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Hydrostatic Test Failure 6

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I came across a YouTube Video yesterday that has completely changed my thinking on hydrostatic testing vs. pneumatic testing. First, after a lot of digging, I found some of the details on the line:
[ul]
[li]ANSI 600 line[/li]
[li]Test was a fully degassed hydrostatic test (water for the test had been loaded 2 days before the test and allowed to degas)[/li]
[li]Tested to 130% of MAWP (1870 psig test pressure)[/li]
[li]All fittings and pipe were U.S. made[/li]
[li]All welds around the failure passed x-ray[/li]
[li]The line was owned by one of the largest pipeline companies in the U.S.[/li]
[li]The construction contractor had done hundreds of hydrostatic tests for that particular pipeline company and others[/li]
[li]The test was done following a procedure that had been reviewed both by the engineering contractor and the pipeline company[/li]
[/ul]
My eyeball is not well calibrated, but it looks like 30-inch pipe, but it might be smaller. I took a screen capture from the video to show the failure point
Ch06Fig32_a5th0d.jpg

You can see from the picture that the failure started next to the weld, not in the weld.

I watched the video and asked myself "where did the energy come from to tear out a flap of steel and bend it up 90° against the curve of the pipe?" That was a huge force.

That is when I realized that the bulk modulus (i.e., the amount of pressure that would decrease the volume by 1%) of water is 319,000 psia, so to reach 1870 psig you would have to add 0.006% of the system volume. I looked at the enthalpy of the water at rest and the enthalpy of the water at test pressure and found a 5.3 BTU/lbm change. For a test that was more than a few joints long, W=m*ΔH+Δm*h turns out to be a really really big number. Archimedes Principle says that a force applied (or removed) from a closed volume will be transmitted everywhere within the closed volume, so this huge energy acts like a coiled spring that releases its entire energy at the failure point.

I've talked on this site many times about the errors in the NASA Glenn Research Methodology used by many to calculate the energy of a pneumatic test. Primarily my point has been that there is no way for distant mass to "know" about a failure and the mass that participates in a in a failure is limited to a few joints worth of gas.

The change in my position is that I've always been a bit defensive about the use of pneumatic tests, but I was wrong to be defensive. The energy available to strike nearby workers is far higher in a pipeline hydrostatic test than a pipeline pneumatic test. If we assume that the failure in the video was 5 miles of 30-inch pipe, then I calculate that the energy release in a pneumatic test would be 0.2% of the energy that could be released in a hydrostatic test. Yep, pneumatic tests are irresponsibly dangerous. NOT.


[bold]David Simpson, PE[/bold]
MuleShoe Engineering

In questions of science, the authority of a thousand is not worth the humble reasoning of a single individual. Galileo Galilei, Italian Physicist
 
We routinely hydro-test (water) our products to burst, with sizes roughly equivalent to the 35 gal. barrel. When done properly (air removed) the test is pretty un-dramatic and quite safe. We occasionally get splashed with water, but nobody gets hurt. This is similar to our typical test experience:

 
btrueblood,
I've done those vessel/pipe expansion calcs before and it didn't matter if the pressure came from a gas or a liquid. The numbers were really small.

I've always agreed that any test where the farthest fluid was less than about 20 m from the failure would have more energy applied to the failure in a pneumatic test than in a hydrostatic test. Nothing about this change in my thinking changes that position. For small volumes the amount of liquid you have to add to raise pressure in a hydrostatic test is tiny and the compressive energy is also pretty small, so when those tests fail you get a "pop" and water on the floor. The physics of this kind of test was very well explained in 1988 in:

“A Review of Energy Release Processes from the Failure of Pneumatic Pressure Vessels”, M. Coleman, M. Cain, R. Danna, C. Harley, D. Sharp, General Physics Corporation Cape Canaveral Air Force Station, Florida.

The thinking fell off the rails when NASA has a summer intern "scale up" that analysis to pipeline scale in the 1990s and he failed to take into account that energy transfer in gas required mass transfer (which is limited by the speed of sound), while in hydraulic systems the energy transfer happens with minimal mass transfer.

Weldstan,
Exactly right, I have had a lot of engineers imply that hydrostatic tests are zero risk and pneumatic tests are literally "playing with dynamite". The change in my thinking is that hydrostatic tests are playing with a lot more dynamite than pneumatic test are on pipeline tests.




