Figure 5. Corrosion rate of various alloys in 80% acetic acid with 2000 ppm chloride ions at 90°C.
Figure 6. Corrosion rate of various alloys in concentrated acetic acid with 200 ppm chloride ions.
Practical experience with Sandvik SAF 2507 in organic acids, e.g. in teraphthalic acid plants, has shown that this alloy is highlyresistant to this type of environment. The alloy is therefore a competitive alternative to high alloyed austenitics and nickel alloys inapplications where standard austenitic stainless steels corrode at a high rate.
Resistance to inorganic acids is comparable to, or even better than that of high alloy austenitic stainless steels in certain
concentration ranges. Figures 7 to 9 show isocorrosion diagrams for sulphuric acid, sulphuric acid contaminated with 2000 ppmchloride ions, and hydrochloric acid, respectively.
Figure 7. Isocorrosion diagram in naturally aerated sulphuric acid. The curves represent a corrosion rate of 0.1 mm/year (4 mpy) ina stagnant test solution.
Figure 8. Isocorrosion diagram, 0.1 mm/year (4 mpy) in a naturally aerated sulphuric acid containing 2000 ppm chloride ions.
Figure 9. Isocorrosion diagram in a hydrochloric acid. The curves represent acorrosion rate of 0.1 mm/year (4 mpy) in stagnant testsolution.
Pitting and crevice corrosion
The pitting and crevice corrosion resistance of stainless steel is primarily determined by the content of chromium, molybdenum andnitrogen. The manufacturing and fabrication practice, e.g. welding, are also of vital importance for the actual performance inservice.
A parameter for comparing the resistance to pitting in chloride environments is the PRE number (Pitting Resistance Equivalent).The PRE is defined as, in weight-%PRE = %Cr + 3.3 x %Mo + 16 x %NFor duplex stainless steels the pitting corrosion resistance is dependent on the PRE value in both the ferrite phase and the austenitephase, so that the phase with the lowest PRE value will be limiting for the actual pitting corrosion resistance. In Sandvik SAF 2507the PRE value is equal in both phases, which has been achieved by a careful balance of the elements.The minimum PRE value for Sandvik SAF 2507 seamless tubes is 42.5. This is significantly higher than e.g. the PRE values for otherduplex stainless steels of the 25Cr type which are not super-duplex. As an example UNS S31260 25Cr3Mo0.2N has a minimumPRE-value of 33.One of the most severe pitting and crevice corrosion tests applied to stainless steel is ASTM G48, i.e. exposure to 6% FeCI3 with andwithout crevices (method A and B respectively). In a modified version of the ASTM G48 A test, the sample is exposed for periods of24 hours. When pits are detected together with a substantial weight loss (>5 mg), the test is interrupted. Otherwise the temperatureis increased by 5 °C (9 °F) and the test is continued with the same sample. Figure 11 shows critical pitting and crevice temperatures(CPT and CCT) from the test.Potentiostatic tests in solutions with different chloride contents are presented in Figure 11. Figure 12 shows the effect of increasedacidity. In both cases the applied potential is 600 mV vs SCE, a very high value compared with that normally associated withnatural unchlorinated seawater, thus resulting in lower critical temperatures compared with most practical service conditions.Figure 10. Critical pitting and crevice temperatures in 6% FeCl3, 24h (similar to ASTM G48).The scatter band for Sandvik SAF 2507 and 6Mo+N illustrates the fact that both alloys have similar resistance to pitting, and CPT-values are within the range shown in the figure.Tests were performed in natural seawater to determine the critical crevice corrosion temperature of samples with an appliedopotential of 150 mV vs SCE. The temperature was raised by 4°C (7F) steps every 24 hours until crevice corrosion occurred. Theresults are shown in the table below.AlloySandvik SAF 25076Mo+NCCT (°C)61In these tests the propagation rates of initiated crevice corrosion attacks, at 1550°C (59122°F) and an applied potential of 150 mVvs SCE were also determined. These were found to be around ten times lower for Sandvik SAF 2507 than for the 6Mo+N alloy.Figure 11. Critical pitting temperatures (CPT) at varying concentrations of sodium chloride, from 3 to 25% (potentiostaticdetermination at +600 mV SCE with surface ground with 600 grit paper).Figure 12. Critical pitting temperatures (CPT) in 3% NaCl with varying pH (potentiostatic determination at +600 mV SCE withsurface ground with 600 grit paper).The corrosion resistance of Sandvik SAF 2507 in oxidising chloride solutions is illustrated by critical pitting temperatures (CPT)determined in a 'Green death' -solution (1% FeCI3 + 1% CuCl2 +11% H2SO4 + 1.2% HCI) and in a 'Yellow death' -solution (0.1 %Fe2(SO4)3 + 4% NaCl + 0.01 M HCI). The table below shows CPT-values for different alloys in these solutions. It is clear that thevalues for Sandvik SAF 2507 are on the same level as those for the nickel alloy UNS N06625. The tests demonstrate a goodcorrelation with the ranking of alloys for use as reheater tubes in flue gas desulphurisation systems.Critical pitting temperature (CPT) determined in different test solutions.AlloyCritical pitting temperature (CPT), °C'Green death'Sandvik SAF 25076Mo+NUNS N06625ASTM 31672.57067.5<25>90>90>9020'Yellow death'Stress corrosion crackingSandvik SAF 2507 has excellent resistance to chloride induced stress corrosion cracking (SCC).
