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Did Faulty Welds Cause Pipeline Explosion?

Posted February 18, 2011 8:00 AM

The aging infrastructure of U.S. gas pipelines is rapidly approaching the 100 year mark in some locations. All together, According to NTSB's report, faulty welds and not meeting weld standards in the 1950's installation were identified. Another gas main explosion in Philadelphia is also being investigated. Now experts are trying to figure out what caused the explosion in Allentown, PA where a 12-in. diameter cast iron gas main — installed in 1928 with no shut off valves then required — apparently ruptured. Considering the 2.5 million miles of liquid and gas pipelines in the country, what do you think could be done to avert recurrences?

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Re: Did Faulty Welds Cause Pipeline Explosion?

02/18/2011 11:19 PM

Below is an exchange between me, a retired Steamfitter Instrument Tech, and a genuine Moon Shot Scientist, a PhD in the relevant area. We advocate two improvements in pipeline safety. I would install rupture discs at each end of each pipeline segment, and Doctor Liu would use precision meters, developed for space, to detect leaks by mass balance. The long seam that opened up was an awful weld, but if the control systems are not improved, we will continue to have Colonial, Bellingham, and San Bruno type incidents. Each of these, and many more I am sure, arose through design, operation or maintenance faults in the system controlling the valves on the pipeline. If, as is reported in the news, new regulations require automatic or even remote operating valves, the communication links are an added vulnerability. Bob Woolery, DC stateoftheartchiro.com miraclechiro.com 326 deAnza dr. Vallejo, CA 94589 707 557 5471 -------------------------------------------------------------------------------- From: safepipelines@yahoogroups.com [mailto:safepipelines@yahoogroups.com] On Behalf Of zumath@aol.com Sent: Tuesday, February 01, 2011 8:05 PM To: safepipelines@yahoogroups.com Subject: Re: [safepipelines] Bad design and slow instruments were important in San Bru... In shock tube experiments, the amplitude of the shock wave can be up to 10x that of the upstream pressure, and are typically of only several milliseconds duration before equilibration begins to take place. Pressure shock waves are typically studied in detonation/deflagration experiments. A great deal of research into the effects of pressure shock waves was done back in the days of the "cold war," typically using high response quartz pressure transducers with "Transductron" type electronic data recovery systems, which attempted to reconstruct the pressure wave by solving a second order differential equation for the change of the pressure using analog circuitry. An classical example of the devastating effect of gaseous shock waves precipitated the demise of natural gas vehicle (NGV) programs at SoCalGas. A naive mechanical engineer with no real experience in fluid mechanics nor thermophysics was put in charge of the refueling station program. He implemented the three bank rapid fill cascade using fast opening solenoid valves. This essentially subjected the fiber wound tanks to three "hits" as the cascade valves were opened. When I pointed out the shock wave problem to him, he was incredulous, even though I showed him a very specific "thou shalt not use fast opening valves at high pressure differentials" statement in the Air Force Design Handbook "System Safety," stating that their pressure gauges showed no such phenomena... Well, a receiving tank failure on an RTD bus subsequently occurred at the RTD depot during refueling, blowing up the entire bus. The RTD Citizens Advisory Committee requested my testimony as an "expert witness" at the hearing on the accident. I read excerpts out of not only the USAF Design Handbook, but also several textbooks on compressible fluid dynamics -- yet the SoCalGas engineer continued to maintain that "That's only Dr. Liu's theory..." However, SoCalGas -- clearly a "deep pockets" organization -- subsequently withdrew as the lead organization for promoting NGVs. This eventually led to the discontinuation of factory NGV programs by all of the USA manufacturers... All because one naive "engineer" wouldn't go to the trouble of implementing compressed gas fueling cascades using controlled opening valves to ramp up the flowrate into vehicle receiving tanks... I personally still believe that NGVs have great potential, given our abundant supplies of natural gas -- if fueling is properly implemented. However, here we have seen the devastating effects of sudden pressure spikes in compressible media. In a message dated 1/31/2011 7:19:30 P.M. Pacific Standard Time, drbob@comcast.net writes: The pressure spike that was the proximate cause of the rupture was likely a great deal higher than the 386 psi reported, apparently by PG&E. Remember that the precipitating event was a UPS failure which allowed a pressure regulating valve feeding from an unspecified higher pressure to flop open. The sudden change in flow caused a shock wave to run down the pipeline until it found the defective long seam. The peak pressure of this shock wave could well have been higher even than the pressure in the transmission line feeding the valve. The instruments used to monitor pressure in these applications cannot detect fast transients. An industry workhorse, the Rosemont 3051 pressure transmitter specifies a minimum of 100 milliseconds to register a full scale change of pressure. Recorders, still mostly recording on rolls of paper, are even slower. The design of the control loop for the regulating valve was faulty. Such valves can be configured for various responses to a loss of power and/or air pressure. They can be set up to open, close, or stick where they are in the event of a supply loss. Clearly, the valve in question was set up to open on power failure. This is a major design error. It is truly a surprise that there were not storage batteries on the 24 volt instrumentation supply, but it may be that it was exactly this feature of the system that was being worked on. Events of this nature can be protected against, but regulatory agencies have not required the installation of the appropriate protective devices. The spikes from rapid valve opening are too fast to control with mechanical pressure relief valves, but several manufacturers offer rupture discs, precision "fuses" that can positively insure that the pressure in the pipeline NEVER exceeds the specified pressure. I would require the installation of such a device at each end of each pipeline segment, guaranteed to open at a pressure no greater than the qualifying hydrotest pressure. Provision for these could be made when installing pig traps and hydrotesting. I am a retired Steamfitter instrumentation technician, with some engineering background. I grew up in a trailer house with my father, a specialist in welding on these large diameter gas pipelines and organizer for the Pipeliner's union. I have retrained as an upper cervical Chiropractor, but continue to be interested in pipeline issues. For a better credentialed source, contact Arnold Liu, zumath@aol.com. He is a bona fide PhD rocket scientist, responsible for the successful metering of fuel in the moon landings. We have been in contact on the safepipelines discussion list, and he has given his permission to make referrals such as this. Please stay on this story, as around half the pipelines in the US are from before 1950 or of unknown age, and the hazards are real. The design and operations issues uncovered here are even more important than this particular long seam failure, tragedy though it was.

