Views: 14 Author: Monica Publish Time: 2026-05-18 Origin: Site
By Monica | Reviewed by JN Alloy Materials Engineering Team | Published 2026-09-23 | Last updated 2026-09-23
Bottom line first: choose Hastelloy C276 when the dominant risk is chemical attack - sulfuric, hydrochloric or phosphoric acid, wet chlorine, mixed or contaminated process streams, and FGD scrubbers. Choose Inconel 625 when the dominant risk is mechanical or thermal - high-temperature strength above 600 C, creep, fatigue, seawater and marine structures, cryogenic LNG service, and weld overlay cladding onto carbon steel. If both risks are present and severe, the usual answer is neither compromise: use 625 as the structural or cladding layer and C276 as the wetted liner or the solid component in the most aggressive zone.
The two alloys solve different problems. Inconel 625 (UNS N06625) is a niobium-stabilised Ni-Cr-Mo alloy optimised for strength, fatigue life and high-temperature stability. Hastelloy C276 (UNS N10276) is a low-carbon Ni-Cr-Mo-W alloy optimised for broad-spectrum chemical resistance, especially in reducing acids. Everything else in this guide - composition, PREN, ASME allowables, cost - follows from that single difference in design intent.
A practical way to remember it: 625 is what you specify when the equipment must carry load at temperature or survive cyclic service; C276 is what you specify when the fluid is trying to dissolve the equipment. Where seawater and structural load combine, 625 dominates marine and offshore engineering. Where acids and chlorides combine, C276 dominates. See the complete Hastelloy C276 hub guide and JN Alloy's Inconel 625 guide for the acid-by-acid data behind that statement, or go straight to the Inconel 625 and Hastelloy C276 product pages for stock, sizes and quotes.
Both are nickel-based with chromium and molybdenum as the principal alloying additions, but the balance is inverted. 625 puts its budget into chromium (20-23%) plus niobium; C276 puts its budget into molybdenum (15-17%) plus tungsten, and holds carbon at 0.01% maximum. Niobium and tungsten are mutually exclusive here - 625 contains no tungsten, C276 contains no niobium - and that single contrast explains most of the performance gap.
| Element | Inconel 625 (UNS N06625) | Hastelloy C276 (UNS N10276) | Why it matters in service |
|---|---|---|---|
| Nickel (Ni) | 58.0 min (balance ~60) | Balance (~57) | Base matrix; provides inherent ductility and resistance to chloride stress-corrosion cracking |
| Chromium (Cr) | 20.0-23.0 | 14.5-16.5 | Higher Cr in 625 drives oxidation resistance above 600 C and passivation in nitric acid; lower Cr in C276 is traded for Mo |
| Molybdenum (Mo) | 8.0-10.0 | 15.0-17.0 | The single biggest differentiator. Mo is what makes C276 survive reducing acids and chloride pitting |
| Niobium + Tantalum (Nb+Ta) | 3.15-4.15 | None | Unique to 625. Stabilises against sensitisation, raises strength via gamma-double-prime, and enables cladding/dissimilar filler use |
| Tungsten (W) | None | 3.0-4.5 | Unique to C276. Reinforces Mo in reducing acids and improves resistance to localised attack |
| Iron (Fe) | 5.0 max | 4.0-7.0 | Residual/controlled element; kept low to avoid secondary phase formation |
| Carbon (C) | 0.10 max | 0.010 max | The ultra-low carbon in C276 is why it resists sensitisation in the weld HAZ without stabilisation |
| Cobalt (Co) | 1.0 max (if specified) | 2.5 max | Controlled for nuclear applications where Co-60 activation matters |
| Manganese / Silicon | 0.50 / 0.50 max | 1.0 / 0.08 max | Deoxidation and hot-workability control; C276 keeps Si very low to limit intermetallic precipitation |
There is no single winner, because corrosion resistance is specific to the medium. In reducing acids and chloride media Hastelloy C276 wins decisively. In strongly oxidising media and in hot oxidising gases Inconel 625 wins. In neutral seawater and sour gas both perform well, and the decision is then made on strength, fatigue and cost rather than corrosion. The matrix below is the fastest screening tool; the sections that follow explain the mechanism behind each row. If you are sizing reactors, columns or heat exchangers, the chemical process equipment page shows how these ratings translate into hardware.
