:
Adding Stiffening Rings, also provides an excellent solution, in some stages of design fabrication and operations
 The first one is, due to miss calculation in designing the thickness prior to fabrication,
 In second scenario, it may possible that some changes have been made in process condition, later on, of previously installed vessel,
 The third possibility is that a newly designed vessel has been started, and it has been reached up to such stage of fabrication, that you can do nothing with vessel length, and diameter.
These issues can be solved simply by adding stiffening rings
Let us start the design procedure,
So, where to start?
Let us first take some overview of, some of the main steps, for the design of stiffening rings, and then we will deep dive in one of each step.
I. In first step Select or suggest the type of stiffening ring and determine its cross-sectional area As, so what is the criteria for the selection of stiffening rings, there are different
type of stiffening rings try to choose any standard stiffening rings available in your local market, but standard stiffening rings creates problems in circular bending and fabrication, then the other way is, to choose a flat plate that can be easily bended and welded to the shell even in small several pieces and then take more flat plat and make angle, c channel, or whatever you suited, and in this way bending and fabrication become much easier whatever you suit but each of the them will have different cross-sectional area.
The calculation of cross-sectional area of ring (As) area we will illustrate later on
Now in the 2nd step
II. Assume the required number of rings and distribute them equally between
1-Head lines at 1/3h of its depth of head h
2-Jacketed section,
3-Cone-to-shell junction
And determine dimension, Ls,
We will see all these cases one by one respectively, so, first in case of cylindrical vessel, we are assuming that four stiffening rings of T-bar type have been, Suggested, and installed, between headlines at 1/3h of depth of head, as they are acting as a line of supports, and shortening the simply supported beam. For the sake of better understanding, it is necessary to discuss the concept of Support lines.
Mechanical Design of External Pressure Vessel | Vacuum Vessel | Finding Factors A and B Using Graphs
th-cam.com/video/vcKdfRrcoAQ/w-d-xo.html
Design of External Pressure Vessel | Vacuum Vessel | Shell Length and Thickness Calculation
th-cam.com/video/0J6ci3IxUkc/w-d-xo.html
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ความคิดเห็น

  • @SanjayYadav-fy4dg
    @SanjayYadav-fy4dg 12 วันที่ผ่านมา

    I have a similar kind of problem. I have a tank with volume of 5 m3 (Dia.= 1.65 m, SH=2.4m) with Limpet coil ( half pipe) outside the tank shell . the is filled with a GMS fatty acids @ viscosity of 40 cp. I ahve to cool the liquid from 100 to 70 degC through cooling water is which is flowing into the coil @ 32 degC Intel temp and 38 degC outlet temp. Questions 1:- What will be the required cooling water flow . Question:2 If the liquid needs heat from 50 to 70 degc through steam flowing into coil @ 100 deg C then what will be required steam flow.

  • @pritamkalita3415
    @pritamkalita3415 หลายเดือนก่อน

    Sir I have a doubt. In a reaction vessel i calculated Pa and I got very less than given Pa . Now I have to change the effective length. How to select the next effective length?

  • @SacchanK
    @SacchanK 2 หลายเดือนก่อน

    Why did the design length change from 1.86 m at 4:10 to 1.78 at 5:55?

  • @아따마-t2k
    @아따마-t2k 4 หลายเดือนก่อน

    Thanks for the good information. Is there any formula to equations outside film coefficients based on Conventional Jacket type???

  • @kirankittu7612
    @kirankittu7612 10 หลายเดือนก่อน

    Hello, could you please keep the link for the chart B, OR where exactly did you got the chart B. I tried in ASME SECTION -2 PART-D, but their the chart is different for (Chart for Determining shell thickness of components under External pressure developed for Austenitic steel, Type 304)...could you plz sort it out.....TQ

  • @kirankittu7612
    @kirankittu7612 ปีที่แล้ว

    Hii, how to find the design pressure for a vacuum chamber. In our case its 10^-2 milli bar

  • @yugzed2233
    @yugzed2233 ปีที่แล้ว

    Hello sir. Can you unhide the fourth video? The derivation of the equation? Or better yet, can you provide me the reference for the book? Thank you :)

    • @chemeng-industrialacademy
      @chemeng-industrialacademy ปีที่แล้ว

      Fourth Video means? please clarify the title of the video and the equation you are asking.

  • @contatophbio9080
    @contatophbio9080 ปีที่แล้ว

    O som e a imagem são péssimos, mas o conteúdo é muito bom, então vai ganhar joinha!