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#2
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Re: Did Faulty Welds Cause Pipeline Explosion?

02/19/2011 12:23 AM

Thank you for bringing this out. I am not very familiar with fast-transient conditions in gas pipelines, but in two-phase flows such as steam and refrigerants, there can be vapor-propelled liquid, collapsing condensation, and similar effects with high dP/dt. These may not be seen at the time on gauges or other instrumentation, but after the fact gauges are sometimes "pegged" past the end pin. Hammering noises are another clue, but maybe not audible in buried pipelines.

Some strategies to avoid problems include proper grading, condensate drainage, slow-acting valves, pipeline heating, and pressure relief schemes.

(I regret to say that I have already argued with some gross naifs on CR4 about such matters.)

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Re: Did Faulty Welds Cause Pipeline Explosion?

02/20/2011 9:35 PM

Thanks for the comprehensive response. Clearly this is NOT simply an "old infrastructure- ya shoulda fixed it!" problem. To be specific : Are you saying that rupture discs at each end of a segment PLUS a regulatory requirement for functional control loops and for backup electrical supply (batteries) will eliminate the need for SLOW-OPENING VALVES?

Much of your posting was background ...and greatly appreciated too... but I was left a little uncertain whether you think the rupture disc plus correct design of control loops and elec supply backup will be a sufficient approach.

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Re: Did Faulty Welds Cause Pipeline Explosion?

02/20/2011 10:41 PM

Not exactly. The point here is that the system should be fail safe. Setting up local control loops such as the regulator valve in Milpitas appropriately, fail open, fail closed, or stick on loss of power is one change needed. Battery backup was apparently there, but got disabled by a maintenance error. Rupture discs are not intended to ever open. But if they do, the failure happens at a known point, and the contents can be vented / flared there. A rupture disc made to burst at the full highest recent hydrotest pressure guarantees that the line never sees more than that, even for an instant. Controlled valve opening time is worthwhile, as is improved operator training. Rupture discs are fast acting (much faster than relief valves), and provide positive assurance of the maximum pressure the pipe will ever see. Thinking about it, I wonder why insurance companies have not forced such a change years ago.

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Re: Did Faulty Welds Cause Pipeline Explosion?

02/20/2011 5:22 PM

Not expect things to last forever?

Spend a portion of profit on refurbishment of plant?

Realise what materials and fabrication suit what application?

Or - Who Would Have Thought a;

"12-in. diameter cast iron gas main — installed 83 years ago, with no shut off valves upgrades, would rupture."

Duh

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