The SCC resistance of Sandvik SAF 2507 in chloride solutions at high temperatures is illustrated in Figure 13. There were no signs of
--SCC up to 1000 ppm Cl/300°C and 10000 ppm Cl/250°C.
Sandvik SAF 2507 Ubend specimens exposed for 1000 hours in hot brine (108°C, 226°F, 25% NaCl) showed no cracking.
The threshold stress for Sandvik SAF 2507 in 40% CaCl2 at 100 °C (210 °F) and pH = 6.5 is above 90% of the tensile strength forboth parent metal and welded joints (TIG-welded with Sandvik 25.10.4.L or MMA-welded with Sandvik 25.10.4.LR).
Figure 14 shows the result of testing in 40% CaCl2 at 100 °C (210 °F) acidified to pH = 1.5. Acidifying of the standard test solution topH = 1.5 lowers the threshold stress for Sandvik SAF 2205, but not for Sandvik SAF 2507. This applies to both parent metal andwelded joints.
The threshold stress for both parent metal and welded joints of Sandvik SAF 2507 in boiling 45% MgCl2 , 155°C (311°F) (ASTMG36), is approximately 50% of the proof strength.
Figure 13. SCC resistance in oxygen-bearing (abt. 8 ppm) neutral chloride solutions. Testing time 1000 hours. Applied stress equal toproof strength at testing temperature.
Figure 14. Results of SCC tests with constant load in 40% CaCl2, pH=1.5, at 100 °C (210°F) with aerated test solution.
Figure 15. Constant load SCC tests in NACE solution at room temperature (NACE TM 0177).
Figure 15 shows the results of SCC tests at room temperature in NACE TM0177 Test solution A (5% sodium chloride and 0.5% aceticacid saturated with hydrogen sulphide). No cracking occurred on Sandvik SAF 2507, irrespective of the applied stress.
In aqueous solutions containing hydrogen sulphide and chlorides, stress corrosion cracking can also occur on stainless steels at
temperatures below 60 °C (140 °F). The corrosivity of such solutions is affected by acidity and chloride content. In direct contrast tothe case with ordinary chloride-induced stress corrosion cracking, ferritic stainless steels are more sensitive to this type of stresscorrosion cracking than austenitic steels.
In accordance with ISO 15156/NACE MR 0175 solution annealed and liquid quenched wrought Sandvik SAF 2507 is suitable for useat temperatures up to 450 °F (232 °C) in sour environments in oil and gas production, if the partial pressure of hydrogen sulphidedoes not exceed 3 psi (0.20 bar).
Sandvik SAF 2507, with a maximum hardness of 32 HRC, solution annealed and rapidly cooled, according to NACE MR0103, issuitable for use in sour petroleum refining.Intergranular corrosion
Sandvik SAF 2507 is a member of the family of modern duplex stainless steels whose chemical composition is balanced to give quickreformation of austenite in the high temperature heat affected zone of a weld. This results in a microstructure that provides thematerial with good resistance to intergranular corrosion. Sandvik SAF 2507 passes testing to ASTM A262 Practice E (Strauss test)without reservation.Erosion corrosion
The mechanical properties combined with corrosion resistance give Sandvik SAF 2507 a good resistance to erosion corrosion. Testingin sand containing media has shown that Sandvik SAF 2507 has an erosion corrosion resistance better than corresponding austeniticstainless steels. Figure 16 below shows the relative mass loss rate of the duplex Sandvik SAF 2507, Sandvik SAF 2205 and an
austenitic 6Mo+N type steel after exposure to synthetic seawater (ASTM D-1141) containing 0.025-0.25% silica sand at a velocity of8.9-29.3 m/s (average of all tests is shown).
