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15 minutes read
18 February 2026

Pressure Vessel Failure: Case-Study

15 minutes read

We were recently hired to investigate the cause of pressure vessel failure. In my line of work, I can rarely post pictures or outcomes of analysis that we do “commercially”. This time it’s different, so I just couldn’t miss the opportunity! Especially since this will be a great educational case-study!

In this article, we will analyze a failure of a pressure vessel. We will search for the cause of failure, and wonder what to do to avoid such issues in your design. And all of that using Engineering Judgment and Nonlinear FEA.

As you can imagine, there will be no names, locations and many “sensitive details”. After all, this is a delicate topic, that is still fresh as I’m writing this. However, I got the permission to use pictures as well as description of the failure (and our outcomes)!

This means that I can write a real industry-grade case study – how awesome is that!

What happened: a short story

The analyzed vessel belonged to a new installation. As with all of such systems, the vessel passed all the leaking tests and pressure tests. Of course, the tests showed no warnings. After all the tests, operator planned the first run.

There were 4 vessels that could be in operation in the installation. For the first run, the operator decided to use only one of those (the smallest vessel of the 4).

After the “first run” started, technical crew noticed a leak from one of the bigger vessels. Of course, they reasonably stopped the process.

This deformation was spotted thanks to the leaking liquid

Initially the assumption was that this is a minor issue with a weld or something similar. However, after the technical crew inspected the inside of the 2 bigger vessels they saw this:

This is how a bad day at work looks like (if you ever wondered)

At this point, as you can imagine things became way more serious. It became apparent that it’s definitely NOT a “small thing”.

As usually in such cases, at some point operator sent a claim to an insurance company they worked with. And that insurer hired an “external expert” (yours truly) to establish the reason of the failure.

I received a set of photographs of what happened (I showed you the most important ones above, of course there were many more). Additionally I received a surprisingly vague drawing documentations of the vessels.

Sidenote:

It’s “funny” how difficult it is to obtain the complete drawing documentation of the vessel when something “goes wrong”.

… not to even mention calculations of any kind, that were performed.

Anyway, based on the drawings I had, I managed to establish that the vessels looked more or less like this:

Schematics of one of the vessels that failed

If you like the challenge:

At this point, I already knew what caused the failure.

During works, more details became available (thicknesses were measured on site, some extra details became “confirmed” etc.).

But the reality is, that what you know already is enough to realize what caused the failure!

If you wish, try to check the failure source from the info above*

*Definitely let me know in the comments how you did!

Funny enough, having an intuition about what caused a failure is one thing.

Proving that your opinion is objectively true is a completely different thing!

Let’s focus on what we know, and how to prove what happened!

What we already know

In a typical crime-novel fashion let’s start by summarizing what we already know:

  • Leaking and Pressure tests detected no issues with all the vessels (also those that failed). This is a weird thing, considering the system failed just after first launch. However, there is no reason to suspect that somebody tempered with the testing! I truly believed (and still believe) that manufacturer did those tests!
  • The start run included only the smallest vessel. It’s interesting since failure happened at the bigger vessels. Vessels that weren’t really used in the installation!
  • Operators noticed leaking in a bigger vessel (one of those that failed). This is another curious thing. What leaked, if the vessel was “not used” as the technical crew reported.
  • Shape of the failed vessels. Thank to the outside and the inside photographs of the vessels we know how the failure mode looked like. The “external” jacket (of the heating space) was ok. The inside chamber wall failed.

I wonder if such an arrangement of facts make it easier to see what was the cause of failure. Do you feel like you want to change your initial estimate?

What kind of failure happened?

All of the above, made me believe that the pressure vessel failure was a typical circumferential buckling issue.

I mean, the pictures from the inside of the shell made it pretty clear! During my work, after a few days, the removal of the failed vessels started.

This is when I also received the pictures of the internal shell from the outside:

Vessel shell with heating jacket removed

Perhaps I just spent too much time working with shells, but the above to me looks like a “classical” case of circumferential buckling at a first glance.

