RiTech® hard coating is a high-velocity oxygen fuel coating process using a hot, high-velocity gas jet to spray a coating of molten particles on to the ball and seat surfaces.
History shows us that valve failures can be catastrophic. Although it occurred in 2010, the effects of the Deepwater Horizon disaster can still be felt on the Gulf Coast and in the courts. From April to July of that year, engineers were scrambling to stop the hundreds of millions of gallons of crude being released into the Gulf of Mexico after the blowout preventer (BOP) on the rig failed to seal the pipe. Of course, major disasters are typically preceded by known, but uncorrected errors, and this was not the first time a company had trouble with isolation valves. As The Washington Post reported in June 2010, an operational integrity report written in 2001 covering the operations found that, “workers believe internal leak-through of isolation valves is a significant problem and under certain circumstances may pose a potential hazard to workers and equipment.” butterfly valve pn10
Such incidents attract a lot of attention, but most leaks are well hidden somewhere deep inside the equipment and piping covering the grounds of a power plant. These valves gradually eat away at performance and profits, a problem that is particularly critical with severe service isolation valves (SSIV). These issues, though, are preventable by using properly designed valves that allow zero leakage. The problem is that “zero-leakage” does not always mean zero-leakage. The usual definition actually means acceptably slow leakage internally, with no visible external leakage. But by applying best available technology and adopting new standards, zero can equal zero, both internally and externally.
SSIVs are isolation valves that are used in high energy conditions at elevated temperatures, and pressures. They are used for numerous applications throughout power plants. These temperatures and pressures exceed the normal operational limits of thermoplastic seals, so the seal needs to be made by the metal components of the valve. There are also challenges the performance of commonly used and industry accepted hard facing materials utilized in high pressure and temperature valve seats. Further complicating the matter, the fluids involved may contain some solid content or abrasive materials that erode the seal surfaces, thereby producing leakage paths.
With SSIVs, the cost of the leakage is far greater than the cost of the valve. High temperatures and pressures coupled with erosive substances entrained in the fluid means that even minor leaks can grow into major ones. This results in unscheduled shutdowns and frequent equipment repair or replacement as well as wasted fuel/process liquids. To protect people from injury and equipment from damage, it is essential to achieve zero-leakage with SSIVs.
Like other valves, leakage can be either internal or external. It isn’t difficult to discover external leakage: you can see the cloud of steam escaping, for instance. Internal leaks, however, are entirely different. Take an isolation valve on a bypass line between the boiler and the steam turbine that redirects steam to the condenser. Any leakage though that SSIV lowers generator output while increasing fuel consumption. Since leakage is internal, it may only show up as a gradually increasing heat rate, requiring additional fuel expenditures and accompanying emissions remediation expenses to produce the same amount of electricity. The cost of replacing a faulty valve, on the other hand, is minimal compared to the lost output.
Keep in mind that there can be hundreds of SSIVs in a power plant. The overall losses are not from a single leaky valve, but the aggregate losses from each of them leaking a tiny amount. Together they add up to millions of BTUs never reaching the turbines. Zero-leakage SSIVs can typically improve a plant’s heat rate performance from 1-2 percent to as high as 3 percent.
To understand the order of magnitude of the losses, consider an industry accepted value of 2 percent in heat rate (efficiency) loss attributable to cycle isolation or passing isolation valves and assume a 300 MWe steam turbine generator.
Further assuming that this turbine generator operates 8000 hours per year at a round-the-clock average wholesale price of electricity of $50/MWh, the resulting loss in profit is $2.4 million per year.
While all valve losses ultimately affect the steam cycle efficiency, the overwhelming majority of the total loss will result from the high energy, sever services such as main steam or high pressure steam, hot reheat, cold reheat and the associated boiler or heat recovery steam generator sections. These high energy systems have the most impact on the output capacity.
Finally, by employing state-of-the-art valve seat leakage diagnostics, the target list of impactful valves can be reduced to the worst of the worst performers. Experience has repeatedly shown that the higher value targets yield paybacks on total replacement cost in the order of a couple of months or less. In any event, the cost of mitigating or eliminating valve leakage is tiny relative to the annual recurring losses which result from poorly performing valves in severe service.
The losses cited above may seem extreme at first glance, but is validated by other well-established research in areas such as leakage through an orifice in a pressurized pipeline, as well as heat and pressure losses in steam traps. Per the ANSI/FCI 70-2 leakage specification, a Class V valve should have a maximum seat leakage of 5 x 10-4 ml per minute of water per inch of seat diameter per psi differential (5 x 10-12 m3 per second of water per mm of seat diameter per bar differential). Buying Class V valves, therefore, would seem to eliminate the leakage losses. However, those standards apply only at the point of installation. Over time, the continuous steam leakage past the plug seat erodes the seal, causing steam cutting and wire drawing. What was once a Class V valve evolves into a Class IV, then Class III, Class II or worse. To try to seal against the high pressures (a two inch ANSI 4500 globe valve is subject to up to 19,623 pounds of force), a hammer-blow handwheel is sometime used. This method uses up to 10 times greater torque to drive the plug against the seat, but the method can damage the valve parts and won’t stop leakage through an eroded seal. Additional damage comes from vibration, flashing, cavitation and internal erosion.
Just as utilities must apply Best Available Control Technologies to eliminate excess emissions, so should they adopt Best Available Isolation Technology (BAIT®) design features to eliminate the problem of erosion and gradually rising losses. Here, for example are some of the elements that make up BAIT® for ball valves:
Adopting BAIT® makes it possible to actually achieve absolute zero-leakage on SSIV. Therefore, is it time for a new valve classification that goes beyond the FCI 70-2 Class VI standard? Introducing a “Class VII” would be zero-visible leakage for a minimum three minutes hydro test and gas test. It’s real, it is very achievable and is standard operating procedure for every valve manufactured at ValvTechnologies.
With this new standard, zero means zero, not something that we hope comes pretty close.
double eccentric butterfly valve Kevin Hunt is president of ValvTechnologies