In chemical equipment, stainless steel can greatly reduce the occurrence of corrosion in the equipment due to its stability and strong corrosion resistance, thus playing a protective role. In heat exchangers and piping systems, due to the corrosive chemicals in the chemical field, stainless steel and duplex steel have become the preferred materials due to their advantages of high temperature, high pressure and corrosion resistance.
JN's stainless steel and duplex steel materials are mainly used in chemical reactors, heat exchangers, piping systems, steam units, distillation towers, storage tanks and oil pipelines. We produce valves, seals, fasteners, pipes and fittings, etc.
Chemical equipment includes many, such as pressure vessels, petrochemicals, power plants, chemical processing and medical equipment manufacturing. The production design of these projects requires the participation lots of corrosion-resistant special metal materials. High-grade stainless steel, duplex steel, nickel-based alloys are widely used to resistant to high temperature and corrosion.
Application Scenarios
Pressure Vessels
Chemical Processing
Medical Equipment
Why Material Selection Decides the Life of Chemical Equipment
In chemical plants, failure is rarely mechanical first — it is almost always corrosion first. A reactor, heat exchanger or distillation column is attacked 24/7 by acids, chlorides, high temperature and pressure. Choosing the wrong grade means leaks, unplanned shutdown, product contamination and, in the worst case, a safety incident. Choosing the right grade means a plant that runs for 15–30 years with only scheduled maintenance.
JN Alloy supplies the full range of corrosion-resistant metals used in chemical equipment: austenitic stainless steels (316L, 317L, 904L, 254SMO), duplex and super-duplex steels, nickel-copper alloys (Monel), nickel alloys (200/201), nickel-chromium alloys (Inconel, Incoloy) and the nickel-molybdenum / nickel-chromium-molybdenum Hastelloy families. We deliver these as pipe, tube, plate, sheet, bar, forging, flange, fitting and prefabricated assemblies for pressure vessels, petrochemical units, power plants, chemical processing and related manufacturing.
The five corrosion modes that kill chemical equipment
UNIFORM General Acid Attack
The whole surface thins evenly. Controlled by corrosion rate (mm/year). The basis for "corrosion allowance" in vessel design.
LOCALIZED Pitting & Crevice
Chlorides drive deep pits or attack under gaskets, deposits and lap joints. Resisted by molybdenum and nitrogen (PREN).
CRACKING Stress Corrosion (SCC)
Chlorides + tensile stress + high temp crack austenitic 300-series stainless. Avoided with duplex, high-Ni or proper stress relief.
GRAIN Intergranular
Sensitization after welding (Cr carbide at grain boundaries). Avoided with low-C or stabilized (Ti/Nb) grades, or solution anneal.
FLOW Erosion-Corrosion
High-velocity slurries or vapors strip the passive film. Needs solid solution alloys with high hardness or hardened overlays.
MIXED Galvanic
Dissimilar metals in electrolyte: the more active one corrodes faster. Managed by insulation or compatible pairings.
UNIFORM General Acid Attack
The whole surface thins evenly. Controlled by corrosion rate (mm/year). The basis for "corrosion allowance" in vessel design.
LOCALIZED Pitting & Crevice
Chlorides drive deep pits or attack under gaskets, deposits and lap joints. Resisted by molybdenum and nitrogen (PREN).
CRACKING Stress Corrosion (SCC)
Chlorides + tensile stress + high temp crack austenitic 300-series stainless. Avoided with duplex, high-Ni or proper stress relief.
GRAIN Intergranular
Sensitization after welding (Cr carbide at grain boundaries). Avoided with low-C or stabilized (Ti/Nb) grades, or solution anneal.
FLOW Erosion-Corrosion
High-velocity slurries or vapors strip the passive film. Needs solid solution alloys with high hardness or hardened overlays.
MIXED Galvanic
Dissimilar metals in electrolyte: the more active one corrodes faster. Managed by insulation or compatible pairings.
Design principle: corrosion allowance + alloy selection + fabrication route (weld procedure, heat treatment) together determine service life. This guide focuses on alloy selection; always confirm the final choice against the actual process chemistry, including trace impurities (F⁻, Cl⁻, oxidizers).
Alloy Selection by Acid: Hydrochloric, Sulfuric, Phosphoric, Hydrofluoric
Acids are not one problem — they are several. Reducing acids (HCl, dilute H₂SO₄) demand high nickel + molybdenum; oxidizing acids and mixed acids demand chromium + molybdenum; hydrofluoric acid is its own special world ruled by nickel-copper. Match the alloy to the acid, its concentration and its temperature.
Hydrochloric Acid (HCl) — the toughest common acid
Hydrochloric acid is a strong reducing acid and attacks almost every stainless steel at useful rates. It is the classic domain of the nickel-molybdenum Hastelloy B family and of nickel metal.