[bold]David Simpson, PE[/bold]
MuleShoe Engineering

In questions of science, the authority of a thousand is not worth the humble reasoning of a single individual. Galileo Galilei, Italian Physicist
 
I guess I've always kind of liked the statement contained early on in the document at
"The hazard posed by a pressure test is a combination of the energy stored in the pressurized fluid in the equipment and the degree of ignorance about the suitability of the equipment to contain pressure..."

When I later took time to look at the OP linked "video", I have a tendency to wonder along with LI on this one. At one thousand eight hundred and seventy psi on this system (and who knows what else e.g. thermal etc?), I believe there would have had to be a substantial transverse resultant thrust on the outside of the 90 ell several feet from the tee. With no backfill around the piping (i.e. nothing but air around same and behind the ell, that of course has little resistance), there would appear to be relatively very little to restrict at least Bourdon movements of that piping in at least the ell area under pressure. Even slight deformation/movement of the 90 ell and adjacent branch piping would of course beam load the connection at the tee branch, introducing some additive localized stress within same (i.e. in "pully-bone" fashion, as they say down South, or "wish-bone" fashion to Northeners). While I'm sure different forensic folks would probably put their finger on what they wish after this event and I would not venture cause without seeing a stress analysis in this condition, I wouldn't be surprised if quite high local stresses were imposed on this one (and one wonders if this layout of testing and the as-built tee strecture was analyzed for such condition?) While I guess the perception may be that modern pipers know a whole lot more and have a whole lot more control over all things that might or can go on in the cradle to grave lifecycle of a pipeline job, maybe one could add just a few words to the HSE statement,

The hazard posed by a pressure test is a combination of the energy stored in the pressurized fluid in the equipment and the degree of ignorance about the suitability of the equipment to contain pressure in the tested condition.

As to relevance to air vs hydrotesting, I don't know what exactly would have happened here had this been a gas test, but I kind of suspect the aftermath may not have looked any prettier (nor the folks standing around's drawers being any drier when it blew!) All have a good weekend.
 
The first is relatively easy to mitigate. The second is the one that is considerably more difficult.
 
elphou,
Speaking of "complete ignorance" please take a glance at a mirror.

The link you provided started with the assumption that hydrostatic tests are inherently safe and that pneumatic tests are inherently hazardous and built from those assumptions. The video that I started this thread with shows that there is nothing inherently safe about hydrostatic tests. The basic assumption is that water is incompressible. That assumption is inherently wrong. If you add 600 gallons of water to a full system, then you have obviously compressed it.

The difference between the results of the failure is "energy distribution" and "energy transport". A gas can only transfer energy at the speed of sound. A liquid will transport its energy in a single event (obvious when you track pressure miles away from a failure and see that pressure drops to zero in micro-seconds in a hydrostatic test while it may take a couple of hours for the pressure at the same place to drop to zero. That energy had to go somewhere. In a pneumatic test you are limited to about 50 ft of pipe that can get to a failure during the "explosive decompression" period. In a hydrostatic test the entire volume participates in the explosive decompression.

[bold]David Simpson, PE[/bold]
MuleShoe Engineering

In questions of science, the authority of a thousand is not worth the humble reasoning of a single individual. Galileo Galilei, Italian Physicist
 
For as much time & money pipeline companies spend these days on "safety", one rule that remains inherently dangerous to contractors & employees across the industry is the required setback distances during pipeline hydrotests (usually only 50 - 200 ft required from my experience). This is ignorance 101. zdas sheds light on a great point. Anyone who's ever been around a pipeline hydrotest failure understands this.

 
Krausen do you have some point you're trying to make? both methods of testing can be very dangerous and each requires certain mitigations to be put in place. One more than others.
 
It appears that failure started in the Heat Affected Zone.
 
Skimming over this thread I didn't see much mention regarding test temperature.

I understand this is pipeline related but I'm going to make some very broad assumptions and generalizations for the sake of getting some numbers, not accurate or directly related to this system;

Code - ASME B31.3
Material - API 5L X52
Pipe Size - 24"
Long Weld Factor - 1.00 Seamless - Why not, for the sake of easy math?

This would put minimum thickness around 3/4". API 5L X52 follows curve A, which for 3/4" gives a MDMT of 53 °F.

Material and welding may have been based on normal operation of 70+ °F process but hydrotesting in winter when it's 40 °F may have not been properly accounted for. It was also mentioned that they left the line to vent entrained air for two days, could have provided time to cool down to ambient temperature. Just curious on the possibility that temperature wasn't properly considered when the hydrotesting was performed and stress risers at the weld caused overstress when the material went brittle.