| Corrosive medium | Inconel 625 | Hastelloy C276 | Engineering note |
|---|---|---|---|
| Seawater / neutral chlorides | Excellent | Excellent | Both far outperform 316L and duplex. 625 is preferred where load and fatigue matter; C276 where crevices and deposits exist |
| Hydrochloric acid (HCl) | Moderate | Superior | Mo + W in C276 is decisive. For hot concentrated HCl, Ni-Mo alloys (B-2/B-3) are usually specified instead |
| Sulfuric acid (H2SO4) | Moderate | Superior | C276 is the benchmark material for sulfuric acid service across most of the concentration range |
| Phosphoric acid (H3PO4) | Good | Excellent | C276 is widely used in phosphate fertilizer and wet-process phosphoric acid plants |
| Nitric acid (HNO3) | Good | Not recommended | Oxidising acid: higher Cr helps 625, while Mo-rich alloys such as C276 suffer in strongly oxidising media |
| Hydrofluoric acid / fluorides | Not recommended | Limited | Anhydrous HF calls for Monel 400. Aqueous HF duty must be coupon-verified for either alloy |
| Wet chlorine / chlorinated solvents | Good | Excellent | C276 is the long-standing industry standard for chlorinated organic processing |
| Mixed or contaminated acid streams | Good | Excellent | Unpredictable, multi-species streams favour C276's broad-spectrum resistance |
| Oxidising flue gas, above 600 C | Excellent | Poor | Above roughly 650 C, C276 loses strength and section stability; 625 is the correct choice |
| Sour gas (H2S + CO2) | Excellent | Excellent | Both are listed under NACE MR0175 / ISO 15156 for sour service |
| Caustic / strong alkali | Excellent | Good | High-nickel 625 resists caustic stress-corrosion cracking better than most stainless grades |
Acid-specific behaviour is where most specification errors happen, because engineers tend to reason from 'nickel alloy' rather than from the acid. The four cases below cover the great majority of chemical-process enquiries we receive.
Choose Hastelloy C276. Hydrochloric acid is a reducing, non-oxidising acid and it attacks the passive film aggressively; resistance scales with molybdenum and tungsten, not chromium. C276's 15-17% Mo plus 3-4.5% W is what makes it usable in HCl-containing pickle lines, chlorinated organic reactors and acidising environments, while Inconel 625's 8-10% Mo is generally insufficient except at low concentration and temperature. Important caveat: for hot, concentrated HCl, neither alloy is the right answer - the nickel-molybdenum alloys B-2 and B-3 are specified for that envelope. Always verify with an iso-corrosion diagram for your exact concentration and temperature.
Choose Hastelloy C276 in almost every case. C276 is one of the very few wrought alloys that covers a wide band of sulfuric acid concentrations and temperatures while also tolerating the chloride and oxidising contaminants that real plant acid always contains. Inconel 625 has usable resistance only in dilute, low-temperature sulfuric acid and is not normally specified for sulfuric service. If your acid is essentially chloride-free, moderate in concentration and below roughly 80 C, Alloy 20 (UNS N08020) is worth pricing as a lower-cost alternative to C276 - it was designed specifically for sulfuric acid.
Choose Hastelloy C276 for wet-process phosphoric acid. Real phosphoric acid carries fluoride, chloride, sulfate and often oxidising contaminants from the ore, and C276's combination of Mo and W handles that mixture far better than 625. This is why C276 is the standard material in phosphate fertilizer evaporators, digestors and acid transfer lines.
Choose Inconel 625. This is the one acid class where the ranking reverses. Nitric acid is strongly oxidising, and molybdenum-rich alloys are penalised in oxidising media - the Mo dissolves as molybdate rather than helping the passive film. Chromium is the element that matters here, and 625 carries 20-23% Cr against C276's 14.5-16.5%. The same logic applies to chromic acid, hot oxidising salts, and oxidising contaminants such as Fe3+ and Cu2+ in otherwise reducing streams: they shift the balance toward 625.
