Dr. Winfried Heimann - Fischer Group
Dr. Winfried Heimann - Fischer Group Dr. Winfried Heimann - Fischer Group
TKp
- Page 2 and 3: • Dr. Winfried Heimann • was he
- Page 4 and 5: Stainless Steel Grades for Seawater
- Page 6 and 7: Physical Properties of Stainless St
- Page 8 and 9: Corrosion Resistance of Stainless S
- Page 10 and 11: Temperature [°C] Critical Pitting
- Page 12 and 13: Influence of PRE (Pitting Resistanc
- Page 14 and 15: Corrosion Resistance of Stainless S
- Page 16 and 17: Galvanic Corrosion in Sea Water Des
- Page 18 and 19: Condenser tubes UNS S34565 TKp
- Page 20 and 21: Corrosion Tests in Simulated MSF De
- Page 22 and 23: Stainless Steel grades for Condense
- Page 24 and 25: Stainless Steel thin walled Tubes f
- Page 26 and 27: Stainless Steels in the Sea-Water-D
- Page 28 and 29: MSF and MED condenser tubing Histor
TKp
• <strong>Dr</strong>. <strong>Winfried</strong> <strong>Heimann</strong><br />
• was heading varios division of R+D, quality control and application engineering in Thyssen Edelstahlwerke and<br />
ThyssenKrupp Nirosta<br />
• was being Senior Manager with Outokumpu Stainless<br />
• after retirement he is acting as Consultant in this field<br />
• Christian Behrle<br />
• is heading the Technical Department for R+D in <strong>Fischer</strong>-group<br />
• specialised in SS-tubes for desalinations<br />
• DME – Member of the Board<br />
• Member of IDA<br />
• Member of EDS<br />
TKp
Corrosion Resistance<br />
Typical Relation of Corrosion Resistance und Mechanical<br />
Strength of some Stainless Steel Grades<br />
Austenitic grades<br />
1.4539<br />
1.4404<br />
1.4547<br />
1.4565<br />
1.4521<br />
1.4362<br />
1.4162<br />
Superferritic grades<br />
28 Cr<br />
+ Mo<br />
+ Ni<br />
1.4410<br />
Ferritic grades<br />
Mechanical Strength<br />
Ferritic-Austenitic<br />
(Duplex)-Grades<br />
TKp
Stainless Steel Grades for Seawater Desalination Plants<br />
EN<br />
10088<br />
ASTM<br />
A 240<br />
Cr<br />
%<br />
Ni<br />
%<br />
Mo<br />
%<br />
Others PRE 1<br />
1.4162 S32101 21 1,5 0,3 N 26 19<br />
1.4362 S32304 23 4,8 0,3 N 26 25<br />
1.4410 S32750 25 7 4,0 N 43 85<br />
1.4521 S44400 18 87<br />
1 PRE= %Cr + 3,3%Mo + 16x%N (Pitting Resistance Equivalent)<br />
2 Critical Pitting Temperature acc. ASTM G 150<br />
Duplex stainless steel grades Austenitic stainless steel grades<br />
Ferritic stainless steel grades<br />
CPT 2<br />
°C<br />
Ref.: Mikael Willför, Outokumpu:<br />
Materials selection for thermal plants<br />
DME-Workshop 2008, Duisburg<br />
TKp
Mechanical properties of Stainless Steel Cold rolled Strip<br />
Minimum Values<br />
EN<br />
10088<br />
ASTM<br />
A 240<br />
Yield Strength<br />
Rp0,2<br />
MPa<br />
EN(ASTM)<br />
Tensile<br />
Strength<br />
Rm<br />
MPa<br />
EN(ASTM)<br />
Elongation<br />
A5<br />
%<br />
EN(ASTM)<br />
1.4162 S32101 (530) (700) (30)<br />
1.4362 S32304 450(420) 650(600) 20(20)<br />
1.4410 S32750 550(550) 750(750) 20(15)<br />
1.4521 S44400 320(275) 420(415) 20(20)<br />
1.4404 S31603 240 530 40<br />
1.4547 S31254 320(310) 650(690) (35)<br />
1.4565 S34565 420 800 30<br />
Duplex stainless steel grades Ferritic stainless steel grades<br />
Austenitic stainless steel grades<br />
TKp
Physical Properties of Stainless Steel grades<br />
(Average values according to EN 10088 or ASTM A240)<br />
Ferritic grades<br />
17Cr 28Cr<br />
2Mo 1-4Mo<br />
0-2Ni<br />
(Superferritics)<br />
Duplex grades Austenitic grades<br />
1.4404 1.4547<br />
1.4565<br />
(Superaustenitics)<br />
