Dr. Winfried Heimann - Fischer Group

Dr. Winfried Heimann - Fischer Group Dr. Winfried Heimann - Fischer Group

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• <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 />

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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 />

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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 />

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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 />

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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 />

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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 />

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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 />

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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 />

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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 />

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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 />

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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 />

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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 />

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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 />

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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 />

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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 />

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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 />

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Condenser tubes UNS S34565<br />

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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 />

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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 />

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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 />

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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 />

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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 />

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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 />

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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 />

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Stainless Steels in the Sea-Water-Desalination<br />

Condenser Tubes made of 1.4565<br />

Source:<br />

VA TECH WABAG<br />

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Stainless Steels in the Sea-Water-Desalination<br />

Technology Heat-Exchanger Tubes<br />

made of 1.4565<br />

Windpowered seawater desalination Plant<br />

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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 />

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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 />

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