Friday, April 17, 2009

TROUBLESHOOTING FEEDWATER HEATER DRAIN COOLER PROBLEMS

Recently a Client called to ask what might be the cause of loud noises coming from the vicinity of the Subcooler in a Closed Feedwater Heater. Here is a summary of the possible causes and actions the plant may take to deal with the problem:


CAUSES














  • Tubes passing through the endplate of the subcooler are not expanded tightly in place to allow them to expand and contract axially as the heater works. The annular space between the tubes and the holes in the endplate will allow steam to intrude into the subcooler if the tube surface contained within the endplate is insufficient. In some very old Closed Feedwater Heaters, the subcooler end plate is too thin (less than 3-inches thick) to condense steam that passes around the annuli. Consequently, when there is sufficient pressure differential between the condensing zone and the subcooling zone, uncondensed, wet steam will enter the Subcooler. The wet steam erodes the cross-flow baffles, especially in the vicinity of the tube holes. As the tube holes enlarge due to the erosion, the effect is to significantly increase unsupported the tube span, making the tubes more vulnerable to vibration and subsequent failure. As the tube holes enlarge due to the erosion, of the tubes making the tubes more vulnerable are subject to vibration and subsequent failure. Current practice is to specify a minimum of 3-inch thick end plates as shown in the figure and modest pressure drops across the end plate. It might seem to be reasonable to plug tubes as they begin to leak. But this is self-defeating because doing so does not allow for cooling/condensing any steam passing through the annuli. A better way to deal with this problem is to fix it as shown below in Fixes. As shown in the sketch, the clearance between the tube and hole is ~0.0045-inch. We recommend holding all end plate drilling to the TEMA Special Close Fit Tolerances with no exceptions for out of tolerance holes that the TEMA Standards allow for drilling tubesheets (4% oversize).


  • The welds of the Subcooler shell to the flat roof plate have failed as shown in the photograph.
















                  • The welds of the Subcooler to the back face of the tubesheet have failed.

                  • Purchasers can avoid failed weld problems by specifying in their procurement specification that all welds of the Subcooler enclosure to the roof plate and to the back face of the tubesheet must be full penetration welds, are fluid penetrant examined and that the Manufacturer perform a standing water test on the enclosure to verify that the welds are intact.
                  FIXES

                  1. Fix the problem with thin end plates by having the tubes expanded into the end plate so they just contact the hole interiors, thereby reducing the volume of steam that can pass between the tubes and hole.
                  2. Fix the problem with failed longitudinal welds by cutting a window in the shell of sufficient size to expose the whole roof plate-to-closure weld. Grind out the failed weld. Attach clamps to pull the roof plate to contact with the enclosure, reweld and examine the weld with fluid penetrant. Replace the removed section in the shell and hydrostatically test. Note that this kind of repair meets the National Board Inspection Code (NBIC) requirements for repairs. Most jurisdictions require such work to be performed only by Repair Organizations that possess the NBIC-issued R Symbol stamp and Certificate of Authorization.
                  3. Attempts to fix the problem of failed Subcooler enclosures to tubesheets have not bee successful. Various schemes have been tried, including injecting sealants at the position of the failed welds. But to our knowledge, none have been successful. We recommend replacing the heater, or in the case of a heater installed in the condenser neck, replacing the bundle and channel.

                  COMMENT

                  It goes without saying that careful and proper level control is the best way to operate Closed Feedwater Heaters. Improper or inadequate level control can also lead to Subcooler problems. But this Technical Tip does not address such problems.

                  Wednesday, April 8, 2009

                  ON HYDROSTATIC TESTING HEAT EXCHANGERS

                  In October 2008 I submitted my paper, “On Hydrostatic Testing Heat Exchangers” to the Journal of Pressure Technology. The ASME has assigned PVT-8-1122 to the paper during consideration of acceptance and peer review if accepted for publication. As of this date, the Journal has taken no action and has neither accepted or rejected the paper.

                  The paper is important for Users, Manufacturers and Designers of shell-and-tube heat exchangers in which leakage from the channel side to the shell side is not visible, such as might take place through faulty tube-to-tubesheet joints in fixed tubesheet exchangers or in designs in which the tubesheet is welded to the shell. The current industrywide method for determining if such leaks occur during hydrostatic pressure testing is by monitoring the test gages for declines in tubeside pressure during the hydrostatic pressure holding period.