PREN (Pitting Resistance Equivalent Number) is the fastest way to rank alloys for chloride pitting, and it is honest about its own limits: it only predicts localised corrosion resistance in chloride media, and it says nothing about acid resistance or strength. Using the standard formula PREN = %Cr + 3.3 x %Mo + 16 x %N, Inconel 625 lands near 50 and Hastelloy C276 near 70. Adding the tungsten term commonly used for C-type alloys widens the C276 figure further.
| Indicator | Inconel 625 | Hastelloy C276 | Interpretation |
|---|---|---|---|
| PREN = %Cr + 3.3 x %Mo + 16 x %N | ~48-52 | ~68-73 | C276 holds a roughly 40 percent advantage in chloride pitting resistance |
| PREN with tungsten term: %Cr + 3.3 x (%Mo + 0.5 x %W) | ~48-52 (no W) | ~72-76 | The W in C276 strengthens the ranking further |
| Critical pitting temperature (CPT), ASTM G48 | Approximately 60-70 C | Approximately 85 C and above | C276 survives chlorides roughly 20-25 C hotter before pitting initiates |
| Critical crevice temperature (CCT), ASTM G48 | Lower than CPT; crevice-sensitive | Lower than CPT but still well above 625 | Where gaskets or deposits exist, design against CCT, not CPT |
| Chloride stress-corrosion cracking | Highly resistant | Highly resistant | Both are the standard upgrade from 316L when chloride SCC is the failure mode |
Two cautions. First, PREN over-simplifies nickel alloys: secondary phases, surface finish, welding and heat treatment all move the real number. Second, PREN ranks pitting - it is not a substitute for an acid iso-corrosion diagram when the medium is an acid rather than a neutral chloride solution. Use it as a screen, then confirm with ASTM G48 coupons on the welded condition you will actually ship.
Inconel 625, by roughly 10 percent on tensile and yield. Its niobium content produces gamma-double-prime strengthening in addition to solid-solution hardening, whereas Hastelloy C276 relies on solid-solution strengthening alone. C276 is the more ductile of the two, which is a genuine advantage in cold forming. Hardness is not a useful differentiator - the typical bands overlap, and published figures differ between sources depending on product form and temper.
| Property | Inconel 625 | Hastelloy C276 | Practical implication |
|---|---|---|---|
| Tensile strength | 827-930 MPa (120-135 ksi) | 690-790 MPa (100-115 ksi) | 625 carries roughly 10 percent more tensile load per unit area |
| Yield strength, 0.2% offset | 414-517 MPa (60-75 ksi) | 283-380 MPa (41-55 ksi) | 625 allows higher working stress at ambient temperature |
| Elongation at break | 30-45% | 40-60% | C276 is more ductile - easier tube bending, deep drawing and cold forming |
| Hardness | Typically 170-210 HB (~85-94 HRB) | Typically 170-200 HB (~84-90 HRB) | Bands overlap; do not select on hardness. Verify against the MTR for your heat |
| Density | 8.44 g/cm3 (0.305 lb/in3) | 8.89 g/cm3 (0.321 lb/in3) | C276 is about 5 percent heavier for the same volume - matters for weight-critical and long-span designs |
| Melting range | 1290-1350 C (2350-2460 F) | 1323-1371 C (2415-2500 F) | Similar; rarely a selection factor |
| Magnetic permeability | Essentially non-magnetic | Essentially non-magnetic | Both suitable for non-magnetic and certain nuclear/MRI-adjacent duties |
| Cryogenic behaviour, -196 C | Excellent toughness retained | Excellent toughness retained | Both are qualified for LNG and cryogenic service |
Inconel 625, and the gap widens with temperature. This is the second decisive difference after acid resistance. Above roughly 650 C, Hastelloy C276 loses strength rapidly and begins to form secondary phases that degrade both mechanical properties and corrosion resistance, whereas 625 retains useful creep-rupture strength and oxidation resistance well beyond that point. If your design metal temperature exceeds about 650 C under load, C276 should be excluded at the screening stage.
| Criterion | Inconel 625 | Hastelloy C276 | Engineering consequence |
|---|---|---|---|
| ASME Section VIII Div. 1 applicability limit | 649 C (1200 F) for SB-443 / SB-444 / SB-446 | 677 C (1250 F) for SB-575 / SB-622 / SB-574 | Within code limits C276 is listed slightly higher, but see the next row for load-bearing service |
| Load-bearing / creep-limited service above 650 C | Retains substantially higher creep-rupture strength | Strength falls away sharply; not normally recommended | For furnaces, gas turbines, exhaust and reformer internals, 625 is the correct choice |
| Oxidation resistance in air | Good to about 980 C (1800 F) | Useful to roughly 1040 C in air, but section loss and embrittlement limit practical use | Oxidation resistance alone does not qualify C276 for loaded high-temperature service |
| Carburisation / nitriding resistance | Good, helped by 20-23% Cr | Poor to moderate; not the usual choice | Petrochemical reformer and pyrolysis duties favour 625 or higher-Cr alloys |
| Thermal fatigue / cyclic service | Superior, helped by Nb-stabilised microstructure | Good at moderate temperature | 625 is the standard for risers, bellows, expansion joints and exhaust systems |
Chromium builds the protective oxide scale, and 625 has roughly 40 percent more of it. That single fact explains why 625 is specified for combustion liners, turbine shroud rings, exhaust ducting, industrial furnace fixtures and heat-treat baskets, while C276 is essentially absent from those applications. C276's strength in hot service is chemistry, not mechanics: it is excellent in hot wet acid and hot wet chlorine, but it is not an oxidation-resistant alloy in the load-bearing sense.
