Thanks for the response.
Original Message:
Sent: 03-21-2023 11:58 AM
From: Matteo Loizzo
Subject: MAASP calculations and degraded fluids
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,
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Matteo Loizzo
Well integrity consultant
matteo.loizzo@mac.com
Berlin, Germany
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Original Message:
Sent: 03-21-2023 04:43 AM
From: Omair Sadiq
Subject: MAASP calculations and degraded fluids
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.
Original Message:
Sent: 12-06-2016 02:31 AM
From: Philippe Rabis
Subject: MAASP calculations and degraded fluids
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.
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Philippe Rabis
Well Integrity TA - Completions Lead
Maersk Oil CTP
Kobenhavn K
Original Message:
Sent: Nov 14,2016 06:19 AM
From: Matteo Loizzo
Subject: MAASP calculations and degraded fluids
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,
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Matteo Loizzo
Well integrity consultant
Berlin
Original Message:
Sent: Nov 14,2016 06:08 AM
From: Paul Hopmans
Subject: MAASP calculations and degraded fluids
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
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Paul Hopmans
Software Portfolio Manager
Shell Technology E&P
Bergen Op Zoom