NOTICE

Forums are temporarily disabled while we are working on a new login procedure.

When migrating the old forums over to our new forums we were unable to retain the identity of the authors, so the old posts will show up as "anonymous". All NEW posts will show up credited to their authors. So please participate and share knowledge just as you have in the past.

You must log in if you are an existing user or register if you are a new user in order to contribute to the discussions.

Discussion Forums - The Hendrix Group
HomeHomeDiscussionsDiscussionsOil Refinery Co...Oil Refinery Co...Nitrogen corrosion or wrong design?Nitrogen corrosion or wrong design?
Previous
 
Next
New Post
7/17/2007 9:00 AM
 
Dear All, A convection heater runs in on/off mode (1hr on/4 hr shut). Gas temperature at bridge wall is 1350F. Unfortunately, during the runs the recirculation damper had broken and very little flow passed thru (this is can be shown from the chamber temprature profile) and at this time the temperature controller did not alarm because it has not been set up for K type thermocouple. (originally J type mode). Eventually, chamber temparature got higher and damaged the first row P11 finned pipe and the tubesheet. Tubes are connecting to a header also. And there are 3 tubesheets, centered and end tubesheets. Normally coil design for 1550F max. But with above senario the tubes at first row snapped. The employees blame the design and complains about tubesheets design and expansion values wrong. Others think about this is happened becuase of damper (data history shows it.) So did anyone comeacross this kind of problem? Becuase of high temperature right around (1203 thru 1582 max tmt and 1203 thru1780 fin tip max metal temp.) cause to intergranular corrosion and lets holes on the pipe and the nitrogen during the cool down period gets in the chamber and thermally damaged the tubes??? and SS 304 tubesheet good enaough for thisconditions? Thanks for input in advance.
 
New Post
7/18/2007 9:00 AM
 
From my point of view for the intermittent working condition of your heater, P11 is not a good material which doesn%E2%80™t withstand sudden forced rapid cooling. P11 when subjected to rapid cooling tends to form martensitic structures which are very brittle. Also at 843%C2ºC your temperatures SS 304 tube sheets and tubes are intermittently subjected and stressed to very different thermal expansion. SS 304 in your working conditions tends to form Sigma phase during the heating and cooling. Sigma phase is a non-magnetic intermetallic phase composed mainly of iron and chromium which forms in ferritic and austenitic stainless steels during exposure at 560%C2º-980%C2ºC (1,050%C2º-1,800%C2ºF). It causes loss of ductility, toughness and is generally strain intolerant at temperatures under 120%C2º-150%C2ºC (250%C2º-300%C2ºF) which in your case is your cyclic cooling and heating conditions. It is possible that your damper failure has also contributed to the damaged. My advice is that you should discuss with the designer of your heater in the sense of reviewing tube and tube sheet materials for on/off mode runs (1hr/4hr shut). Good luck Luis Marques
 
New Post
7/19/2007 9:00 AM
 
Thank you very much for your response. I am sure I will get back to you with questions. Thanks again,
 
New Post
7/19/2007 9:00 AM
 
Paul / Luis Luis's observations on P 11 behaviour when subjected to rapid cyclic heating and cooling may be relevant to some extent. P 11 has an inherent characteristics of "temper embrittlement" in cyclic heating and cooling. If that is taken care, by careful slow heating after a shut down cracking problem may not persist . Besides this, P 11 is not meant for a continuous service duty of > 450 deg cent. From the description of what was explained in Paul's question, the coil was subjected to higher temperature excursions - which may be detrimental to P11's performance. SS 304 was also subjected to a sudden cyclic temperature excursion of 800+ deg centigrade. Even SS 304 tube sheet cannot stand this high temperature excursion / variations even for a short duration. To me, it appears the basic problem lies in damper failure. With damper failure chances of some run away temperature excursion in both P 11 tube, P 11 header and in SS 304 tube sheet are always possible. For damper to fail, Paul's operation personnel should look into any operational miss for the heater coil failure. For possible run away heating and cooling, like what was described, Paul may have to look from design improvements with material improvement combined - if needed. Problem is : compounded by operational failure combined with material failure. Both needs improvement - from my view of this problem Trust this will help to solve C.V.Srinivasan Nishi Engineers Pvt Ltd India July 20,2007 E-mail: nishi@vsnl.com >From my point of view for the intermittent working condition >of your heater, P11 is not a good material which doesn%E2%80™t >withstand sudden forced rapid cooling. P11 when subjected to >rapid cooling tends to form martensitic structures which are >very brittle. Also at 843%C2ºC your temperatures SS 304 tube >sheets and tubes are intermittently subjected and stressed >to very different thermal expansion. SS 304 in your working >conditions tends to form Sigma phase during the heating and >cooling. Sigma phase is a non-magnetic intermetallic phase >composed mainly of iron and chromium which forms in ferritic >and austenitic stainless steels during exposure at >560%C2º-980%C2ºC (1,050%C2º-1,800%C2ºF). It causes loss of >ductility, toughness and is generally strain intolerant at >temperatures under 120%C2º-150%C2ºC (250%C2º-300%C2ºF) which in your >case is your cyclic cooling and heating conditions. It is >possible that your damper failure has also contributed to >the damaged. My advice is that you should discuss with the >designer of your heater in the sense of reviewing tube and >tube sheet materials for on/off mode runs (1hr/4hr shut). > >Good luck > >Luis Marques
 
Previous
 
Next
HomeHomeDiscussionsDiscussionsOil Refinery Co...Oil Refinery Co...Nitrogen corrosion or wrong design?Nitrogen corrosion or wrong design?


  

News

With a little delay, our Calculation of Ammonium Salt Deposition Temperatures...read more
Our sulfidic corrosion calculators are now available at hghouston.com/calcula...read more

Stay Current

Sign up for our quarterly newsletter

covering updates on corrosion

Sign Up