Both are readily weldable by GTAW, GMAW, SMAW and SAW, and neither normally requires post-weld heat treatment. Inconel 625 is the more forgiving of the two in production, because its niobium content stabilises the weld metal against carbide precipitation during cooling. Hastelloy C276 achieves the same freedom from sensitisation through ultra-low carbon, but it is more sensitive to heat input and to grain growth in the heat-affected zone, so it demands tighter procedure control.
| Factor | Inconel 625 | Hastelloy C276 |
|---|---|---|
| Matching filler metal | ERNiCrMo-3 (GTAW/GMAW), ENiCrMo-3 (SMAW) | ERNiCrMo-4 (GTAW/GMAW), ENiCrMo-4 (SMAW) |
| ASME Section IX P-Number | P-No. 43 | P-No. 43 (nickel-based family) |
| Post-weld heat treatment | Not normally required | Not normally required; solution anneal recommended for the most severe acid service |
| Sensitisation risk in the HAZ | Low - Nb stabilisation ties up carbon | Low - C held to 0.010% maximum |
| Heat-input sensitivity | Relatively tolerant | Tighter control needed; HAZ grain growth is the main risk |
| Role as a dissimilar-metal filler | ERNiCrMo-3 is the industry default for dissimilar joints and carbon-steel cladding | ERNiCrMo-4 used for C276-to-C276 and for C276 overlays |
| Welding to the other alloy | Both directions are weldable; ERNiCrMo-3 is the common choice | See the dedicated section below |
A point that surprises many engineers: Inconel 625 filler metal is used far more often than Inconel 625 base metal. ERNiCrMo-3 is the standard consumable for weld overlay cladding on carbon-steel vessels and pipelines, for joints between dissimilar alloys, and for buttering layers before C276 or other service alloys are deposited. If your project involves clad pipe, overlay, or dissimilar welds, 625 consumables will almost certainly be in the procedure.
Neither alloy is easy - both work-harden rapidly and both require rigid setups, carbide tooling and generous coolant. The differences are modest but real: C276's higher elongation makes it somewhat friendlier in cold forming, while 625's higher strength demands more forming force and often benefits from warm forming.
Both are supplied and used in the solution-annealed condition, and neither requires age hardening in standard grades. Getting the anneal and the quench right matters more than most fabricators expect, because a slow cool through the 550-1050 C range can precipitate secondary phases that quietly destroy corrosion resistance without visibly changing the material.
Both alloys are covered across every standard wrought form and are recognised by ASME, NACE and the major aerospace material specifications. The practical work is matching your product form to the right ASTM specification, then pulling the correct ASME allowable for that specification - allowables differ by form, temper and Division, so 'Inconel 625 allowable stress' is not a single number.
| Form / Standard | Inconel 625 | Hastelloy C276 |
|---|---|---|
| Plate, sheet, strip | ASTM B443, AMS 5599, ASME SB-443 | ASTM B575, ASME SB-575 |
| Bar, rod, wire | ASTM B446, AMS 5666, ASME SB-446 | ASTM B574, ASME SB-574 |
| Seamless pipe and tube | ASTM B444, B829, ASME SB-444 | ASTM B622, ASME SB-622 |
| Welded pipe and tube | ASTM B705, B775 | ASTM B626, B619, B775 |
| Forgings and flanges | ASTM B564, ASME SB-564, AMS 5666 | ASTM B564, ASME SB-564 |
| Buttweld fittings | ASTM B366, ASME SB-366 | ASTM B366, ASME SB-366 |
| ASME BPVC Section VIII | Div. 1 and Div. 2, to 649 C (1200 F) | Div. 1 and Div. 2, to 677 C (1250 F) |
| Sour service | NACE MR0175 / ISO 15156 compliant | NACE MR0175 / ISO 15156 compliant |
JN Alloy stocks both alloys across these forms. If you need flanges, see ASME SB564 Inconel 625 flanges and the complete guide to Hastelloy C276 flanges. For plate, see ASTM B443 UNS N06625 plate and sheet and the comprehensive analysis of Hastelloy C276 plate. For pipe and tubulars, Inconel 625 pipe and Hastelloy C276 pipe fittings are the relevant starting points.
