Wet Corrosive Service: Selection of Heat Exchanger Tubes
Introduction
High nickel alloy stainless steels are categorized as having a chromium + nickel content greater than 50%, with most alloys having a nickel content greater than 30%. These materials are widely used in the petrochemical, chemical, refining, and organic acid industries due to their excellent overall corrosion resistance to all media types and high-temperature harsh environments.
Austenitic stainless steels are not as expensive or have as long lead times but are unsuitable for severe corrosion applications. Even when they are used, they have a concise life.
In the past few years, duplex steel has been widely used as an alternative to austenitic steel because of its excellent corrosion resistance under certain conditions. However, the main disadvantage of duplex steels is the limited temperature region in which the equipment operates. In addition, the stress relief heat treatment after U-bending is problematic.

Super Austenitic Stainless Steel Heat Exchanger Tubes
Description
Super austenitic stainless steels have a PREN value (calculated by the formula: PREN = %Cr + 3.3 x %Mo + 16 x %N) greater than 35. These steels can also be categorized as Cr-Ni-Mo or Cr-Ni-Mo-Cu steels, with chromium contents between 17% and 25%, nickel contents between 14% and 25%, and molybdenum contents between 3% and 7%. Many of these steels are also alloyed with nitrogen to increase corrosion resistance and strength further. Some grades are also alloyed with copper to improve resistance to certain acids. In the annealed condition, it also has a fully austenitic grain structure, good cold and hot working properties, and is easy to weld. Some of the grades detailed in this paper are super austenitic, as shown in Table 1.
Wet Corrosion Characteristics
Pitting Corrosion
Pitting corrosion is a rat hole through the wall of the localized corrosion. The formation of pitting depends on several factors, such as the corrosive environment (e.g., halides-chlorides, bromides, and fluorides), temperature, and, most importantly, defects and weaknesses in the passive protective layer of the steel. Once pitting corrosion has started, it expands at a much faster rate. The higher the chromium content in stainless steel, the stronger the passive protective layer of chromium oxide forms on the surface, thus contributing to resistance to pitting. Similarly, the higher the molybdenum content, the more excellent the resistance to pitting, as it helps reduce the pitting growth rate. Higher nitrogen levels in steel help neutralize acidic corrosive solutions, thus helping to prevent pitting. Under these conditions, PREN (i.e., Pitting Resistance Equivalent) is used as a rule of thumb for selecting materials, i.e., PREN = %Cr + 3.3 x %Mo + 16 x %N (for austenitic, duplex, and super austenitic steels).
| Common Grade Name | ASTM | UNS Number | EN | C max | Cr | Ni | Mo | N | Cu |
| 6 Moly | S31254 | 1.4547 | 0.200 | 19.5-20.5 | 17.5-18.5 | 6-6.5 | 0.18-0.22 | 0.5 max | |
| Alloy 926 | N08926 | 1.4529 | 0.200 | 19-21 | 24-26 | 6-7 | 0.15-0.25 | 0.5-1.5 | |
| Alloy 6XN | N08367 | 0.200 | 20-22 | 24-25.5 | 6-7 | 0.20-0.25 | 0.75 max | ||
| 904L | 904L | N08904 | 1.4539 | 0.200 | 19-23 | 23-28 | 4-5 | 1-2 | |
| Alloy 28* | N08028 | 1.4563 | 0.200 | 26-28 | 30-34 | 3-4 | 0.10 max | 0.7-1.5 | |
| Duplex | S31803 / S32205 | 1.4462 | 0.300 | 21-23 | 4.5-6.5 | 2.5-3.5 | 0.08-0.20 | ||
| Super Duplex | S32750 | 1.4410 | 0.300 | 24-26 | 6-8 | 3-5 | 0.24-0.32 | ||
| 316L | 316L | S31600 | 1.4401 | 0.030 | 16-18 | 8-12 | 2-3 | ||
| 304L | 304L | S30400 | 1.4301 | 0.030 | 18-20 | 10-14 |
*Alloy 28 can also be considered as a kind of Nickel Alloy. However, it has been featured in this list for comparison purposes only.
As can be seen in Table 2, super austenitic stainless steels have a PREN of more than 27, which is higher than that of standard austenitic steels, and for some of these grades, the PREN is also higher than that of duplex (35) and super duplex (42) steels. The critical pitting temperature (CPT) is calculated from the ASTM G48 Method A corrosion test, which involves exposing the material to a 6% wt ferritic chloride solution for 72 hours (usually 24 hours). This is the temperature at which pitting may begin. The CPT of a material is directly proportional to the PREN of the material and gives a good indication of the ability of these materials to resist pitting.
| Common Grade Name | PREN Max |
| 6 Moly | 43 |
| Alloy 926 | 46 |
| N08367 | 47 |
| 904L | 37 |
| Alloy 28 | 39 |
| Duplex | 35 |
| Super Duplex | 42 |
| 316L | 27 |
| 304L | 19 |
Super austenitic steels perform much better than standard austenitic steels and duplex steels in terms of pitting caused by chlorides.
Stress Corrosion Cracking
Stress Corrosion Cracking (SCC) is cracking caused by a combination of tensile stress and a corrosive environment. The effect of stress corrosion cracking on a material is usually between dry cracking and the material fatigue threshold. The required tensile stress can be either a directly applied stress or a residual stress.
Chloride stress corrosion cracking (CSCC) is one of the most severe forms of localized corrosion. Elevated temperatures and lower pH values increase the probability of CSCC. The resistance of alloys to SCC has been determined to increase at levels above 12% nickel and 3% molybdenum. The SSC of super austenitic stainless steels is superior to that of standard 300 series austenitic stainless steels and some duplex stainless steels.
As shown in Figure 2, alloys 6Mo, 926, and UNS N08367 are resistant to chloride-induced stress corrosion cracking. The resistance to chloride stress corrosion cracking improves from alloy 6Mo to alloy 926 to alloy UNS N08367. When chlorides are present, they are immune to SCC at boiling temperatures. Grades UNS N08926, with more than 20% nickel and 2% molybdenum, have improved SCC properties compared to standard austenitic steels.
Reducing and Oxidizing Acids
Most super austenitic stainless steels are copper alloys, which gives them good resistance to reducing and non-oxidizing acids such as sulfuric and phosphoric acids. In addition, the high chromium content produces a strong passive layer that improves corrosion resistance to sulfuric and phosphoric acids.
In highly concentrated sulfuric acid at temperatures up to 50 degrees Celsius, the corrosion rate of alloy 28 is less than 0.1 millimeters per year.