Hastelloy B2 / B3 (UNS N10665 / N10675): the standard choice for HCl across a wide concentration and temperature range, including boiling dilute-to-medium acid. B3 adds better thermal stability and fabrication tolerance over B2.
Nickel 200 / 201 (UNS N02200 / N02201): good in HCl at low-to-moderate concentration and temperature; Nickel 201 is preferred above ~315 °C for lower carbon.
Avoid: 300-series stainless, 904L, 254SMO, Inconel and the C-family Hastelloys — they are rapidly attacked by HCl. Use them only for trace HCl in otherwise mild streams.
Concentration / Temp
Recommended
Use with caution
Avoid
All conc., up to boiling
Hastelloy B2 / B3
Nickel 200/201 (lower temp)
316L, 904L, 254SMO, C276
Dilute (<10%), ambient
Hastelloy B2/B3, Nickel 200
—
Standard stainless
Trace HCl in neutral stream
904L, 254SMO, Alloy 31
316L
—
Sulfuric Acid (H₂SO₄) — concentration and temperature dependent
Sulfuric acid behavior flips with concentration. Dilute/medium H₂SO₄ is reducing (favors high-Ni/Mo); very concentrated hot H₂SO₄ becomes oxidizing (favors high-Cr). Selection is a moving target.
≤ ~50%, up to ~60 °C: Alloy 20 (N08020), 904L (N08904), 254SMO, even 316L/317L for the mildest cases.
Higher concentration / higher temperature / contaminated: Hastelloy C276 (N10276), C22 (N06022), Alloy 31 (N08031) — the versatile workhorses for aggressive H₂SO₄.
Hastelloy B2/B3 also performs well in H₂SO₄ but is less versatile than the C-family when chlorides or oxidizers are present.
H₂SO₄ condition
Best choice
Acceptable
Dilute (<40%), <80 °C
Alloy 20, 904L
316L, 317L, 254SMO
Medium (40–80%), warm
Hastelloy C276, C22, Alloy 31
Alloy 20
Concentrated, hot, impure
Hastelloy C276 / C22
Alloy 31
Phosphoric Acid (H₃PO₄) — moderate, but watch the impurities
Phosphoric acid is milder than HCl. Commercial (wet-process) phosphoric acid, however, carries fluoride and chloride impurities that sharply raise aggressiveness.
Pure / mild H₃PO₄: Alloy 20, 904L, 254SMO, 316L/317L are widely used.
Hot, concentrated, or impurity-laden (F⁻/Cl⁻): Hastelloy C276 / C22, Alloy 31 give the margin you need.
Alloy 20 was essentially designed around phosphoric and sulfuric acid service and remains a cost-effective favorite here.
Hydrofluoric Acid (HF) — the nickel-copper rule
Hydrofluoric acid is chemically unique. The classic, field-proven material is Monel 400 / K500 (Ni-Cu), with Nickel 200/201 also performing well. A non-negotiable rule: avoid silicon-bearing alloys (including many high-silicon stainless and cast irons not specifically rated for HF) — silicon dramatically accelerates attack.
Critical: Never specify a silicon-containing alloy for HF service. Monel 400, Monel K500 and Nickel 200/201 are the safe, proven choices for anhydrous and aqueous HF across broad concentration and temperature ranges. Carbon steel is sometimes used only for very high-concentration anhydrous HF.
Acid
Top alloy(s)
Also usable
Avoid
HCl
Hastelloy B2 / B3
Nickel 200/201
All stainless, C-family
H₂SO₄
Hastelloy C276 / C22, Alloy 31
Alloy 20, 904L, 254SMO
Carbon steel (hot conc.)
H₃PO₄
Alloy 20, Hastelloy C276
904L, 254SMO, 316L/317L
Plain carbon steel
HF
Monel 400 / K500
Nickel 200/201
Silicon-bearing alloys
Limits are indicative. Always verify against the producer's corrosion chart for your exact concentration, temperature, aeration and impurity profile before finalizing.
Material Selection by Equipment Type
The same acid can demand different materials depending on where it lives in the plant. Thin-wall tubing, agitated vessels and tall columns each create their own corrosion and mechanical challenges.
Heat Exchangers
Heat-exchanger tubes run thin walls (often 0.5–2.0 mm) with high surface area and thermal cycling, so a small corrosion rate means a short life. Tube sheets are thicker and often a different, heavier grade or explosively clad. U-tubes need excellent ductility (annealed condition) to bend without cracking.
General corrosive service: 904L, 254SMO, Alloy 20 seamless tubes.
Aggressive acid / chloride: Hastelloy C276, B2/B3, or Titanium/Monel for specific streams.
