ryu.changmyong
Mechanical
- Apr 19, 2017
- 19
Dear ALL,pls let me ask you some technical advice for tube failure in Heat exchanger
as shown on attached Tube failure status.
Since Heat Exchanger operation in 2001 year, for 15 years
Tube failure occurred in drain outlet where located between
Tube sheet and 2ND baffle at 3, 4 pass area particularly
as much as 8~10 tube leakage yearly.
Currently total Tube Plugged q'ty is 127 of 932 tubes.
this is issue why this area damaged rather than other zone.
at the moment, this is related to operating level of condensate water
due to corrosion compound when chemical cleaning.
1. Tube OD 19.05, thk 1.65mm
2. Shell Side Flash Vapor : 0.3% of Terephthalic Acid contained Water,Condensate water pH 3.8
3. Tube side : Reactor Feed
4. Material : Shell-SS304L, Tube-SS316L
5. Tube side Pass ; 4 pass
6. Tube failure major status : Founded Pitting and Crack assumed by SCC (Stress and Corrosion Cracking)
at tube outside surface. For more information, refer to Lab inspection data as attached file.
Lab inspection report for sample tube say as follows.
1. Major damage : Pitting and Stress Corrosion Cracking
2. Tube surface crack into tube inside : 1.1mm and growing slowly
3. Most damage area : It occured at back side of Tube sheet (2ND baffle area)
in 3 pass and 4 Pass zone in a length of 600mm.
Also,Scale cluster founded this area.
4. It founded S,Cl,Na at damage tube as corrosion factor. Chloride 0.75~0.99Wt%
Could you advise me of your technical opinion in this regard.
Ryu Changmyong/P.E
as shown on attached Tube failure status.
Since Heat Exchanger operation in 2001 year, for 15 years
Tube failure occurred in drain outlet where located between
Tube sheet and 2ND baffle at 3, 4 pass area particularly
as much as 8~10 tube leakage yearly.
Currently total Tube Plugged q'ty is 127 of 932 tubes.
this is issue why this area damaged rather than other zone.
at the moment, this is related to operating level of condensate water
due to corrosion compound when chemical cleaning.
1. Tube OD 19.05, thk 1.65mm
2. Shell Side Flash Vapor : 0.3% of Terephthalic Acid contained Water,Condensate water pH 3.8
3. Tube side : Reactor Feed
4. Material : Shell-SS304L, Tube-SS316L
5. Tube side Pass ; 4 pass
6. Tube failure major status : Founded Pitting and Crack assumed by SCC (Stress and Corrosion Cracking)
at tube outside surface. For more information, refer to Lab inspection data as attached file.
Lab inspection report for sample tube say as follows.
1. Major damage : Pitting and Stress Corrosion Cracking
2. Tube surface crack into tube inside : 1.1mm and growing slowly
3. Most damage area : It occured at back side of Tube sheet (2ND baffle area)
in 3 pass and 4 Pass zone in a length of 600mm.
Also,Scale cluster founded this area.
4. It founded S,Cl,Na at damage tube as corrosion factor. Chloride 0.75~0.99Wt%
Could you advise me of your technical opinion in this regard.
Ryu Changmyong/P.E