For curious readers:

Those short stiffeners on the shell were only there to aid the flow of medium in the heating space.

Such short horizontal stiffeners could not help with the buckling (you would need full rings for that), and I honestly don’t think designer of the vessel treated them as helping.

In pressure vessel design circumferential buckling usually happens when there is underpressure in the vessel. This underpressure is commonly called “vacuum”, even through full vacuum is not always there:

Underpressure (vacuum) can cause pressure vessel failure in buckling

Such vacuum/underpressure causes compression in circumferential direction of the shell, which may lead to buckling, of the kind you saw on the photos.

The problem here is, that those vessels should not have vacuum inside! The process (as designed) should not end with underpressure developed in the vessel at all!

Furthermore, the vessels that failed weren’t even in operation when failure happened!

So, we know what happened… we just don’t know how!

What caused the pressure vessel failure?

Luckily, we have another fact at our disposal, that will help us to identify the failure cause:

Something actually leaked during failure!

We know that the vessels that failed were not used. But we also know they were in the same installation as the small vessel that was used during the first run.

When analyzing the task, I instantly assumed, that the main chamber of the vessel was empty and “unused” during failure. After all vessel was not working during failure. I figured this is what the operator meant.

However, I suspected circumferential buckling, so I knew that something needed to cause circumferential compression in the shell. I assumed that it is at least possible that all 4 vessels have a common heating installation.

If my assumption was correct, it would solve one of the “mysteries”. It is obvious that the heating was “on” even if only one vessel was working. This would mean, that the heating space in each vessel would be full, even if only one vessel was in operation.

This fits the observations for 2 reasons:

  • First and foremost, that would give us the medium that could leak. After all operators noticed something leaking!
  • And what is at least as important, that would cause the circumferential compression that lead to failure we observed!

Of course, my first question to the Customer was: do the vessels have a common heating system? And as you can suspect at this point, they confirmed my suspicions.

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How the pressure vessel failure happened?

At this point, the story is fairly straightforward I feel. But let’s get to the end!

As you can see on the sketch I’ve made, the heating space was super small (30-40mm wide if my memory serves). The amount of medium that it could contain was minimal of course. This made it easy for people to “discard this” when they explained what was happening (but also in calculations).

However, hydrostatic pressure doesn’t care how many liters of medium there is! It only cares how high the medium surface is! And in our case, with a full heating space, it would look like this:

External hydrostatic pressure also can cause pressure vessel failure in buckling

Of course, if there would be an overpressure (due to technology) in the heating space, if would be even worse!

With this understanding, proving how the failure happened is very easy. Just use Nonlinear FEA, and you won!

Technically speaking you can make a very simple hand calculations to check that the shell “had no chance”. However, such calculations can never include those short stiffeners on the shell. And while I knew those did not help, I had to consider that someone may doubt this… so I simply included those in our model.

In the end, the failure of this vessel obtained in FEA looks like this:

And for failure comparison, this is the FEA outcome and the image of the pressure vessel failure (both without the outside heating jacket):

Without a doubt buckling shape is a bit random. It strongly depends on initial imperfections, and of course we could not have measured those pre-failure. But even with this in mind, the similarity of failure mode in reality and FEA is very good.

Of course, the analysis showed, that when the heating space was full (with some overpressure that was present), the inner shell had no chance! The capacity was significantly too low, and failure… simply must have happened (and it did).

Conclusions

From time to time my Customers ask me, why I want to analyze so many things when we do industrial calculations. To them, it may seem that some of the things are simply “unimportant” or “negligible”. It’s tempting to ignore them in design!
I usually politely reply, that we already ignored the things we believe are “unimportant”, and that the rest should really be there.

I feel this case study shows very well, why paying attention to details really matter in engineering, and why I’m so accurate when it comes to those things.

The heating space could contain about 600l of medium (0.6m3), causing a total vertical load of 6kN. This is around 6% of what the main chamber could hold.

I can easily see, how one could say this is “negligible”, especially since heating space was really narrow, so it also looked “innocent”.