Figure 16. Relative mass loss rate after testing of the resistance aginst erosion corrosion.Corrosion fatigue
Duplex stainless steels which have a high tensile strength usually have a high fatigue limit and high resistance to both fatigue andcorrosion fatigue.
The high fatigue strength of Sandvik SAF 2507 can be explained by its good mechanical properties, while its high resistance tocorrosion fatigue has been proven by fatigue testing in corrosive media.
Heat treatment
The tubes are normally delivered in heat treated condition. If additional heat treatment is needed due to further processing thefollowing is recommended.Solution annealing
10501125°C (19202060°F), rapid cooling in air or water.
Welding
The weldability of Sandvik SAF 2507 is good. Suitable welding methods are manual metal-arc welding with covered electrodes orgasshielded arc welding. Welding should be undertaken within the heat input range of 0.2-1.5 kJ/mm and with an interpasstemperature of 150°C (300°F) maximum.
Preheating or post-weld heat treatment is not necessary.
Matching filler metals are recommended in order to obtain a weld metal with optimum corrosion resistance and mechanicalproperties. For gas-shielded arc welding use Sandvik 25.10.4.L, and for manual metal-arc welding the covered electrode Sandvik25.10.4.LR.
Fabrication
Bending
The starting force needed for bending is slightly higher for Sandvik SAF 2507 than for standard austenitic stainless steels (AISI 304Land 316L).
If the service conditions are on the limit of the stress corrosion resistance of Sandvik SAF 2507 heat treatment is recommended aftercold bending. For pressure vessel applications in Germany and the Nordic countries heat treatment may be required after colddeformation in accordance with VdTÜVWb 508 and NGS 1609. Heat treatment should be carried out by solution annealing (Seeunder Hest treatment) or resistance annealing.
Hot bending is carried out at 11251025 °C (20601880°F) and should be followed by solution annealing.Expanding
Compared to austenitic stainless steels, Sandvik SAF 2507 has a higher proof and tensile strength. This must be kept in mind whenexpanding tubes into tubesheets. Normal expanding methods can be used, but the expansion requires higher initial force and shouldbe undertaken in one operation. As a general rule, tube to tubesheet joints should be welded if the service conditions include a highchloride concentration, thus limiting the risk of crevice corrosion.Machining
Being a two-phase material (austenitic-ferritic) Sandvik SAF 2507 will present a different tool wear profile from that of single-phasesteels of type AISI 304L. The cutting speed must therefore be lower than that recommended for AISI 304L. It is recommended thata tougher insert grade is used than when machining austenitic stainless steels, e.g. AISI 304L.
Applications
Sandvik SAF 2507 is a duplex stainless steel especially designed for service in aggressive chloride-containing environments. Typicalapplications are:
Typical applications: Sandvik SAF2507Oil and gas industryChloride-containing environments such as seawater handling and process systems. Hydraulic and process fluid tubes inumbilicalsSeawater coolingTubing for heat exchangers in refineries, chemical industries, process industries and other industries using seawater orchlorinated seawater as coolantSalt evaporation industryDesalination plantsGeothermal wellsEvaporator tubing for production of corrosive salts, e.g. chlorides, sulphates and carbonatesPressure vessels for reverse osmosis units, tube and pipe for seawater transport, heat exchanger tubingHeat exchangers in geothermal exploitation units, systems exposed to geothermal or high salinity brines, tubing andcasing for productionRefineries andpetrochemical plantsPulp and paper industryChemical industryMechanical componentsrequiring high strengthDesulphurisation unitsTubes and pipes where the process environment contains a high amount of chlorides, or is contaminated withhydrochloric acidMaterial for chloride-containing bleaching environmentsOrganic acid plants, also when process solutions are contaminated with e.g. chloridesPropeller shafts and other products subjected to high mechanical load in seawater and other chloride-containingenvironmentsAs reheater tubes in flue gas desulphurisation systems. The good mechanical and corrosion properties make SandvikSAF 2507 an economical choice in many applications by reducing the life cycle cost of equipment.Disclaimer: Recommendations are for guidance only, and the suitability of a material for a specific application can be confirmed only when we know the actual service conditions.Continuous development may necessitate changes in technical data without notice. This datasheet is only valid for Sandvik materials.
因篇幅问题不能全部显示,请点此查看更多更全内容
Copyright © 2019- igat.cn 版权所有 赣ICP备2024042791号-1
违法及侵权请联系:TEL:199 1889 7713 E-MAIL:2724546146@qq.com
本站由北京市万商天勤律师事务所王兴未律师提供法律服务