For bar stock and machined parts, see Inconel 625 bar applications and Hastelloy C276 bar. For buttweld fittings, see ASTM B366 UNS N06625 fittings. For flanges machined to ASME B16.5, see ASTM B564 UNS N06625 flanges. Project reference: 41 tons of Inconel 625 pipe shipped to Malaysia.
Specifying from application precedent is often faster than specifying from data sheets, because the precedent already encodes decades of field corrections. The table below lists the duties where each alloy is the default choice.
| Industry | Inconel 625 - default choice | Hastelloy C276 - default choice |
|---|---|---|
| Chemical process | High-temperature reactors, caustic service, oxidising acid duty | HCl, H2SO4 and H3PO4 reactors, columns, heat exchangers, mixed-acid transfer lines |
| Oil and gas | Subsea wellheads, flexible risers, umbilicals, sour-gas tubulars | Sour and acidising environments, contaminated produced water, refinery overhead condensers |
| Power generation | Gas turbine exhaust, combustion liners, heat-recovery ducting | FGD absorber towers, scrubber ductwork, damper and outlet-duct linings |
| Marine and offshore | Propeller blades, seawater piping, mooring hardware, risers | Seawater contaminated with H2S, acid-wash and chemical-injection systems |
| Pharmaceutical and fine chemicals | High-temperature process steps, qualified 625 systems | Halogenated solvents, aggressive intermediates, multi-product reactors |
| Pulp and paper | Recovery boiler and digester components at temperature | Bleach plant equipment, chlorine dioxide stages, kraft digesters |
| Waste treatment and incineration | High-temperature incinerator internals | Scrubbers and quench systems handling unpredictable corrosive streams |
| Nuclear | Reactor core components, spent fuel storage, control rod components | Reprocessing and waste-evaporator acid streams (low-Co grades where specified) |
| Cryogenic / LNG | LNG tanks, piping and transfer systems to -196 C | Cryogenic acid or chloride-bearing process streams |
Hastelloy C276 typically carries a 15-20 percent price premium over Inconel 625 per kilogram, driven mainly by its higher molybdenum content and somewhat narrower mill base. That premium is real but it is frequently the wrong number to optimise, because it ignores density, wall thickness, fabrication hours and - above all - service life.
| Factor | Inconel 625 | Hastelloy C276 | Comment |
|---|---|---|---|
| Indicative plate price, USD/kg | 45-75 | 55-90 | C276 premium of roughly 15-20%; varies with Ni and Mo spot markets |
| Principal cost driver | Nickel and niobium | Nickel and molybdenum (plus tungsten) | Molybdenum is the more volatile and more expensive addition |
| Density effect | 8.44 g/cm3 - lighter per metre | 8.89 g/cm3 - about 5% heavier | On a per-metre pipe basis the C276 premium widens slightly |
| Mill availability and lead time | Broad - many qualified mills worldwide | Somewhat narrower sourcing base | 625 usually offers shorter lead times on common forms |
| Filler metal cost | ERNiCrMo-3, widely stocked | ERNiCrMo-4, widely stocked | Comparable; not a differentiator in most projects |
| Machining and forming cost | High (work hardening) | High (work hardening) | Similar; 625 needs more forming force, C276 needs tighter weld control |
| Service-life effect on TCO | Longest life where load, temperature or fatigue dominate | Longest life where chemical attack dominates | Correct alloy selection typically delivers 3-5x the service life of an underspecified alternative |
The TCO arithmetic is simple and it usually overwhelms the material premium. A heat exchanger bundle that fails in four years instead of twenty does not cost 20 percent more - it costs five replacement cycles, five shutdowns, and the associated lost production. That is why the decision should be framed as 'which alloy survives this specific environment', not 'which alloy is cheaper per kilogram'. If budget really is the binding constraint, and the medium is moderate, consider whether a lower alloy such as 904L stainless or Alloy 20 covers the duty at all - but never downgrade without coupon data.
Work through these steps in order. Steps 1 to 3 eliminate one alloy in most real projects, and step 8 is what protects you when the first seven leave genuine doubt.