Density g/cm³ 7,7 7,7 7,8 8,0 8,1<br />
Modulus of<br />
Elasticity GPa<br />
Thermal<br />
Conductivity<br />
Thermal<br />
Expansion<br />
W/mK<br />
RT - 300°C<br />
10 -6 /K<br />
Specific Heat<br />
J/kg°C<br />
220 200 200 200 195<br />
23 17,5 15 15 12<br />
11 10 14,0 17,0 16,5<br />
430 500 500 500 450<br />
TKp
Corrosion of Materials in Sea Water Desalination Plants<br />
Forms of corrosion<br />
• General corrosion<br />
• Pitting and crevice corrosion<br />
• Erosion corrosion<br />
• Galvanic corrosion<br />
TKp
Corrosion Resistance of Stainless Steel in Sea Water<br />
• Stainless Steels have negligible thinning in sea water<br />
• Chromium oxide film (passive layer) forms immediately<br />
on steel surface with exposure to air<br />
• Oxygen levels as low as 20 ppb are still sufficient to<br />
repair itself after being damaged<br />
TKp
Corrosion Resistance of Stainless Steel in Sea Water<br />
• Pitting and Crevice Corrosion<br />
• Under certain conditions the protective surface film<br />
on stainless steels can break down locally:<br />
oxyginated water<br />
high chloride<br />
too high chlorination level<br />
low pH-value<br />
pitting and crevice corrosion<br />
more resistant grade has to be selected<br />
acc. to PRE = %Cr + 3,3% Mo + 30 (16)% N<br />
ranking of alloys can be carried out<br />
TKp
Temperature [°C]<br />
Critical Pitting and Crevice Corrosion Temperatures<br />
of Stainless Steel Grades<br />
100<br />
80<br />
60<br />
40<br />
20<br />
1.4404<br />
1.4404<br />
According to ASTM G 48<br />
Pitting<br />
Crevice Corrosion<br />
1.4462<br />
1.4439<br />
1.4462<br />
1.4439<br />
1.4539<br />
1.4547<br />
1.4539<br />
1.4547<br />
1.4410<br />
1.4410<br />
1.4565<br />
0<br />
25 35 45 55<br />
PRE (%Cr + 3.3 %Mo + 30 %N)<br />
1.4565<br />
TKp
Critical Pitting Temperature of Stainless Steel Grades<br />
(Values determined according to ASTM G 150)<br />
Critical Pitting Temperature<br />
Duplex Stainless Steel Grades Austenitic Stainless Steel Grades<br />
Ref.: Outokumpu Stainless<br />
Corrosion Handbook<br />
Ninth Edition, 2004<br />
TKp
Influence of PRE (Pitting Resistance Equivalent)<br />
%Cr + 3,3x%Mo on the CPT (Critical Pitting Temperature)<br />
of welded and unwelded Stainless Steels<br />
Critical Pitting Temperature<br />
90<br />
°C<br />
80<br />
70<br />
60<br />
50<br />
40<br />
30<br />
20<br />
10<br />
unwelded<br />
TIG-welded,<br />
without filler<br />
TIG-welded,<br />
overalloyed filler<br />
(THERMANIT ® 625)<br />
Laser-welded tubes<br />
(0,3x30)mm,<br />
minimum value<br />
1.4438<br />
1.4404<br />
1.4439 1.4539<br />
1.4462<br />
1.4529<br />
0<br />
25 30 35 40<br />
PRE = % Cr + 3.3 • % Mo<br />
1.4565<br />
20 Cr / 6,6<br />
Mo<br />
Test according to ASTM G48<br />
20 Cr / 6,1 Mo<br />
TKp
Erosion Corrosion in Sea Water Desalination Plants<br />
Erosion corrosion is the most common failure, e.g. in the heat rejection<br />
• Copper alloys, brasses and bronzes are prone to impingement attack,<br />
at sea water velocities above 3m/s.<br />
• In sea water polluted with solids copper based alloys suffer<br />
severe erosion corrosion even at very low flow rates (< 0,5 m/s)<br />
• Stainless steels and especially high alloyed grades like Duplex and<br />
Superaustenitics are much better resistant to erosion corrosion than<br />
copper based alloys.<br />
There is no risk of erosion corrosion with special stainless steels<br />
at velocities up 20 m/s even up to 40 m/s with high nitrogen containing<br />
Superaustenitic steel UNS S34565.<br />