                  The paper demonstrates that the current method is flawed because the insensitivity of the pressure testing equipment is such that it cannot disclose small leaks of tubeside fluid into the shell that can lead to catastrophic events.

                  My position that the ASME Code should require other means, such as leak testing beyond the Code-required hydrostatic testing, to disclose such leaks is controversial. Many of my colleagues hold the opinion that the current practice is adequate providing that Users make Designers and Manufacturers aware of hazards that small leaks might create. My experience is that Users do not always provide such information to Designers and Manufacturers during the bidding stage. None of the many procurement specifications I have reviewed addressed this problem.

                  If the reviewers at the Journal of Pressure Technology reject the paper, I will publish it in its entirety on this blogsite.

                  Here is the abstract of this paper.

                  ABSTRACT

                  This paper discusses the requirements of Section VIII Division 1 of the ASME Boiler and Pressure Vessel Code (the Code) for hydrostatically testing shell-and-tube heat exchangers. It uses an approximate calculation method to delmostrate that the common practice of using pressure gage indications of pressure loss to determine if there is a leak from the tube side to the shell side when the back face of the tubesheet is not visible is flawed and does not meet the basic no-leak requirement of the Code.

                  I would appreciate any comments that readers of this blog would care to submit with respect to hydrostating shell-and-tube exchangers in which leakage from the channel side to the shellside is not visible during testing.

                  Sunday, March 1, 2009

                  MGT Inc.'s Courses and Course Notes

                  MGT Inc. now has available for sale CDs with Power Point Presentations of our following copyrighted courses:

                  Closed Feedwater Heaters - Mechanical Aspects

                  Power Plant Auxiliary Heat Exchangers

                  Shell-and-Tube Heat Exchangers - Mechanical Aspects

                  The price of each CD F.O.B. Boulder, Colorado is US$1,500.

                  For purchasers with WebCams, we offer up to four hours of telephone discussions using Skype.

                  For futher information call Stanley Yokell, P.E., Fellow of the ASME at 303-494-9608, or email him at syokell@mgt-inc.com.

                  Tuesday, February 3, 2009

                  Stan Yokell's book Dog Stories is now Available for Purchase


                  Dog Stories Book is now Available for Purchase !!!

                  Soft and hard cover editions of Dog Stories are now available for purchase.
                  ISBN: Hardcover 978-1-4363-9830-5
                  Price: $24.99
                  ISBN: Softcover 978-1-4363-9830-9
                  Price:$15.99
                  To order copies of this book, contactXlibris Corporation1-888-795-4274
                  Order from these organizations:

                  Friday, January 30, 2009

                  The 2009 Update of the Closed Feedwater Heater Suite is now Available

                  The updated version of the MGT Inc. Closed Feedwater Suite is now available. The suite consists of a CD with an MSWord Generic Procurement Specification for procuring new and replacement closed feedwater heaters and replacement bundles, PDF versions of Guide to Plugging Feedwater Heaters, Specification for Performing Feedwater Heater Autopsies and Xcel Spreadsheets for estimating the thermal and pressure drop effects of sleeving feedwater heater tubes.

                  The current price, F.O.B Boulder, Colorado is US$325 plus shipping and handling. Orders will be shipped within two business days. Payment by check only.

                  Saturday, January 17, 2009

                  Carl Andreone's Unavailability

                  Carl Andreone is currently unavailable. Viewers should address communications to Stanley Yokell until further notice.

                  Sunday, January 11, 2009

                  On Hydrostatic Testing Heat Exchangers

                  Viewers of this blog are advised that I have submitted a paper to the ASME's Journal of Pressure Technology dealing with hydrostatic testing of shell-and-tube heat exchangers. As of today, the paper has neither been accepted nor rejected. If I am notified that it is not accepted for publication in the Journal, I will publish it on this blog. Following are the title and paper number along with the abstract of the paper.

                  ON HYDROSTATIC TESTING HEAT EXCHANGERS PVT-08-1122

                  ABSTRACT


                  This paper discusses the requirements of Section VIII Division 1 of the ASME Boiler and Pressure Vessel Code (the Code) for hydrostatically testing shell-and-tube heat exchangers. It uses an approximate calculation method to demonstrate that the common practice of using pressure gage indications of pressure loss to determine if there is a leak from the tube side to the shell side when the back face of the tubesheet is not visible is flawed and does not meet the basic no leak requirement of the Code.