Hydrostatic pressure in the heating space (along with some extra overpressure there) was a direct reason why the vessels buckled (when the main chambers were empty).

Clearly, hydrostatic pressure in the heating space was not something you could neglect in the end…

But it seemed like something that *could* be unimportant, and it actually was neglected! Not only in design, but also in testing of the vessel.

And this neglect was the direct reason that lead to vessel failure.

As I’m writing this, I’m pretty certain that the design never considered external pressure on the main vessel shell. If it would… the simplest of checks would show that something is wrong.

Sadly, I was unable to confirm if the vessel tests really happened. Personally I believe they did happen. I simply don’t want to think that someone said they did tests and simply lied.

But why the tests found no issues?

I believe, the issue lies in planning of the tests. If I would have to guess, I would say that testing order was something like this:

STEP 1: Fill in main chamber. Test for leaks and pressure in the main chamber.

STEP 2: Add medium to the heating space. With both areas filled test the heating space for leaking and pressure.

… and that’s it!

I mean, it would be deceivingly easy to think “more medium must be worse”, and “those extra 6% change nothing” during testing as well. And its very short from there to saying “let’s not waste time testing the heating space alone”.

After all, the test of the heating space with an empty main chamber would fail in any reasonable circumstances. After all, the vessels failed on the very first run of the installation!

Worth remembering:

The next time you will feel like removing something from the scope of the calculations (or someone will ask you to do so), remember that even seemingly small things may have big consequences.

Finding this fault at any stage of design, manufacturing and testing would lead to significantly less trouble and costs.

The worst thing that can happen is, that you “hope” that something is negligible, you don’t check it… and then it fails on site!

Those cases are the true nightmare of costs and legal responsibilities.

Heck, maybe even send your Customer the link to this article, so they can read about it themselves (I will do this for sure!).

In the end: If you have any interesting design, or failure you need help analyzing – definitely send me an email – I will gladly discuss it!

Tying all loose ends… for extra curious readers!

Above, I outlined the most important things that allowed to determine the cause of failure. However, a few more things crossed my mind when I was examining this case.

I figured you may be as curious as me, so below a few extra considerations:

  • Boundary Conditions. For shell buckling they of course play an important role. Of course the bottom and the top are easy to represent (just model them!). However, brackets boundary conditions could potentially be a mystery. For example brackets could be welded to infinitely rigid structure or something improbable like that).

    Luckily, the vessels were standing on weighting equipment that didn’t restrain rotation at all. This is a small thing, and the impact on outcomes would be small. But I’m still satisfied with the fact that I could be accurate there.
  • Small stiffeners on the shell. Funny enough, if the small horizontal stiffeners would be welded to both inside shell and the outer heating jacket, they would help! I don’t mean the “stiffening of the shell” (although that would help as well a little). The trick is much easier.

    We have a hydrostatic pressure on both inner and outer shell. Since the hydrostatic pressure acts on the shells in opposite directions, one shell pulls to the “left” and the other to the “right”. If we connect both shells quite often, the acting forces balance each other out! In such a case a significant circumferential compression would not develop.

    Sadly, there isn’t really a way to weld such stiffeners at both ends (not enough space for the 2nd welds!). Not only that, but the inside pictures show the heat marks on the shell from welding. You can’t find such marks on the outside jacket from the outside (hence no welding). And finally – after the jacket was removed, it became clear that the stiffeners were not welded to it.
  • If this vessel had higher “design” internal pressure… it could work. The thing is, that if significant pressure was foreseen in the main chambers the walls of the vessel would be thicker. With that, they could have a chance to withstand the buckling…

    Of course, it’s always better to simply check the capacity, rather than “hope for the best”.
  • Only the inside shell failed. Hydrostatic pressure was acting with the same value on the external jacket and internal shell. But only the inside shell was compressed (the jacket was in tension). This is why the external jacket looked nice, and they noticed the buckling only after looking to the inside of the vessels.
  • Leaking was a result of deformations. Funny, because it’s the leaking that indicated the failure. And leaking is completely a secondary issue. After the vessels buckled, the shells deformed heavily, and some welds failed to accommodate the deformations and cracked. This caused the leak that alarmed the technical crew.

