Polythionic Acid Stress Corrosion Cracking

The chemical reaction of sulfur compounds, oxygen, and water at elevated temperatures, which typically occurs during process unit shutdowns, can lead to the formation of oxoacids known as polythionic acids (PTAs). These acids can destroy the passive oxide layer of austenitic steels and alloys. Consequently, if the austenite stainless steel is sensitized and subjected to stress, it can lead to an intergranular cracking phenomenon known as Polythionic Acid Stress Corrosion Cracking (PTASCC). This mechanism can occur in any unit that using sensitized austenitic material in high-temperature sulfur containing environments. PTASCC is typically seen in FCC regenerators and heater/furnace tubes in crude and hydroprocessing units.

General Information

Polythionic Acid Stress Corrosion Cracking (PTASCC) is a form of intergranular cracking that requires coexistence of three elements: a susceptible material (e.g. sensitized austenitic stainless steels and some Ni alloys), presence of polythionic acids and stress.1 2 Therefore, PTASCC occurs commonly in areas typically operating in range of 370-843°C (700-1550°F) where sensitization of austenitic materials will progress.2 3 4

Polythionic acids, the second element, are typically formed during shutdown or process upset events when oxygen and water/moisture ingress may take place. Stress, the third necessary element for PTASCC and typically arises during cold and/or hot mechanical operations such as welding and bending. The interaction of these three elements is schematically shown in Figure 1.


PTASCC mechanism general concept.
Figure 1: PTASCC mechanism general concept.

The most common areas of PTASCC are listed in Table 1.

Table 1 Typical Areas for PTASCC in Refining and Petrochemical Industries. 1 2 4 5

UnitPTASCC Affected AreaComments
Steam ReformingHeater tubesExternal PTASCC when using sour fuel
Catalytic ReformingFeed/effluent exchangerHot side
HydrocrackingREAC-
HydrotreatingFeed heater tubes
Feed/effluent exchanger
-
FCCReactor
Regenerator Overhead line
Flue gas line
Expansion joints
Typically, at HAZ areas
CDU/VDUAtmospheric and Vacuum heaters tubesIt is believed that oil film and/or
coke layer may reduce the likelihood for PTA attack
SRUAcid gas preheaters321 steel

Mechanism

Role of Sensitization: The sensitized austenitic material is a key factor in the occurrence of PTASCC. Sensitization results from carbide precipitation at the grain boundaries of austenitic (300 series) and ferritic-martensitic (400 series) stainless steels. This process occurs when these steels are exposed for prolonged periods to temperatures typically ranging from 537°C (1000°F) to 843°C (1550°F). Carbide formation depletes the areas near the grain boundaries of the alloying element (chromium), making these areas susceptible to intergranular cracking when exposed to an aqueous corrosive environment.3

Carbide precipitation occurs spontaneously during normal process operation, material fabrication, or welding. Sensitization can be slowed down either by limiting the amount of carbon present in the material—hence the use of low carbon (L) stainless steel grades—or by adding elements such as titanium and niobium (use in steels type 321 and 347), which have a higher affinity for carbon and replace chromium in the carbide composition.

While sensitization is relatively simple in its fundamentals, it is a complex process influenced by a combination of material composition, temperature, and exposure time. Moreover, when steels are sensitized, they can undergo a reversal process known as desensitization when exposed to high temperatures (>650°C / >1202°F) for prolonged periods. Although slower, this process can mitigate the negative effects of sensitization to some extent. The temperature at which sensitization starts varies for different materials, as shown in Table 2.4

Table 2 Sensitization temperature for common austenitic materials after 1 4

MaterialTemperature
300 series standard carbon stainless steels:
304 (UNS S30400), 316 (UNS S31600), 317 (UNS S31700)

370°C (700°F) - 815°C (1,500°F)
300 series high carbon stainless steels:
304H (UNS S30409), 316H (UNS S31609)

370°C (700°F) - 815°C (1,500°F)
Ti/Ni Stabilized steels:
321 (UNS S32100), 347 (UNS S34700)

400°C (750°F) – 815°C (1,500°F)
Ni-based austenitic alloys
Alloy 800 (UNS N08800)
Alloy 825 (UNS N08825)
Alloy 625 (UNS N06625)

370°C (700°F) to 815°C (1,500°F)
650°C (1,200°F) to 760°C (1,400°F)
650°C (1,200°F) to 760°C (1,400°F)

Hot work, such as welding, can sensitize the material due to the locally applied heat flux. Therefore, post-weld heat treatment (PWHT) is essential for mitigating PTASCC. Typically, all steels and alloys operating in PTASCC-risk environments are used in a solution-annealed state, and areas of hot work (welding) are subject to mandatory PWHT. An example of a generic, qualitative ranking of PTASCC risk versus operating temperature and PWHT for various materials is presented in Table 3.6

Table 3 PTASCC cracking susceptibility versus temperature and heat treatment after 2 6

Polythionic acids: Polythionic acids (PTA) are a group of oxoacids with the general formula H₂SₓOᵧ, where x is typically in the range of 1 to 5 and y is from < 1 to 6. PTAs are formed during the oxidation and hydrolysis of iron sulfide films present on the surface of austenitic stainless steel, as shown in the example equation below:

\(\ce{2FeS + 4O2 + H2O -> H2S2O6 + Fe2O3}\) Equation 1

It is important to highlight that PTAs may form not only from FeS but also from other oxidizable sulfur-containing species such as H₂S.

