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MAASP calculations and degraded fluids

  • 1.  MAASP calculations and degraded fluids

    Posted 11-07-2016 01:59 AM

    Dear All,

    what is your approach to the determination of mud gradient in annuli of 'old' wells for the calculations of MAASP (or minimum pressure to maintain in production annulus to avoid the risk of collapse of the production casing) ?

    ISO 16530 annex K 'MAASP calculations' refers to 'highest MG' and 'lowest MG' however we all know that mud quickly degrades and loses its gradient/weight properties (sagging effect,etc..).

    So how to consider the hydrostatic column of fluid left behind the casing (all the more critical when the top of good cement is much lower than expected) ? 

    For old wells candidates for workovers, calculations based on initial fluid properties seem overly conservative.

    Meanwhile, considering base fluid of the mud left behind casing seems also an extreme view.

    As a reference, I'd like to quote paper AADE-12-FTCE-47.

    Thanks to All

    ------------------------------
    Philippe Rabis
    Well Integrity TA
    Maersk Oil CTP
    Kobenhavn K
    ------------------------------


  • 2.  RE: MAASP calculations and degraded fluids

    Posted 11-07-2016 02:16 AM

    Dear Philippe,

    A very interesting discussion. There is indeed some settling and sagging in most drilling fluids, but very little to no data about how quickly and how far (if you could share the paper "What Happens to Invert Mud Left Behind the Casing?" I'd be grateful).

    This seems to be a very local phenomenon that depends on the suspension mechanism (e.g. some polymers get eaten by bugs), geometry of the annulus and subtle ageing processes. On top of it, density gradients do not affect total hydrostatic, unless the solid particles bridge the annulus: wall friction then takes over from hydrostatic and you only transmit the base fluid weight. Incidentally: hydrostatic can only decrease: part of the particle weight will be taken over by axial stresses in the casing. Normal stresses can be concentrated where solids accumulate, but average hydrostatic will be reduced (if that's what you're concerned about when you talk about production casing collapse).

    The safest way would be to consider hydrostatic of your base fluid (brine or base oil): your actual situation will be somewhere in the middle. If you want to be precise and you can log, an ultrasonic imaging tool will allow you to calculate fairly accurately the MG profile, if properly acquired and calibrated.

    ------------------------------
    Matteo Loizzo
    Well integrity consultant
    Berlin



  • 3.  RE: MAASP calculations and degraded fluids

    Posted 11-08-2016 09:30 AM

    Hi Philipe,

    Mud degradation is an issue we wrestle with at all times during our well integrity & casing design review projects. This can become critical especially in association with the annular pressure build-up phenomenon (APB) that may be occurring on either side the casing.  For example if an annulus is only partially cemented, with a TOC located in the open hole, then any APB developing in that annulus and driven by the formation fracture gradient (or a higher value in some cases) would be largely dependent upon the density of the mud located in that annulus.  Hence a reduction in fluid density could significantly increase the MASP for that annulus.  Using the base fluid density is indeed the worst case, while some operators tend to simply use a density reduction by 2 ppg, in lack of any real data.  Ideally, you would like to have some long term test data to see the how mud density changes in down-hole P-T conditions for long periods of time.

    From a casing design perspective, it is critical to account for all such options, identify the worst cases realistic scenarios and go with that. Especially if APB is an issue, many loads cases should be defined in order to account for all possible scenarios.

    Regards,

    Nick Stefu

    Senior Tubular Design Specialist

    Halliburton Consulting

    ------------------------------
    Nick Stefu
    Senior Tubular Design (WellCat) Specialist
    Halliburton Consulting
    Email: Nick.Stefu@halliburton.com



  • 4.  RE: MAASP calculations and degraded fluids

    Posted 11-14-2016 05:08 AM

    Please Note ISO 16530-1 That is now out for final ballot does address degrade fluids in the Maasp calculations examples, Please have a look 

    ------------------------------
    Paul Hopmans
    Software Portfolio Manager
    Shell Technology E&P
    Bergen Op Zoom



  • 5.  RE: MAASP calculations and degraded fluids

    Posted 11-14-2016 05:19 AM

    That's interesting, Paul! I guess the new version is still not out. Could you share with us the outline or the approach, or a draft copy of the standard?

    Thanks,

    ------------------------------
    Matteo Loizzo
    Well integrity consultant
    Berlin



  • 6.  RE: MAASP calculations and degraded fluids

    Posted 12-06-2016 02:32 AM

    Thanks to All for the discusion.

    Regarding the new ISO, looking foward to reading the new version. However, until now, degraded mud was looked after only on a conservative point of view, ie fully degraded on the outer annulus of the tubular for burst calculations, for example.