    It’s so good that they knew what to do, and looked inside of the vessels! After all, they also could try to “fix the leaking weld” from the outside.

I really hope that this case study shows the beauty and complexity of engineering.

Sure, this was a failed design, but thanks to the company that hired me to search for the failure, I could share the above conclusions, so we can all learn from this.

I hope you can also see that Nonlinear FEA is great at solving such issues and leaving no stone unturned. But I also hope that it’s obvious that you also need a good engineering knowledge.

After all, if you would not think to check such a load case, Nonlinear FEA wouldn’t find an issue either! You need to know what you need to check to properly use FEA (or any other design method).

I really hope you enjoyed this one!
Let me know what you think in the comments, and feel free to recommend this to any colleague of yours who may benefit from reading this case study!

Author: Łukasz Skotny Ph.D.

I have over 10 years of practical FEA experience (I'm running my own Engineering Consultancy), and I've been an academic teacher for a decade. Here, I gladly share my engineering knowledge through courses, and on the blog!

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Comments (10)

Frye - 2026-03-21 13:57:20

I found it a bit surprising that the hydrostatic pressure was enough to cause circumferential buckling. I'm making some very rough assumptions to get ballpark figures (assume 3m PV length, assume conservative 1200 kg/m3 fluid density) results in a peak hydrostatic pressure of 35ish kPa. As you noted the axial buckling capacity of the PV was 100ish kN, I backed out some diameters and thicknesses that result in that capacity, and it seems like that should be able to carry 35kN without resulting in circumferential buckling. However giant caveat as I'm making a ton of assumptions in terms of geometry, not to mention material assumptions. Anyway, interesting read, thanks for sharing!

Reply
Łukasz Skotny Ph.D. - 2026-04-06 20:37:12

Hey Frye!

To be honest, this is not that surprising. Shells are insanely more resistant to circumferential tension (I.e. pressure from the inside). Plus, the fact that there was 100kN of liquid inside doesn't change the fact that hydrostatic pressure from the inside (the tension one) wasn't all that much higher than the compressive pressure from the outside from the heating space (when vessel was empty). The difference was only from the fact that on the inside the liquid level was "higher" than the heating space, so the hydrostatic pressure was proportionally higher.

And also, the fact that there is 100kN of liquid in the shell, doesn't mean that it's buckling capacity in axial direction should also be 100kN... that liquid is not "standing" on top of the vessel to cause vertical compression - if anything it "stands" on the bottom (causing vertical tension in the shell). Perhaps this assumption there, lead to discrepancies in your estimates and my calculations.

I admit that I'm writing this from memory, but I don't think that the inside pressure when the tank was full was more than 30% higher than the external pressure from the heating space. In such proportions, external pressure causing buckling is SO MUCH WORSE to the shell that it's not even funny...

Reply
Ievgen K - 2026-03-11 18:01:16

It was a pleasure to read the article. Thanks

Reply
Łukasz Skotny Ph.D. - 2026-03-11 18:53:35

Thank you for a kind comment. I'm so glad that you enjoyed it :)

Reply
Paul Stevens - 2026-02-26 15:21:16

Interesting case Lukasz, and perfectly explained.

Reply
Łukasz Skotny Ph.D. - 2026-02-26 17:14:46

Thank you Paul! I'm so glad that you liked it :)

Reply
Hubert - 2026-02-25 07:18:24

Fascinating to see such a small detail causing such dramatic consequences.

Reply
Łukasz Skotny Ph.D. - 2026-02-25 11:32:11

In my experience it quite often happens, that "small details" are the reason for dramatic consequences. And yet, in many projects I faced issues because someone at some point ignored something... and now we have a big problem.

I hope this article at least shows the importance to checking stuff...

Reply
k - 2026-02-24 15:44:55

Thanks. It is very good real life example .

Reply
Łukasz Skotny Ph.D. - 2026-02-24 18:06:38

I'm glad that you liked it Mate :)

Reply

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