  • @JE-ed6te
    @JE-ed6te ปีที่แล้ว

    Titan Sub failure brought me here…

    • @darethrylls9747
      @darethrylls9747 ปีที่แล้ว

      Same. Kinda sent me down the rabbit hole of Submarine Hulls

    • @chemeng-industrialacademy
      @chemeng-industrialacademy ปีที่แล้ว

      It is exactly, where you should be. It seems that Titan was not designed to withstand such tremendous external pressure, approximately 406 bar at a depth of 13,000 ft.

    • @chemeng-industrialacademy
      @chemeng-industrialacademy ปีที่แล้ว

      @chemeng-industrialacademy 1 second ago It is exactly, where you should be. It seems that Titan was not designed to withstand such tremendous external pressure, approximately 406 bar at a depth of 13,000 ft.

  • @deadsoul391
    @deadsoul391 ปีที่แล้ว

    Thank you for sharing such detailed explanation. However one question , which figure no or chart is used to determine factor B for material SS and temperature 300F?

  • @nayeemrahiman3230
    @nayeemrahiman3230 ปีที่แล้ว

    Hello, I need to design a vessel which has internal vacuum and external pressure, is it possible to design with ASME standard. Kindly help me. My application is for high vacuum with external cooling coil and pressure

    • @chemeng-industrialacademy
      @chemeng-industrialacademy ปีที่แล้ว

      yes, you can design with above stated ASME Standards. Suppose your maximum jacket pressure is 3 bar and inside shell is with prefect vacuum that is equal to -1 bar the total external pressure would be 4 bar as there is inside pressure and all the pressure is external one, and you have to design an external pressure vessel with 4 bar external design pressure or even slightly increased to consider other safety factors and margins.

  • @gurudattrajendrapatil3319
    @gurudattrajendrapatil3319 2 ปีที่แล้ว

    provide Excel Cal Sheet if you did it

  • @skeller823
    @skeller823 2 ปีที่แล้ว

    Very helpful and comprehensive! By the way at 6:11 in video A is not from ASME Section 11 it is ASME Section 2 or II "Materials Part D"

  • @siddharthshah4929
    @siddharthshah4929 2 ปีที่แล้ว

    Thank you so much for sharing the knowledge. I appreciate your efforts. I have 1 doubt that, how you calculated design pressure P which is 15 bar. And what will be the value of P when my vacuum chamber is under 2 mbar inside pressure

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 2 ปีที่แล้ว

      I think, it would be 15 psi, not 15 bar, that's very high external pressure, and as concern to you vessel's vacuum pressure, if vessel is exposed to atmospheric pressure that's almost 15psi then your external pressure of vessel would be 15psi minus your internal pressure of vessel that's 2mbar =0.03psi that would be 14.97 psi external pressure, or in brief you can choose your external pressure 15 psi for this vessel and perform calculation using your shell thickness, for allowable pressure, and then compare with design external pressure .

  • @h7opolo
    @h7opolo 2 ปีที่แล้ว

    what is the formula for pressure of liquid at the bottom of a helical pipe?

  • @gustinnuraniputri6059
    @gustinnuraniputri6059 2 ปีที่แล้ว

    What friction factor do you use in this formula? fanning or moody?

  • @haithamalmalki8178
    @haithamalmalki8178 2 ปีที่แล้ว

    thanks a lot about this video

  • @naufalhadi8684
    @naufalhadi8684 2 ปีที่แล้ว

    Verry helpfull video. Recently I develop calculation of heat transfer on agitated, jacketed, and insulated tank. Could you please provide refference on this nusselts number calculation. Thankyou

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 2 ปีที่แล้ว

      Browse these 1-Handbook of industrial mixing , science and practice 2-Ludwig' s applied process design for chemical and petrochemical plants( 4th edition volume 3) 3-Advances in industrial mixing

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 2 ปีที่แล้ว

      see the part 2 of video

  • @thomasapgoodwin5768
    @thomasapgoodwin5768 3 ปีที่แล้ว

    This 100% does not work. in way at all

  • @harryfikri2083
    @harryfikri2083 3 ปีที่แล้ว

    thank you

  • @yeyeneinfeche9376
    @yeyeneinfeche9376 3 ปีที่แล้ว

    Thank you for the video, this is very helpful when I need an instrument for piping

  • @pandianshanthakumar4163
    @pandianshanthakumar4163 3 ปีที่แล้ว

    Very interesting and collective information about the pressure drop in the Helical & the Curved pipe lines. I like it very much and thanks a lot to the and the team.

  • @alankaranand2904
    @alankaranand2904 3 ปีที่แล้ว

    thank you for video sir. I am from India

  • @rakshitkajala1667
    @rakshitkajala1667 4 ปีที่แล้ว

    why does the axial velocity profile become skewed in helical flow, i.e. why does the maximum velocity countor goes towards outer edge of the pipe and not towards the inner edge?