Thanks,
Ehzin
 
As a separate comment, I think there's quite a bit more emphasis on the compressibility of water and not enough on the spring forces caused by induced pipe strain. The circumferential increase due to internal pressure for a long pipeline system can add up drastically.
 
Thanks, Don(there is an old saying in research to the effect that a test may be worth a good many opinions). As to the observed conditions of this break in the photo, intersecting cylinder-to cylinder e.g. "tee" pressure connections are an interesting study, with I suspect untold numbers of technical papers etc. written about same even long before I got into the piping field. I am however aware a paper by some U.S. Energy Research and Development Administration's (ERDA) Oak Ridge National Laboratory folks concerning some analytical and experimental work written way back about the time I got into the piping field entitled "EXPERIMENTAL STRESS ANALYSES OF CYLINDER-TO-CYLINDER SHELL MODELS AND COMPARISONS WITH THEORETICAL PREDICTIONS", that is perhaps not an overly complicated read. This work is now/still available online at . One can see in that work that "accurate" design information for same was reportedly some hard to come by at that time and, "This is true even for idealized configurations consisting of two cylindrical shells intersecting normally, with no transitions, reinforcements, or fillets in the junction region." The ORNL models and corresponding experimental samples were subjected to various loadings including "internal pressure" and also some out-of-plane (bending) loads. One would also read there a conclusion (probably not all that surprising to most), "In all the chosen cases, the maximum measured stresses occurred at the junction between the nozzle and cylinder."
While there is certainly not enough firm info defined at least in the OP of this thread to know whether or not any of this is applicable to the present case, see that the results of the ORNL research revealed "maximum stress ratios" (it appears basically stress multipliers they defined as the ratio of the actual determined maximum principal stress divided by the nominal hoop stress of a similar dimensioned cylinder) of from 9.0 to 13.3, due to internal pressure alone on the model tees.
It would thus be at least interesting to look at the "design" of this actual connection for withstanding the internal pressure and any other loads imposed, given enough firm information.
I also happen to have a hard-copy only of another paper entitled, "Approximate Analysis of Intersecting Equal Diameter Cylindrical Shells Under Internal Pressure" written by professors Kalnins and Updike of Lehigh I think not long after the ORNL work (obtained when same could be had for $1.50 from ASME!) that also elaborated on "radial displacement"/shape changes of intersecting cylinders. It explained that due to the fact the "hoops" of one cylinder, which intersect those of another. are in effect "broken" (if there is to be unimpeded flow passage), the load in addition to the stress concentrations also tends to push the top meridian of the branch outward, and thereby ovalling same outward in the process. In looking at the one picture provided, it thus appears that once the fracture cut loose that flap of metal went basically where it was wont to go, as the specific meridian the Lehigh profs referred to would appear to basically bisect that pointy flap of metal looking at one in the pic. In conclusion, one has to wonder about the localized stresses that actually came to bear on this connection, and accept that the flap of metal was bent basically in the direction it was loaded. I'm not sure what else can be concluded now, but the new video added here may well be helpful.
All have a good weekend.
 
Don56,
The video compared a 20 gallon vessel hydrostatic test to a pipeline test of undisclosed (but very large) volume. Yep, a thousand pounds of TNT makes a bigger hole than a firecracker would, even though both have about the same blast-propagation speed. So what?

The audio in the link was garbled so I couldn't tell what they were saying, but the dismembered body parts make it pretty clear that they weren't being favorable towards pneumatic testing.

[bold]David Simpson, PE[/bold]
MuleShoe Engineering

In questions of science, the authority of a thousand is not worth the humble reasoning of a single individual. Galileo Galilei, Italian Physicist
 
The resolution of that video is pretty low. On the left is the "victim", which is impacted before the cylinder on the right explodes? Is that what I'm seeing?
 
While it took some doing, I found a version of at least the second part of the video with quite clear audio (from a speaker who looked strikingly like now departed Glenn Ford!) at I guess these clips thus may well be from an old "Dowell" safety video, and while the piping for the second part was indeed much longer than the fatter vessel we saw at the other URL, it was also a whole lot smaller diameter, and I'm not real sure it was an extremely/infinitely long stretch they had under pressure, nor exactly what their motive would have been for making the contained volume much different?
 
The line was "purposely weakened" in at least 5 places that I could pick out on the video. That made 5 distinct explosions. In real life, it would have been a single explosion and a pipeline blowdown.

[bold]David Simpson, PE[/bold]
MuleShoe Engineering

In questions of science, the authority of a thousand is not worth the humble reasoning of a single individual. Galileo Galilei, Italian Physicist
 
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