Monday, November 9, 2009

Hi Friends:Need Advice on piping materials

To my understanding of 31.8, the distrbution and the processing units part of hte distr. shall all be in acc. with 31.8
You may not use 31.3. The thk calc. are fundamentally different though it is going to be within the processing unit.
If you deem the code 31.3 and 31.8 together will suit the reqt. You can get the clients approval in first place.
It is quit similar to the way of B31.3/31.1/IBR all going together as need based.
 
On the material aspect the code does not restrict the use A672 or API 5L. The general diff of C60 and C70 is that
it is made from A516 killed fine grain material. C70 is a higher tensile strength material than C60 so the chem comp. is
diff. Pl. loook into the ASTM for more info. 
 
Regards,
Kannan


From: Raghuram <r.bathula@ticb.com>
To: piping_valves@yahoogroups.com
Sent: Tue, November 3, 2009 1:08:49 PM
Subject: [piping_valves] Re: Hi Friends:Need Advice on piping materials

 

you can use API 5L X65, basic allowable stresses are given in Table A-1

--- In piping_valves@ yahoogroups. com, "satish hingalkar" <satish_hingalkar@ ...> wrote:
>
> Hi all friends,
>
> We are doing Nitrogen distribution project in middle east,Project brief:Project is basically 48" N2 High pressure (600#) Pipeline and distribution to process units.
>
> 48" Pipeline of materail API 5L X65 with metering and filtering skid is comming to the battery limit of process unit,My query is that can we use same material (API 5L X65) by doing thickness calculation as per ASME B31.3 inside the process unit.Pl.advice me the requirement inside the process units or we have to use only ASTM Pipe A672 C60/70 cl.22.Also let me know the difference between the two materials.
>
> Responce will be appreciated.
>
> Thanks in advance.
>
> Regards,
> Satish Hingalkar
>

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    Thursday, September 24, 2009

    Fwd: Re: Double offset butterfly valve with metal seat

    Pl. read catalogs for more understanding.

    The subject of seating in double ot triple offset butterfly is litte bigger than other valves due to the emphasis given to the application and operating conditions.

    There are quit a few proprietary seat designs. For eg. the graphite layers gets eroded in few weeks to months due to operating condition resulting in big leak and pressure drops. The profile of the seat and disc is also important which developes the cavitation effect and pitting of the seat. So in the selection of a seat the operating condition such as the opening angle, pressure, which in turn will affect the operating pressure in turn the system design itself. So a well thought process is essential in the butterfly valve type and seat selection.

    In solid seat the cost makes the big difference.

    Regards,
    Kannan

    --- In piping_valves@yahoogroups.com, "ashoksiva1982" <ashoksiva1982@> wrote:
    >
    > Dear all,
    >
    > I have an enquiry for Double offset butterfly with metal seat. The design pressure shall be 40 bar. Can any one know the seating arrangement of competitor valves.
    >
    > I got some information from the below link. I need some more arrangement for the above requirements.
    >
    > http://www.sz-yll.cn/upload/814/200631485558638680174.pdf

    Wednesday, September 23, 2009

    UL LISTED/FM APPROVED Valves fro fire water network(Sea Water) Options

    There are quit a no. of vendors with FM/UL in the market.
     
    However I would suggest Mapag GmbH, having UL certification for a wider size range and for all kind of standard designs.
    Even Tyco has only upto 12" with UL.
     
    Regards
    Kannan
     
     
    Respected Sirs,
    In our project, we have fire water network(sea water used as fire water).
    As per requirements, all valves shall be UL LISTED/FM APPROVED.
    we have valves sizes ranges from 2" to 30"- we require almost more than 2500 valves.
     
    May i have list of vendors from USA,UK or EUROPE who can  supply these valves.
    Your esteeem reply ill be highly appreciated.
     
    from
    Ashok

    Welding qualification of very low sulfur steels.

    ----- Forwarded Message ----
    From: kannan_cit <kannan_cit@yahoo.com>
    To: piping_valves@yahoogroups.com
    Sent: Wednesday, September 23, 2009 7:26:46 PM
    Subject: [piping_valves] Welding qualification of very low sulfur steels.