The grade also performs well in phosphoric acid heaters where phosphate rock is contaminated with high concentrations of chlorides and fluorides. 904L is also widely used in the phosphoric acid industry.
Applications
Conventional Refineries and Biorefineries:
Several types of exchangers can be used as condensers and coolers. Pitting is usually a problem for overhead condensers, surface condensers, chillers, and interstage coolers with water on the tube side. The extent of the pitting depends on water quality, chloride content, and temperature. Super austenitic can be used in such conditions due to its high pitting resistance equivalent.

The higher temperature limit of super austenite compared to duplex steels also reduces operational failures due to elevated surface temperatures. The fouling factor should also be considered; fouling increases the surface temperature and leads to premature failure of duplex steels. Amine-poor and amine-rich coolers have similar conditions and can be used as potential applications for super austenitic grades. Cases have been made for 6Mo and Alloy 28 in refineries for such applications. Other possible applications in refineries include sour water strippers and sulfur condensers. In addition, the high molybdenum content of the super austenitic grades makes them suitable for resistance to naphthenic acid corrosion.
Sulfuric and Phosphoric Acid Industries:
Some super austenitic steels, such as Alloy 28, 904L, and Alloy 926 (also known as nickel-chromium-molybdenum-copper alloy steels), have good acid resistance. They are suitable for use in sites where sulfuric and phosphoric acids are produced or in industries where these acids are used for other recovery and treatment purposes, such as copper recovery. Suitable exchangers include sulfuric acid coolers, phosphoric acid heaters (for wet process phosphoric acid production), and acid reheaters.

Flue gas condenser piping is also subject to corrosion due to the condensation of sulfur vapors, which combine with moisture to form sulfuric acid. Super austenitic steels are suitable for piping carrying dilute sulfuric and phosphoric acids, even if the piping is contaminated.
LNG / Cryogenic:
Most super austenitic steels have a lower operating temperature limit of -175°C. They can also be used to transport sulfuric acid and phosphoric acid, even if they are contaminated. Super austenitic steels, therefore, have the dual advantage of operating in cryogenic environments and having good resistance to pitting. Standard austenitic steels, such as 316L, can also be used in cryogenic conditions, but they are much less resistant to chloride pitting than super austenitic steels.
Conclusion
Super austenitic steels offer superior corrosion resistance to both pitting and stress corrosion compared to standard austenitic steels. In addition, super austenitic steels provide the same or better performance than duplex steels. It has been widely used in reducing and oxidizing acids in various concentrations, although its application in highly concentrated and contaminating acids can be limited by temperature. It is more stable in price and availability than high-nickel alloy steels so that it can be selected based on process conditions and final application. It is also easy to weld and fabricate. These materials are available in various forms, including plates, sheets, tubes, and fittings.






GSM
GSM
GSM