  • @salmabachar812
    @salmabachar812 4 ปีที่แล้ว

    Hello, I have a question how can i calculate heating time in shell and tube exchanger . Thank You

  • @punkisinthedetails1470
    @punkisinthedetails1470 4 ปีที่แล้ว

    impeller vs turbine what is the difference

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 4 ปีที่แล้ว

      Impeller and turbine work opposite to each other, impeller transfer its energy to the fluid and tubine take energy from the fluid.

    • @Peter-bg1ku
      @Peter-bg1ku ปีที่แล้ว

      @@chemeng-industrialacademy perfect explanation.

  • @zainamohsinkhan1733
    @zainamohsinkhan1733 4 ปีที่แล้ว

    Could you please tell me the heat and mass tranafer through the helicall coiled tube .

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 4 ปีที่แล้ว

      Heat transfer in helical coil has been discussed in detail. You can go to the school of heat transfer in channel playlist and almost each and every detail has been given regarding to inside, outside heat transfer and overall heat transfer coefficient for helical coil, from overall heat transfer coefficient you can calculate net heat transfer to or from the coil, However as concern to mass transfer, mass is not transported through helical coil

  • @aldrinobliosca3335
    @aldrinobliosca3335 4 ปีที่แล้ว

    Thank you sir

  • @aldrinobliosca3335
    @aldrinobliosca3335 4 ปีที่แล้ว

    Hi sir, can you explain about the force of a liquid in a straight pipe and a liquid in a coil pipe at a 10 meters high. How gravity help in this situation?

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 4 ปีที่แล้ว

      The most prominent force exerted by the fluid on wall of pipes are pressure force act normaly to the wall of pipes. forces exerted by the fluid on the wall of a pipe generaly are considered in term of stress not force in pipes whether it is straight, bended or something else.These all stresses are calculated and considered . For example we have to calculate the stress by fluid on pipe to find out the thickness of pipe wall and also for pipe supports. So we consider stress (force per unit aera) which is more useful than alone force.other forces are frictional forces between fluid and wall of pipe between fluid layers itself, these are considered in pressure drop calculation in pipes, and more we will explain all this in a video soon.

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 4 ปีที่แล้ว

      As cocern to your second question gravity effect is understood and has a effect on fluid in pipes ,coils and are considred in pressure drop equation and berrnoull equation

  • @adnanzakki1528
    @adnanzakki1528 4 ปีที่แล้ว

    KAZTRO FAN LOVE YOU

  • @adnanzakki1528
    @adnanzakki1528 4 ปีที่แล้ว

    SUPERCHAT👍🥰🥰🥰

  • @joshgaerke7159
    @joshgaerke7159 4 ปีที่แล้ว

    Any chance that excel spreadsheet became available somewhere? I have some neat test I'd like to try for some flows through a geo-thermal coil set up.

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 4 ปีที่แล้ว

      Excel spread sheet will be available in 1 -2 days.

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 4 ปีที่แล้ว

      I will provide link in 1 to 2 days.

    • @joshgaerke7159
      @joshgaerke7159 4 ปีที่แล้ว

      @@chemeng-industrialacademy Is the link posted somewhere? I haven't seen it. Just checking in.

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 4 ปีที่แล้ว

      Dear Friends link has been provided above in the video description.

    • @joshgaerke7159
      @joshgaerke7159 4 ปีที่แล้ว

      @@chemeng-industrialacademy Thanks so much!

  • @NationFirst1627
    @NationFirst1627 5 ปีที่แล้ว

    I want your help ragarding this topic.. can i get your whats app number?

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 5 ปีที่แล้ว

      Please describe your problem briefly then i will see what type of help you needed

    • @NationFirst1627
      @NationFirst1627 5 ปีที่แล้ว

      Currently I'm working on a project on heat transfer coefficient in an agitated vessel using baffle plate of various liquid solutions... So i need your help

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 5 ปีที่แล้ว

      you want to calculate heat transfer coefficient ?

    • @NationFirst1627
      @NationFirst1627 5 ปีที่แล้ว

      @@chemeng-industrialacademy yes

    • @NationFirst1627
      @NationFirst1627 5 ปีที่แล้ว

      Can i get your number so we can communicate further quite fast?

  • @saraboom6613
    @saraboom6613 5 ปีที่แล้ว

    In cadworx, if we xref equipment to the piping module,by using nozzle generic, gasket & bolt generate automatically. But, In autocad plant 3d, by using "PLANTINSERTAUTODESKCONNECTIONPOINT" we can mention the point of connection, then how to generate gasket and bolts automatically.