     

    Quit some time ago, I was having great difficulty in finding mills manufacturing steels with sulfur limited to 0.001% max. due to a wrong prescription by one of the well known PMC. Though it was resolved with higher relaxation later, I started to look into the issues concerning the restrictions posed in the sulfur content in steels, which were mainly added to increase the machinabilty, in various applications including the H2S/Sour service applications. The article in the link provides an insight in welding a low sulfur material.

    The issue in the context of welding is that, while sulfur content is reduced the surface tension is reduced resulting in wider concave welds with lesser penetration, which pose a problem in thick walled pipes which are common in sour services. The insert ring solution proposed in the link below may solve the problem of higher weld penetration, which calls for different weld procedure. Similar to ASME BPE standard's prescription of limitation on, weld sulfur with appropriate quality check, does such requirement called in the BPV.

    I seek our member's suggestion on the subject of welding procedure qualification, in such applications where sulfur content is restricted from 0.002% to 0.010% in sour/H2S applications.

    http://www.thefabri cator.com/ tubepipefabricat ion/tubepipefabr ication_article. cfm?ID=533

    With regards,
    Kannan

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    Monday, June 22, 2009

    Hydrogen Embrittlement on metals.

    Though the subject is quit huge to discuss, I would like add few morepoints though not all.

    1) The purity level of the Hydrogen is also categorised as less than 99% ormore than 99%.
    2) The pressure is one important element(hardly addressed during designphase by material engineers), for less than 99% purity which means amixture, the partial pressure should be >1bar for the hydrogen to have itsshow.
    3) Limits are present for Carbon monoxide and Oxygen and other elements aswell, which induces the phenomenon described by you(Owen).
    4) Whether the system is under cyclic condition or not which applies to PSA and likes.
    5) Materials are defined by their yield and tensile strengths limitations.Take note the equipment material prescription varies differently frompiping material for the same conditions.
    6) Not the least though, Hydrogen embrittlement should not be equated withHydrogen induced cracking.

    Coming to the point of temperature, linked to materials, considering carbonsteel as the material of constr., for eg. A well known refinerylicensor prescribes the temp. limitation at 260 deg.C, A German company holding numerous technologies in the subject of Hydrogen limits the use of Carbon steel to 200 deg.C, A UK Engg. company having H2 licenses, limits it to 240 deg.C. As I had seen lab test reports andfound H2 effects above 200 deg.C, such variation of 200 to 260 is quit abig gap under standard test procedures.

    Let me know the thoughts of our groups on the temperature factor, what could be the reasoning behind such broader limits.

    Some useful links for members interested further study.
    http://www.uni-saarland.de/fak8/wwm/research/phd_barnoush/hydrogen.pdf
    Some site generalises the subject which cannot be put into practice or inyour engg. Take caution, in your understanding of the subject.
    http://octane.nmt.edu/waterquality/corrosion/hdamage.htm
    http://www.corrosionist.com/Corrosion_Control_Offshore_Oil_Gas.htm
    http://hrc.nevada.edu/qa/SIP/SIP-UNR-018R0D0.pdfhttp://www.hydrogen.energy.gov/pdfs/progress05/v_a_4_adams.pdf

    With regards,
    Kannan Sundaram

    "Owen Jenkins" <owen@osjl.co.uk> Sent by: Tomaterials-welding@googleg <materials-welding@googlegroups.com>roups.com cc
    Subject21/04/2009 20:49 [MW:2002]
    Re: effect of H on notch strengthPlease respond to materials-welding@googleg roups.com

    Ali,The name is Owen, not oven. An oven is something in which you heat food, oroccasionally heat-treat metals!

    For hydrogen embrittlement to occur, you must have monatomic hydrogendiffusing through the metal and gathering in grain boundaries. Monatoms ofhydrogen are small enough to diffuse through grains of steel. Theembrittlement occurs as a result of monatomic hydrogen atoms diffusing intothe grain boundaries, reacting to form molecules of hydrogen gas, whichthen force the grains apart. Diffusion and reaction rates both slow withdecreasing temperature, hence the effect of hydrogen embrittlementdecreases below a certain temperature. The effect of the ductile-brittletransition then becomes more important with decreasing temperature. It isalso worth remembering that, at constant pressure, the volume of a givenmass of hydrogen will decrease with temperature, or, at constant volume,the pressure will decrease with decreasing temperature, hence the drivingforce pushing the grains apart will be reduced. If it is too cold for thehydrogen atoms to diffuse through the steel, HE can't occur.