Tube sheets: often solid Hastelloy or a carbon-steel base explosively clad with the tube alloy to control cost.
Tip: size the corrosion allowance to the tube wall, not the vessel wall. A 0.1 mm/year rate eats a 1 mm wall in 10 years — far shorter than the 20+ year life expected of the shell.
Reactors / Reaction Kettles
Reactors are pressure vessels, often jacketed and mechanically agitated, so they need both corrosion resistance and strength. For thick walls, solid high-alloy is expensive; cladding is the standard cost-control move.
Clad construction: carbon-steel or low-alloy base + explosively welded / weld-overlaid Hastelloy C276, 625, 825 or 904L.
Solid alloy: for smaller or highly aggressive vessels — Hastelloy C276/C22, Alloy 625, Alloy 20, 904L.
Agitator shafts & impellers: often higher-strength alloys (Inconel 718, Monel K500) or hard-faced to resist erosion-corrosion.
Distillation Columns / Towers
A column is not one environment — it is many, stacked vertically. The overhead (cool, often condensing chlorides) and the bottoms / reboiler (hot, concentrated) are the two extremes that drive selection.
Overhead, trays, packing: 316L, 904L, 254SMO for chloride-bearing condensing streams.
Reboiler & hot concentrated bottoms: Hastelloy C276, Alloy 625, Alloy 31 — high temperature plus concentration is the harsh corner.
Trays / packings: match the most aggressive local condition; consider higher-Mo grades where fouling creates crevices.
Rule of thumb: design each column zone for its own worst case. A single "column material" rarely survives both the cool chloride overhead and the hot concentrated reboiler.
Equipment
Typical duty
Common alloys
Shell-and-tube exchanger
Acid cooling / heating
904L, 254SMO, Alloy 20, Hastelloy C276/B2 tubes
Reactor / kettle
Pressure + acid + agitation
Clad C276/625/825, solid Alloy 20/904L
Distillation column
Fractionation of acids
316L/904L overhead, C276/625 reboiler
Welding and Fabrication
Selecting the alloy is only half the job. A corrosion-resistant grade fabricated with the wrong procedure can corrode faster than a cheaper grade done correctly. Welding, heat treatment and forming all change the microstructure at the joint — precisely where failures start.
The weld zone is the weak point
Welding heats and cools the metal rapidly. In austenitic stainless steels this can sensitize the heat-affected zone (chromium carbide precipitation at grain boundaries), creating intergranular corrosion routes. In the nickel alloys, improper filler or excess heat input can dilute chemistry and lose corrosion resistance. The controls are well established:
Use matched or over-alloyed filler. Hastelloy C276 is typically welded with ERNiCrMo-4 (C276) filler; Alloy 625 with ERNiCrMo-3; Monel with ERNiCu-7. Under-matching filler is the most common cause of weld-line attack.
Control heat input and interpass temperature. Lower heat input and a cool interpass reduce sensitization and distortion, especially in thin exchanger tubing.
Solution anneal when required. After welding thin-wall or critical components in 300-series stainless and some nickel alloys, a full solution anneal restores corrosion resistance. For field-fabricated large vessels, low-carbon (L) grades and stabilized (321/347) grades reduce the need for post-weld heat treatment.
Avoid contamination. Copper, zinc, lead and sulfur contamination from tools, paints or shop dust causes rapid selective attack. Dedicate tools and keep the alloy separate from carbon steel.
Forming, cladding and inspection
Cold forming (e.g., U-tube bending, dished heads) work-hardens the metal and can raise residual stress — a driver of stress corrosion cracking in chloride service. Stress-relief or solution anneal after heavy forming is standard for critical parts. For clad construction, the bond between the carbon-steel base and the corrosion-resistant layer must be verified by ultrasonic inspection, and the overlay thickness confirmed to cover the design corrosion allowance. Final acceptance relies on NDE (PT/MT/UT/RT as specified) plus a mill test certificate to EN 10204 3.1 or 3.2.
Field reality: most premature chemical-equipment failures are weld or fabrication defects, not base-metal selection errors. Invest in the weld procedure qualification (WPS/PQR) and inspector before you invest in a more expensive grade.
Alloy Quick-Reference Table for Chemical Equipment
UNS numbers, family and the acids/equipment each grade is best known for. Use it to shortlist, then confirm with corrosion data.