TKp
Corrosion Resistance of Stainless Steel in Sea Water<br />
• Erosion and Erosion Corrosion<br />
• The passive layer is maintained at<br />
very high flow rates and<br />
• Sea water velocities in excess of 40 m/s can<br />
be accommodated (in praxis usually below 10m/s)<br />
TKp
Corrosion rate [g/m² d]<br />
1000<br />
100<br />
10<br />
1<br />
Corrosion of Stainless Steels<br />
in Contaminated (Solids) Flowing Sea Water<br />
Ferritic Cr-Steels<br />
Duplex Stainless Steels<br />
Austenitic<br />
Mn-Steels<br />
Austenitic<br />
Steel<br />
Superaustenitic Steels<br />
UNS S34565<br />
0 20 40 60<br />
Flow velocity [m/s]<br />
TKp
Galvanic Corrosion in Sea Water Desalination Plants<br />
Multi-metal systems: Stainless steels, titanium, copper aloys<br />
• Titanium is cathodic to most of other metals.<br />
• Stainless steels are towards the more noble end of<br />
the galvanic series.<br />
• Superaustenitic stainless steels are compatible with titanium<br />
because their free corrosion potential is close together.<br />
• Galvanic corrosion occurs when using titanium or stainless steel<br />
tubing together with copper based alloy tube sheets, increasing<br />
corrosion attack to the tube sheet to a point where cathodic<br />
protection is required in the water boxes.<br />
TKp
Chlorination – Performance of Stainless Steel<br />
• Chlorination is used to control microbiological films.<br />
To prevent the build-up of biofilms and remove settled biological species.<br />
• Practice of chlorination is the addition of a hypochloride solution<br />
to the sea water<br />
• Chlorination can be either continuous or<br />
intermittent (Chlorine is added for shorter periods<br />
e.g. twice a day 15 minutes)<br />
• Chlorination level<br />
- continuous: 0,1 - 0,4 ppm<br />
- intermittent: several ppm<br />
total amount of chlorine is less than with systems<br />
using continuous systems<br />
• The objective: Keep the residual chlorine level < 0,5 ppm<br />
• Stainless steel perform well up to 2ppm<br />
TKp
Condenser tubes UNS S34565<br />
TKp
Weld shape of TIG and Laser welded Stainless Steel –<br />
thin walled tubes, welded from 1,5 mm cold rolled strip<br />
Tungsten inert gas welding - TIG<br />
Welding root sag < 0,2 mm<br />
Laser welding<br />
Welding root planed<br />
Welding root sag<br />
< 0,15 mm<br />
TKp
Corrosion Tests in Simulated MSF Desalination<br />
Plant Evironments<br />
Tests carried out by Cortest Laboratories, Sheffield<br />
Experimental Test Program<br />
Material:<br />
• UNS S34565, laser welded tube with<br />
0,35 mm wall thickness,<br />
20 mm and 30 mm diameter<br />
• UNS S31603, S31803, S32760, and S34565,<br />
plate material<br />
Test Environment:<br />
• Alloy C276 autoclave<br />
• Syntetic sea water heated to 90°C<br />
• Three oxigen levels, 750, 150, and 65 ppb<br />
Test Duration: 30 days<br />
Tube assembly specimen<br />
Methodes of joining:<br />
• Welding to the tube plate<br />
• Rolling into the tube plate<br />
Ref.: NACE Corrosion 2001, Paper No. 01484<br />
NACE Corrosion 2002, Paper No. 02190<br />
TKp
Corrosion Tests in Simulated MSF Desalination<br />
Plant Evironments<br />
Tests carried out by Cortest Laboratories, Sheffield<br />
Results:<br />
• UNS S34565 thin walled, laser welded tubing did not<br />
corrode in any of the tests<br />
• No corrosion occurred at the welds of any<br />
tubeplate material studied.<br />
UNS S34565, S32760, S31603<br />
• Some corrosion was observed at non welded joints.<br />