    The monatomic hydrogen is commonly formed as a result of acid/metalcorrosion reactions (e.g. pickling steel prior to painting) or otherreactions in which hydrogen is liberated as a cathodic reaction (e.g.fusion welding where water is present or there are hydrogen compounds inthe flux). The hydroxonium (or hydrogen) ions are reduced to monatomichydrogen by electrons from the dissolving (corroding) metal or the weldingcurrent flow. The monatomic gas can diffuse through metal grains - thediatomic gas molecules can't.

    2H+ + e- ® 2H.2H. ® H2

    Some steels are much more prone to hydrogen embrittlement than others. HSLAand high strength carbon steels tend to be more problematic than others.Hydrogen embrittlement can be prevented by suitable heating to anappropriate temperature after the process which generated the hydrogen (oneof the functions of post-weld heat treatment), to allow the hydrogen todiffuse out of the steel. If you have a properly qualified weld procedure,the PWHT should be designed to mitigate the effects of hydrogenembrittlement.

    When HE is suspected in cases of failure, there is never any sign of thehydrogen - it has all long gone, so it is usually inferred from thecircumstances and the nature of the cracks.

    Regards,
    Owen

    Thursday, May 14, 2009

    New in Piping field

    Welcome Sanjay.

    I do not know of any ebook as such to cover the big subject of piping. However you should start with OP Nair's Piping Handbook. And you can also have a read of the B31.3 lite in the below page.

    http://tech.groups.yahoo.com/group/piping_valves/files/

    Good luck.
    Kannan

    --- In piping_valves@yahoogroups.com, "sskukade007" <sskukade007@> wrote:
    >
    > Dear All,
    > I have joined new in piping.
    > can you recommend me e books for theory of piping and allied components
    > (valves/flanges etc),reference tables,diagrams etc.
    > Thanks.
    > Sanjay.

    Double offset butterfly valve with metal seat

    Pl. read catalogs for more understanding.

    The subject of seating in double ot triple offset butterfly is litte bigger than other valves due to the emphasis given to the application and operating conditions.

    There are quit a few proprietary seat designs. For eg. the graphite layers gets eroded in few weeks to months due to operating condition resulting in big leak and pressure drops. The profile of the seat and disc is also important which developes the cavitation effect and pitting of the seat. So in the selection of a seat the operating condition such as the opening angle, pressure, which in turn will affect the operating pressure in turn the system design itself. So a well thought process is essential in the butterfly valve type and seat selection.

    In solid seat the cost makes the big difference.

    Regards,
    Kannan

    --- In piping_valves@yahoogroups.com, "ashoksiva1982" <ashoksiva1982@> wrote:
    >
    > Dear all,
    >
    > I have an enquiry for Double offset butterfly with metal seat. The design pressure shall be 40 bar. Can any one know the seating arrangement of competitor valves.
    >
    > I got some information from the below link. I need some more arrangement for the above requirements.
    >
    > http://www.sz-yll.cn/upload/814/200631485558638680174.pdf
    >

    --- End forwarded message ---

    Tuesday, January 13, 2009

    US Equivalent of Workstoff Nrs.


    The official Beuth's listed equivalent are

    1.8963 - ASTM A618 GR.II
    1.7218 - ASTM A 29 /A 322 / A 519 GR.4130
    1.0037 - ASTM A 36, A 109, A570 GR. 30

    Regards,
    Kannan.

    On 1/12/09, Darji Nilesh (Mumbai - Machinery) <N.Darji@ticb.com> wrote:
     
    Dear Friends,
     
    Requesting you help to furnish Eq. ASTM Grades for the following material: -
     
    1.        1.8963 (Is it better than SA 242 Gr.2 ??)
    2.        1.7218 (Required material by Process data sheet is A 1045. Material 1.7218 is better than A 1045 ??)
    3.        1.0037 (Required material by Process data sheet is CS-Epoxy painted. Selected material by Vendor is 1.0037, Is it better option ??).
     
    Matter is little bit urgent so, kindly furnish your response before noon.
     
    With regards,
     
    Nilesh.

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