  • @swapnilpawar4103
    @swapnilpawar4103 5 ปีที่แล้ว

    Can i get that excell sheet

  • @ElPsyKongroo
    @ElPsyKongroo 5 ปีที่แล้ว

    Good

  • @munazahmalick8154
    @munazahmalick8154 5 ปีที่แล้ว

    Good

  • @munazahmalick8154
    @munazahmalick8154 6 ปีที่แล้ว

    Good

  • @jeffstone2601
    @jeffstone2601 6 ปีที่แล้ว

    As an accessory is added, either valve or flanges to a secondary route? if you can perform this action. Thank you

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 6 ปีที่แล้ว

      i will respond you in a few days.Thanks

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 6 ปีที่แล้ว

      Hi Jeff Stone i have uploaded a video in response to your question. Please feel free to ask me again if you not satisfied with the stuff th-cam.com/video/NRcFRZIVFdo/w-d-xo.html

  • @munazahmalick8154
    @munazahmalick8154 6 ปีที่แล้ว

    Way more better thn previous, keep it up, good luck

  • @munazahmalick8154
    @munazahmalick8154 6 ปีที่แล้ว

    First one

  • @parikshitshahane6799
    @parikshitshahane6799 6 ปีที่แล้ว

    what is the name of the book you are refering?

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 6 ปีที่แล้ว

      Please you should see the references at end of video , however i repeating again for your help. Following are the four books i referred 1-Handbook of industrial mixing , science and practice 2-Ludwig' s applied process design for chemical and petrochemical plants( 4th edition volume 3) 3-Advances in industrial mixing 4-Heat transfer design methods by John J.M

  • @krupachanrockz
    @krupachanrockz 6 ปีที่แล้ว

    can you please suggest any references for in depth knowledge of fluid flow in helical channels

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 6 ปีที่แล้ว

      Paul, E.D (Ed.) , Handbook of Industrial Mixing Science and Practice. Hoboken, New Jersey: John Wiley & Sons, Inc., Publication. Coker, A.K , Ludwig’s Applied Process Design for Chemical and Petrochemical Plants(4th eds. , vol.3 , PP. 444-451). Amsterdam: Gulf Professional Publishing. Kresta , S.M , Advances in industrial mixing : A Companion To the handbook of Industrial Mixing(pp. 512-515). , Hoboken, New Jersey: John Wiley & Sons, Publishers. John, J.M , Heat Transfer Design Methods (pp.376-384). Consult these reference books my dear , I will try more for you in some free moments.

  • @SvilenBaev
    @SvilenBaev 6 ปีที่แล้ว

    Wow what a interesting channel -I'm a chemist and work for a pharmaceutical company! You tube needs a channel like yours! I liked and subbed here to support you, please support me back 😊

  • @munazahmalick8154
    @munazahmalick8154 6 ปีที่แล้ว

    Good effort, keep it up

  • @AJ4d
    @AJ4d 6 ปีที่แล้ว

    Do you have any good sources I can refer to?

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 6 ปีที่แล้ว

      Hi A.J Ford good to see you unfortunately "References" is missed in CEI-Academy tutorials due to editor mistake , however we are updating all the stuff very soon. Here providing the desired stuff for your help. Cheremisinoff, Nicholas P. ( Ed.), Multiphase reactor and polymerization system hydrodynamics (PP.390-397). Houston, London, Paris, Zurich, Tokyo: Gulf Publishing Company. Schlichting H. (1979). Boundary-Layer Theory (7th ed., p.627). New York, USA: McGraw-Hill book Company. Moss, D. Pressure vessel design manual (3rd ed., pp.340-350), Amsterdam: Gulf Professional Publishing. Rennels, Donald C. & ‎Hudson, H.M. Pipe flow: A practical and comprehensive guide.( pp 166 -168), Wiley Publishers. Ali, s. (2001).Pressure drop correlations for flow through regular helical coil tubes. Fluid Dynamics Research 28 (2001) 295-310. KRISHNA B.S.V.S.R. Prediction of pressure drops in helical coil with single phase flow of non-newtonian fluid.

  • @mohammedali2013
    @mohammedali2013 6 ปีที่แล้ว

    Can i get your email and phone number please

  • @enammsuchiang418
    @enammsuchiang418 6 ปีที่แล้ว

    what is the name of the software use

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 6 ปีที่แล้ว

      Autodesk Inventor Professional 2018

    • @enammsuchiang418
      @enammsuchiang418 6 ปีที่แล้ว

      Is it free for window

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 6 ปีที่แล้ว

      you have three options 1.Go to autodesk website make an account and get free software as a student for 3 years 2.Get full cracked version from various link on internet free of cost for liftime 3.Get paid licensed software as given on the web

    • @enammsuchiang418
      @enammsuchiang418 6 ปีที่แล้ว

      thank you for the info.

    • @chemeng-industrialacademy
      @chemeng-industrialacademy 6 ปีที่แล้ว

      Thanks