    ------------------------------
    Philippe Rabis
    Well Integrity TA - Completions Lead
    Maersk Oil CTP
    Kobenhavn K



  • 7.  RE: MAASP calculations and degraded fluids

    Posted 03-21-2023 04:44 AM

    Dear Matteo, Philippe & 'whoever else who can help',

    What's your advise on gradient assumption for MAASP calculation in case there is cement (assuming solidified with an initial weight of 16 ppg) outside the pipe and 9 ppg liquid inside the pipe? 

    I am stuck with what gradient is practical to assume outside the pipe considering the cement solidifies over time and hence should not exert hydrostatic pressure.  I have been told to use the cements gradient. Your thoughts please.

    The standards I see talk about degraded mud gradient, which seems to be a case when cement is intentionally not to surface rather it is limited to a few hundred feet above the affected casing shoe leaving the vacant space filled by mud or some other fluid.




  • 8.  RE: MAASP calculations and degraded fluids

    Posted 03-21-2023 11:59 AM

    Dear Omair,

    As much as I would like to give you a simple answer, I'll play the geologist and tell you "it depends".

    As you correctly point out, pore pressure (if it makes sense to define such a thing) in cement is below hydrostatic, effectively close to zero. That depends on cement weight: soft, porous lead will have pore pressure gradient equal to a light brine.

    However, you want to know what is the pressure in a possible leakage pathway, since that is the value you subtract from the reservoir pressure to compare the annular profile to the ratings of the different wet elements (it would be a different story if you wanted to compute casing failure, but I digress).

    So here are a couple of rules of thumb:

    • If it is a chimney left behind by early gas migration, or a mud channel (very rare, only consider it if well deviation at the top of cement >60 deg), then the pathway cross section is enough to allow liquid counter-flow. In this case the pathway hydrostatic gradient will be equal to reservoir fluid density. There may be phase separation if there is no constant flow (e.g., in case of a build up). In this case density will decrease to gas.
    • If it is a microannulus, then you have two scenarios:
      • If the reservoir is light gas (gas will always be water saturated), then for an initial short time you will have gas gradient. Then as the microannulus floods and you move to scenario 2.
      • In any other case, including after an initial transient with a gas reservoir, you will have water gradient. As in freshwater or seawater gradient.

    What you're guaranteed never to have is slurry gradient, as you pointed out.

    Degraded mud is another can of worms: WBM tends to degrade, as polymers rot, but OBM/SBM can have surprising stability. In practice, though, you may have a gas cap (because of cement dropping), base oil separated at the top (which doesn't change hydrostatic), and barite sagging that may create "plugs". How much can you transmit hydrostatic below such a plug? No reliable data. So you need to measure the gas cap volume.

    Would I use degraded mud gradient, like the fudge factors wireline engineers are alleged to use to make logs look good? (Of course they don't, it's a legend!) No.

    Hope it helps,



    ------------------------------
    Matteo Loizzo
    Well integrity consultant
    matteo.loizzo@mac.com
    Berlin, Germany
    ------------------------------



  • 9.  RE: MAASP calculations and degraded fluids

    Posted 03-22-2023 12:11 AM

    Thanks for the response.




  • 10.  RE: MAASP calculations and degraded fluids

    Posted 03-22-2023 08:38 AM
    I’ve worked with several companies (consulting) working within their design rules and have seen quite a bit of disparity on this point. I’ll list a few of this I consider to be the most commonly accepted ones. But first, I must point out that as you do the MAASP calculations, you must examine all anticipated or probably event conditions, AND recognize that this includes temperature as well as pressure, particularly for production events that include water; this means you should have the working pressure at temperature for all of the exposed components. It is best practice to include the entire anticipated lifetime of the well in deciding which events to consider.



    Now onto the rules for external gradient that I am familiar with:



    1. Cement slurry gradient only for events during cementing operations when the slurry is present on the outside.
    2. Cement mix water gradient is used by a few for events that occur soon after the cement sets. This is conservative for burst cases, but not for collapse.
    3. Pore Pressure outside set cement is almost universally accepted.
    4. If there is an uncemented section, the fluid gradient is applicable. In most cases this is higher than the pore pressure. In collapse cases you might consider what happens to the column with leak-off.
    5. If the fluid contains weighting solids, than at some point these may settle. Several operators have rules on how quickly and how complete the fluid settling should be considered. The fluid seller (mud company, brine company, etc.) can usually provide this information.




  • 11.  RE: MAASP calculations and degraded fluids

    Posted 03-21-2023 11:55 PM

    Dear,

    For degradation, this is my personal opinion to use cements gradient/mud gradient. You never now the cement all the way to surface or maybe some top up job,

    1. use a percentage base degradation per year. 1% - 2% should be ok
    2. assume the solids in the fluid no longer contribute to the hydrostatic,
      1. use the based fluid, freshwater or lighter base oil s.g. 0.8 to 1.0
        1. Normal design i would say Usually has lighter fluid compare to the outer. The idea to avoid burst of casing, 
          1. so degradation will impact the burst calculation (differential pressure_
      2. Calculate Inner annulus pressure gradient & outer annulus pressure gradient
      3. Net impact will tell you whether potential burst or not
    3. Use Tri-axial analysis and incorporate Temperature effect
      1. You can use wellcat to model this and i think the latest version you can input the degradation for fluid
    4. Top up your annulus fluid with heavier brine - so degradation can be excluded



  • 12.  RE: MAASP calculations and degraded fluids

    Posted 03-22-2023 12:12 AM

    Thanks for the response.




