The half-day “HRSG Spotlight” session that HRST Inc, Eden Prairie, Minn, has conducted in conjunction with the 7F meeting for the last several years is designed for plant personnel who want a refresher on heat-recovery steam generators and an update on industry concerns with large triple-pressure units.
Focus of the 2012 workshop was fatigue cracking, with Amy Sieben, PE, presenting on failures in superheater/reheaters and panelized economizers, and Scott Wambeke, PE, addressing drum-nozzle cracking and fatigue in return-bend economizers. Sieben opened the session by saying that fatigue cracking is one of five mechanisms that account for more 90% of all pressure-part failures suffered by HRSGs. The others are flow-accelerated corrosion (FAC), corrosion fatigue, chemical attack/under-deposit corrosion, and dew-point corrosion.
Fatigue cracking occurs, she said, when material is repeatedly stressed beyond its yield point. Low-cycle fatigue is the term used to describe fatigue failures that occur in fewer than 1000 cycles. Sieben introduced an important term into the lexicon of many attendees when she stressed the importance of managing the HRSG’s “fatigue bank account.” Fatigue cracking can initiate on the inside or outside surfaces of pressure parts, the boiler designer continued, noting the three components of fatigue: pressure, temperature, and external piping stress.
Fatigue cracking in superheaters (reheaters). Tube-to-tube temperature differences cause cracking in superheater (reheater) panels for two primary reasons:
• Condensate blockage and poor drain design. Inability to remove condensate in timely fashion during/following a unit purge often is traced to undersize, ganged, or closed drains.
• Water introduced through interstage desuperheaters, which are located between the primary and secondary superheaters and reheaters. Typical causes include leaking spray-water supply valves, hunting, poor piping arrangements, overspray, and a primary/secondary superheater (or reheater) surface arrangement that is incompatible with a given turbine’s performance at startup or low load.
Note that attemperators sometimes are installed downstream of the final superheater or reheater surface in lieu of, or in conjunction with, an interstage desuperheater. Two concerns shared by owner/operators regarding the use of “downstream” attemperators: (1) Additional cost and (2) the risk of steam turbine damage in the event of a failure. A couple of slides illustrated for first timers the two basic types of desuperheaters used in HRSGs: (1) Probe style with single or multi-nozzle axial injection and single or multi-nozzle radial injection. Reported advantages of the latter are that spray nozzles are not in the steam path and steam/water mixing generally is more efficient than with the probe style attemperator. For more on the subject, access “Avoid desuperheater problems with quality equipment, proper installation, tight process control” by HRST’s Scott Wambeke.
Sieben then expanded her coverage of the two bullet points above. She began with a few photos and drawings illustrating how humping of lower headers equipped only with center drains can allow condensate to block tubes at the ends of superheater and reheater panels and cause buckling of those tubes. Having multiple drain locations is one way to solve this problem. Discussion of the dos and don’ts of drain system design came next. Here are the important take-aways:
• Purge condensate from lower headers before every start. Automatic valves are needed to do this effectively.
• Drain condensate as it forms during the gas-turbine purge cycle.
• Proper sizing of drains is critical. Keep in mind that drains too large or too small can be problematic.
• Locate blowdown tanks below header drain locations.
• Avoid combining drains (Fig 1). Be especially careful not to interconnect drains operating at different pressures: The higher pressure drain can block condensate flow from the lower-pressure line. More on drains at “Incorporate lessons learned into specifications for new units” and “Learn the basics of HRSG inspection.”
 1. Poorly designed drain arrangement has manually operated under-size drain lines and multiple drains ganged together |
Sieben next noted that a proper drain must allow for a full range of motion between the penetration seal and the access hole in the HRSG casing. Differential expansion between ganged panels amplifies drain lateral displacement, she said, illustrating the point with Fig 2. Drains that collide with the floor liner or casing often suffer stress-induced cracking (Fig 3).
 2. Differential expansion amplifies drain lateral displacement |
 3. Drains that collide with the floor liner or casing often suffer stress-induced cracking |
Ineffective draining of cold reheat lines, and occasionally main steam piping, also is conducive to damage. Sieben spoke about water hammer resulting from a slug of condensate being pushed through steam piping during startup. Typically, she said, pipe supports are bent, or thrown out of position; piping may be damaged as well. Tube damage is a possibility, too, if a slug of water reaches the HRSG. Sieben offered a checklist on how to avoid water hammer:
• Drain steam piping before every gas-turbine start. Best practice: Automate valves and install condensate detection for added protection.
• Confirm piping slope and the ability of the drain system to clear condensate from the entire line.
• Prevent the possibility of water accumulation upstream of valves—especially the steam-turbine bypass.
• Tightly control bypass/letdown valve attemperation.
• Check for leaking bypass attemperator spray water.
Before addressing in detail the desuperheater problems identified earlier, Sieben reminded attendees of recent (2007 and 2009) changes to the ASME Boiler & Pressure Vessel Code regarding attemperators. First, drain pots downstream of desuperheaters must be able to detect water automatically and to drain it without operator intervention. Second, superheater and reheater drains must be able to detect and drain condensate both under pressure and at atmospheric pressure.
Leakage by block and control valves usually can be prevented, Sieben added, sometimes by simply specifying class V shutoff or better. Confirm leak tightness by finding no drop in steam temperature across the desuperheater. Attemperator hunting, most common at low load, causes chronic cycling with the possibility of fatigue damage in the probe, liner, and/or piping. Hunting increases the likelihood of finding water in the superheater.
Attemperator overspray can damage superheaters and reheaters, and, in the case of desuperheaters downstream of those heat-transfer surfaces, may cause catastrophic damage to the steam turbine. More on overspray at “2011 Outage Handbook – HRSG Clinic.” Overspray usually is attributed to one or more of the following conditions:
• Poor atomization of spray water because of probe/nozzle damage or partial plugging.
• Improper piping design—in particular an insufficient straight run of pipe upstream and/or downstream of the attemperator.
• An arrangement of superheater and/or reheater surface that allows overspray to occur at some operating points (typically startup or low load) because all the water cannot be evaporated.
Sieben spent several minutes explaining the last point by way of diagrams with actual gas and steam temperatures and spray-water flow rates for varying loads both with and without supplementary firing, and for different ratios of superheater and reheater primary and secondary surface. One example presented: A superheater for an F-class HRSG designed with 60% primary surface area and 40% secondary surface area requires no spray water when operating at base load without duct burners in service, but needs 43,000 lb/hr of spray water at min load without supplemental firing. For a superheater having 70% of its surface area in the secondary bundle, 55,000 lb/hr of spray water would be required at min load without duct burners.
Correcting for overspray can be extremely challenging and expensive, Sieben continued. Options she offered included these:
• Bypass a portion of the HP saturated steam flowing from the drum to the primary superheater thereby cooling steam exiting the secondary superheater. Same logic can be applied to the reheat circuit, with some of the cold reheat steam being withdrawn ahead of the heat-transfer surface to cool hot reheat. This option is rarely practical because of the expense involved and because reducing steam flow to superheater/reheater panels can increase metal temperatures above recommended limits.
• If too much surface is installed, remove fins and/or gas baffles, or use tube shields, to reduce heat transfer.
• Add a final attemperator or an additional interstage desuperheater.
• Minimize or eliminate the need for spray water on startup by installing an air attemperation system. More at “Air attemperation protects HRSGs against damage at low loads.”
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