Alloy (UNS)
Family
Best for
Max useful temp*
Hastelloy B2 (N10665)
Ni-Mo
HCl, dilute H₂SO₄
~370 °C
Hastelloy B3 (N10675)
Ni-Mo
HCl (better fab. than B2)
~370 °C
Hastelloy C22 (N06022)
Ni-Cr-Mo
H₂SO₄, mixed acids, chlorides
~650 °C
Hastelloy C276 (N10276)
Ni-Cr-Mo
Versatile oxidizing + chlorides
~650 °C
Hastelloy C4 / C2000 / G30
Ni-Cr-Mo
Specialized acid regimes
~650 °C
Alloy 20 (N08020)
Fe-Ni-Cr-Mo-Cu
H₂SO₄, H₃PO₄
~450 °C
Alloy 31 (N08031)
Fe-Ni-Cr-Mo-N
Aggressive H₂SO₄/H₃PO₄ + Cl⁻
~550 °C
Monel 400 / K500 (N04400/N05500)
Ni-Cu
HF, non-oxidizing acids
~480 °C
Nickel 200 / 201 (N02200/N02201)
Ni
HCl, HF, caustic
200/315 °C
Inconel 625 (N06625)
Ni-Cr-Mo-Nb
High-temp acid, reboilers
~650 °C
Incoloy 825 (N08825)
Fe-Ni-Cr-Mo-Cu
Sulfuric, phosphoric, seawater
~550 °C
904L (N08904)
Austenitic SS
Mild H₂SO₄, H₃PO₄
~400 °C
254SMO (S31254)
Super-austenitic
Chloride + mild acid
~400 °C
317L / 316L (S31703/S31603)
Austenitic SS
Mild acid, water, steam
~400 °C
2205 / 2507 (S32205/S32750)
Duplex / Super-duplex
Chloride + strength, seawater
~300 °C
*Indicative continuous-service ceiling for corrosion resistance; mechanical design limits under pressure are set by ASME Section VIII and may be lower.
Corrosion-Resistant Alloys We Supply for Chemical Equipment
All grades are available as pipe, tube, plate, sheet, bar, forging, flange and fitting, with mill test certificates and third-party inspection on request.
What is the best all-round alloy for chemical equipment?
There is no single best alloy. For broad oxidizing-acid service (sulfuric, phosphoric, mixed acids with chlorides) Hastelloy C276 or Alloy 31 are the most versatile. For strong reducing hydrochloric acid, Hastelloy B2/B3 or Nickel 200 are preferred. Always match the alloy to the specific acid, concentration and temperature — see the acid tables above.
Can 316L stainless steel be used in chemical equipment?
Yes, but only for mild duties: dilute sulfuric and phosphoric acid at low to moderate temperature, and neutral-to-mildly aggressive water/steam. 316L is attacked by hydrochloric acid and by hot concentrated sulfuric acid, so it is unsuitable for HCl service and aggressive acid concentration ranges.
Why is Monel used for hydrofluoric acid?
Monel 400 and K500 (nickel-copper alloys) resist hydrofluoric acid across a wide concentration and temperature range where most stainless steels and even many nickel-chromium alloys fail. A critical rule: avoid silicon-containing alloys in HF, because silicon accelerates attack.
What alloy should I use for a heat exchanger tube?
Choose based on the process fluid. For general corrosive service 904L, 254SMO or Alloy 20 tubing is common. For aggressive acids use Hastelloy C276 or B2/B3 seamless tubes. Thin walls demand alloys with good ductility (annealed condition) and sufficient corrosion allowance; tube sheets are often a heavier grade or explosively clad.
How do I select material for a distillation column?
Distinguish the overhead (cool, often condensing chlorides) from the bottoms/reboiler (hot, concentrated). Overhead and trays often use 316L, 904L or 254SMO; reboilers and hot concentrated sections use Hastelloy C276, Alloy 625 or Alloy 31. Packing and trays should match the most aggressive local environment.
What is the difference between Hastelloy B and C families?
The B family (B2, B3) is nickel-molybdenum with little chromium, optimized for reducing acids like hydrochloric and dilute sulfuric acid. The C family (C22, C276, C4, C2000, G30) is nickel-chromium-molybdenum, optimized for oxidizing acids, mixed acids and environments containing chlorides and wet process streams.
Is cladding a cost-effective option for reactors?
Often yes. For thick-wall pressure vessels, a carbon-steel or low-alloy base with an explosively welded or weld-overlaid corrosion-resistant alloy (Hastelloy C276, 625, 825, 904L) gives the needed corrosion resistance at a fraction of the solid-alloy cost. The overlay grade and thickness must meet the corrosion allowance and code requirements.
Which standards apply to chemical equipment alloys?
Common specs include ASTM B574/B575/B619/B622/B626 (Hastelloy), B127 (Monel), B162 (Nickel 200/201), B463/B464/B473 (Alloy 20), B625 (904L), B649 (Alloy 31), and ASME SB equivalents for pressure service. Pressure vessels also follow ASME Section VIII; some sour services require NACE MR0175/ISO 15156.
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