Greatest on S32760 and least on S34565.<br />
• The extend of corrosion on the non-welded assemblies<br />
was not great. In particular for the S34565 the corrosion is<br />
insignificant at the lowest oxigen level tested of 65 ppb.<br />
Conclusions:<br />
• UNS S34565 thin walled laser welded tubes when welded to S34565, S32760 or S31603<br />
tubeplates would be suitable for MSF plant evaporators.<br />
• UNS S34565 thin walled laser welded tubes when rolled into S34565 tubeplate<br />
would be suitable for MSF plant evaporators.<br />
Ref.: NACE Corrosion 2001, Paper No. 01484<br />
NACE Corrosion 2002, Paper No. 02190<br />
TKp
Stainless Steel grades for Condenser Tubes<br />
for MSF-Desalination Plants<br />
Superaustenitic stainless steels:<br />
1.4565 (S34565)<br />
Superduplex stainless steels:<br />
1.4410 (S32750)<br />
1.4501 (S32760)<br />
Superferritic stainless steels:<br />
Seacure(S44660)<br />
1.4592 (S44735)<br />
TKp
Stainless Steel grades for Condenser Tubes<br />
for MED-Desalination Plants<br />
Austenitic stainless steels:<br />
1.4404 (S31603)<br />
Duplex stainless steels:<br />
1.4162 (S32101)<br />
1.4362 (S32304)<br />
Ferritic stainless steels:<br />
1.4521 (S44400)<br />
TKp
Stainless Steel thin walled Tubes for Desalination Plants<br />
MSF Plants:<br />
• Heat recovery stages<br />
• Heat reject stages<br />
• Brine heater<br />
• Vacuum systems<br />
MED Plants<br />
• Evaporator shell<br />
• Tube and Tube support plates<br />
• Vacuum ejectors<br />
• Condenser tubes<br />
TKp
1,4 Million Meters<br />
Condenser Tubes of 1.4565<br />
(UNS S34565)<br />
Producer: <strong>Fischer</strong> Edelstahlrohre GmbH<br />
Technical Data:<br />
MED - HTE Multi Effect Distillation<br />
Horizontal Tube Evaporation<br />
Capacity:<br />
2 x 12.000 m³ / d<br />
Operating Temperature: 95 %<br />
TKp
Stainless Steels in the Sea-Water-Desalination<br />
Condenser Tubes made of 1.4565<br />
Source:<br />
VA TECH WABAG<br />
TKp
Stainless Steels in the Sea-Water-Desalination<br />
Technology Heat-Exchanger Tubes<br />
made of 1.4565<br />
Windpowered seawater desalination Plant<br />
TKp
MSF and MED condenser tubing<br />
Historically titanium and copper alloys<br />
Trends and options<br />
• Poor availability of titanium<br />
• Environmental impact of toxic copper ions<br />
• Decreasing use of copper alloys<br />
• Use of corrosion resistant stainless steels<br />
Duplex stainless steels<br />
Austenitic and superaustenitic stainless steels<br />
Ferritic and superferritic stainless steels<br />
• Reduction of wall thickness, e.g.<br />
heat exchanger tubes with 0,3 to 0,1 mm,<br />
UNS S34565 Ref. AVR Rotterdam<br />
Ref.: DME-Seminar Materials and Corrosion in<br />
Desalination Plants, June 2007<br />
Heike Glade, Bremen<br />
Jan Olsson, Outokumpu Stainless<br />
TKp
Reference List<br />
<strong>Fischer</strong> Edelstahlrohre GmbH<br />
Rügen Evaporator-Condenser Tubes of UNS S34565<br />
in Operation since 1998 at about 80°C<br />
St. Martin Testing of Condenser Tubes of UNS S34565<br />
since 1998<br />
Rotterdam MED-Plant of AVR Rotterdam, NL<br />
in Operation since Dez. 1999,<br />
1,4 Mio m Tubes of UNS S34565<br />
Al-Taweelah A1 Condenser tubes of 316 L (1.4404) / MED<br />
Creek Island Evaporator-Condenser Tubes of UNS S34565<br />
will start up in 2009 at about 80°C<br />
South Korea Evaporator-Condenser Tubes of UNS S34565<br />
Installation in a MED test plant<br />
Sharjah U.A.E. Layyah Station for Power Generation & Water<br />
Desalination – Intake Pump Cooling Coil<br />
TKp