Water is typically introduced to the unit during the steaming operation, which is conducted to purge any remaining hydrocarbons. Oxygen, on the other hand, is usually sourced from the surrounding air when the unit is open to the atmosphere. Additionally, oxygen can enter the system through air-contaminated nitrogen, which is often used in purging and blanketing during shutdown operations. However, the above examples do not account for all potential sources of water and oxygen. Therefore, it is important for process engineers to conduct a thorough analysis of the system, identify all possible entry points for water and oxygen, and assess the risks associated with the formation of PTAs.

Tensile stress: The third element required for PTASCC is the presence of tensile stress. This stress can be either residual or applied. Residual stress often arises from fabrication processes such as welding, machining, or hot/cold forming. Applied stress, on the other hand, comes from mechanical loads imposed on the material during service. This could include pressures from internal fluids, external forces, or even thermal expansion and contraction. Both residual and applied stresses contribute to the susceptibility of austenitic stainless steel to PTASCC. The specific levels of tensile stress and the degree of sensitization required to initiate PTASCC are not well understood. Given these uncertainties, it is crucial to implement relevant stress relief practices as one of the preventive measures.

Prevention and Mitigation

Like any other stress corrosion cracking mechanism, PTASCC can be prevented by disrupting or eliminating one of the components involved in the interaction matrix of parameters. This matrix includes factors such as the presence of tensile stress, the material’s susceptibility to sensitization, and the corrosive environment containing polythionic acids. Disrupting one or more components within this interaction matrix—whether it’s tensile stress, material sensitization, or exposure to corrosive environments—can effectively prevent PTASCC. Table 4 presents various mitigation strategies and practices aimed at preventing Polythionic Acid Stress Corrosion Cracking (PTASCC).4

Table 4 Various Mitigation Strategies and Practices for Preventing PTASCC

MitigationDescriptionComments
Material* Use low carbon <0.03% stainless steels
* Use stabilized steels (with Ti or Nb)
* Will slow sensitization but not eliminate
* Ti-C = 5:1; Nb-C=8:1
Fabrication/welding* Use matching filler material (low carbon)
* Dual grade 300 series steels e.g. 316/316L can be used
* For stabilized steels stabilizing heat treatment is beneficial to retard sensitization
* Weld overlays using Low-C or stabilized grades as-deposited or with PWHT are resistant to PTASCC
* Stress-relief heat treatments are not considered as a way to reduce the likelihood of PTASCC
* Heat-affected zones (HAZs) of welded stabilized material need a thermal stabilization to prevent PTASCC
* Typical; 843-900°C (1,550-1,650 °F); 2- 4h – for 321/347. For other stabilized materials holding time may be different.
* Stabilizing should be done after annealing process.
* PWHT treatment is beneficial from stress relief perspective.
* Thermal gradient controls during PWHT is beneficial to avoid thermal stresses followed by stress relaxation cracking of weldments.
* Important in heavy-wall (> 25 mm thick) sections.
Process* Operate below sensitization temperature
* Use nitrogen purge
* Use washing with Na2CO3 solution
* Use dry air to prevent water condensation.
* See Table 2
* Nitrogen should be dry and oxygen free (min N4.0 or 99.99%)
* When steaming prior nitrogen purging, steam injection should be stopped before cooling to temp. c.a. 72°C above water dew point
* Concentration: typical between 1 and 5wt% Na2CO3 – most common – 2wt%.
* NaOH (caustic soda) – should not be used
* There is no specific limit for chlorides in alkali solution but for certain units e.g. hydrocracking chlorides should be limited to max 250ppm
* Proper draining is required to avoid dry alkali and chloride deposits
* When draining is problematic – use low chloride alkali solutions (max 25ppm)
* For details see Ref 4
* Careful with potential pyrophoric substances present inside the equipment/catalyst etc.
* Air dew point should be lower by min of 22°C than equipment/pipe surface temp.

References

This Article has 6 references.

1:American Petroleum Institute Recommended Practice – API RP 571, latest edition

2:C.A. Shargay, T. Tajalli, K. Moore, L. Roberts, J. Allen - Assessing Stress Corrosion Cracking Risks on Stainless Steel Piping and Equipment - NACE Corrosion Conference 2017, paper no. 8899

3:ASME Boiler and Pressure Vessel Code, Section II, part D, latest edition

4:AMPP/NACE - Protection of Austenitic Stainless Steels and Other Austenitic Alloys from Polythionic Acid Stress Corrosion Cracking During a Shutdown of Refinery Equipment - Publication no SP0170, latest edition

5:M.A. Al-Hammad, A. Kermad - Sulfur Recovery Plant; Corrosion Controls - NACE Corrosion Conference 2016, paper no. 7428

6:American Petroleum Institute Recommended Practice – API RP 581, latest edition