  • 13.  RE: MAASP calculations and degraded fluids

    Posted 03-22-2023 06:24 AM

    Hello Omar,

    In addition to other replies here's how I'd handle this:

    1. After the cement has set the original slurry density becomes irrelevant > use the sg of your mix water
    2. After many years (old wells) same approach: fluids will degrade over time, weighing agents in particular will tend to sag, emulsions will break > use your base fluids sg (you can make an assumption re: your brines as those will likely exchange ions with formation water if any, and gradually lose salinity/weight

    If this quick-look approach shows you might be dangerously close to your limits, you probably should take a closer look...
    Pls note (I assume you know) that internal yield is easier to predict, affected by potential cement, etc... The collapse case is a lot more tricky to assess and will also likely be affected (if not driven...) by ovality, wall thickness and... presence of cement too!

    Rgds.




  • 14.  RE: MAASP calculations and degraded fluids

    Posted 03-24-2023 01:47 AM

    Thanks for the valuable input Pierre.




  • 15.  RE: MAASP calculations and degraded fluids

    Posted 03-23-2023 08:46 AM
    The gradient behind pipe is definitely not the density of set cement. During cement jobs the weight often fluctuates a few tenths of a ppg and if they lose a tub of cement and have to restart they sometimes can pump 8 - 10 bbls of water in your cement column. This has lead to many casing failures due to bucking and bur,st made worse by engineers not using the proper gradient behind pipe.

    The safest method is to assume the original formation gradient. So, If you are normally pressured to 10,000 ft use 9.0. If you get into abnormal pressure below that raise the gradient to accommodate for it.

    Mike Chaffin
    Valence Operating Company




  • 16.  RE: MAASP calculations and degraded fluids

    Posted 03-24-2023 01:48 AM

    Thanks for the valuable input Mike.




  • 17.  RE: MAASP calculations and degraded fluids

    Posted 03-22-2023 06:25 AM

    Bonjour Philippe,

    Feel free to get in touch directly and we can chat... I recently posted a query on a somewhat related subject and have some info to share, if you'd like.

    Cheers.




  • 18.  RE: MAASP calculations and degraded fluids

    Posted 03-23-2023 03:45 AM

    PT point of view.

    Its not uncommon for us to see mud in the production annulus for wells that are 15 years or older.

    To calculate MAASP, however, you should take the decision from the conservative approach. 
    An event happens and you have to explain to the government authorities why you calculated a MAASP based on a solids laden fluid that supposedly can never degrade over time. Its usually an ugly explanation.
    Thank god, we have evolved and the newer wells only have non solids annulus brines

    So,

    1.    We do not degrade the static gradients of non solids annulus brines

    2.    We degrade WBM muds to the base fluid (which is usually almost a water gradient). Yes, there is most likely a big huge plug of solids above the packer (or TOC) that is a barrier but we cannot prove that. (or test it, legally). This provides a very low MAASP with many operational pressure reliefs cycles but we have no choice but to deal with it.
    Some years back, we actually used an echometer on 15+ wells in the middle east to discern the fluids/solids interface in the annulus. Yup, it all sagged to a nice blob of solids at the bottom of the annulus.

    3.    OBM and SOBM is a more complicated story.
    (We generally don't deal with this problem too much, since its rare for the drillers to leave this expensive mud behind in the annulus!)
    We always get the mud vendor to provide us the sagging properties of the mud. They generally have pretty good data for their long term ageing mud performance. If they don't have any data, get them to perform a 3-6 month mud ageing test under pressure and temperature. (Your drilling team can help you with this).
    Our experience, generally the OBM/SOBM's that are left behind in the annulus are usually of "lesser quality" and usually fall apart very quickly in less than one year.
    So, we are stuck to grudgingly using the base fluid. (and yelling at the drilling not to leave mud in the annulus.)

    Note: The entire conversation above is related ONLY to a full fluid column for MAASP calculation for the A,B,C,D annulus above the TOC (or packer).
    It does not consider the cement column, we consider that solid. (since the drillers told us so…!). 
    Legal verbiage important here!! 😊



    ------------------------------
    Basker Murugappan
    Principal Production Technologist
    Villalbilla, Spain
    +34 644485970

    Three basic rules:
    1) Change is inevitable.
    2) Everybody resists change.
    3) You cant stop change
    ------------------------------



  • 19.  RE: MAASP calculations and degraded fluids

    Posted 03-24-2023 01:49 AM

    Thanks for the input Basker.