Yes, and it is done routinely. Dissimilar joints between the two alloys are welded with ERNiCrMo-3 (Inconel 625 filler) or ERNiCrMo-4 (C276 filler); ERNiCrMo-3 is the more common choice because it is over-alloyed relative to both base metals and tolerates dilution well. Preheat is generally not required, but interpass temperature control matters, and for severe corrosion service a post-weld solution anneal should be evaluated. The critical point is procedural: qualify the WPS under ASME Section IX for the actual combination, and run ASTM G28 on a production-representative weldment if intergranular attack is a credible failure mode. The same logic applies when 625 is used as a buttering or cladding layer beneath a C276 deposit - control dilution on the first layer or the chemistry will drift out of specification.
Inconel 625, in most structural and dynamic applications. Both alloys resist seawater extremely well - both outperform duplex stainless steels and are far superior to 316L - so corrosion is rarely the deciding factor. What separates them is strength, fatigue resistance and the ability to survive cyclic loading in a chloride environment. Subsea wellheads, flexible risers, umbilicals, propeller blades, mooring hardware and seawater lift pumps are specified in 625 for exactly that reason. Choose C276 instead when the seawater is sour (H2S-contaminated), when acid-wash or chemical-injection cycles are part of the operating envelope, or when crevice corrosion under deposits and gaskets is the dominant risk. See JN Alloy's marine engineering page for the full application breakdown. For offshore and subsea nickel-alloy tubulars more broadly, see nickel alloy pipe for offshore service.
Both are compliant, so the question is usually answered on strength and temperature rather than on NACE status. Both Inconel 625 and Hastelloy C276 are listed under NACE MR0175 / ISO 15156 for sour service and both resist sulfide stress cracking in the qualified conditions. In practice, 625 is more commonly specified for downhole tubulars, wellhead components and subsea hardware where sour exposure combines with high stress and fatigue; C276 is specified where the sour stream is also acidic, chloride-laden or subject to acidising treatments. Always confirm the environmental severity limits and the required heat-treatment condition against the current edition of NACE MR0175 / ISO 15156 before finalising the material.
Sometimes neither alloy is the optimum. Three alternatives come up regularly in the same enquiries.
Working through both alloys in more depth first will pay off: start with the Hastelloy C276 introduction and everything you need to know about Hastelloy C276, then the complete Inconel 625 overview, before you commit to a specification.
Start from the failure mode you are trying to prevent. If the equipment is most likely to fail because it is being dissolved, specify Hastelloy C276 - it brings roughly 40 percent more pitting resistance, double the molybdenum, and the broadest chemical envelope of any widely available wrought alloy. If the equipment is most likely to fail because it is being stressed, cycled, or heated, specify Inconel 625 - it brings more strength, more fatigue life, niobium stabilisation for welding and cladding, and oxidation resistance to about 980 C. Where both failure modes are real, combine them: 625 as the structural or cladding layer, C276 as the wetted surface. And in every borderline case, spend the small amount required for ASTM G31 coupons in your actual process stream - it is the cheapest insurance available.
JN Alloy stocks both alloys in plate, sheet, bar, pipe, tube, flange and fittings with full material traceability, EN 10204 3.1 / 3.2 certification and PMI reports. Send us your medium, concentration, temperature, chloride content and design code and our materials engineers will return a side-by-side recommendation with a firm quotation.
Only in mild, dilute and low-temperature acid duty. In concentrated hydrochloric or sulfuric acid, Inconel 625 will corrode significantly faster because it carries roughly half the molybdenum of C276. Substituting 625 for C276 in a reducing-acid service without corrosion testing is one of the most common causes of premature failure. Always run ASTM G31 coupons in the actual process fluid at operating temperature before accepting a substitution.
No. At room temperature Inconel 625 has roughly 10 percent higher tensile and yield strength, and the gap in load-bearing capability widens further at elevated temperature. Hastelloy C276 is the more ductile alloy, with 40-60 percent elongation against 30-45 percent for 625, which makes it easier to cold form. Hardness is not a reliable differentiator because the typical bands overlap.
Inconel 625 for structural and dynamic marine components, because it combines excellent seawater corrosion resistance with higher strength and superior fatigue resistance - which is why it is specified for subsea wellheads, flexible risers, propeller blades and mooring hardware. Hastelloy C276 is preferred when the seawater is contaminated with H2S, when acid-wash or chemical-injection cycles are part of the duty, or when crevice corrosion under deposits and gaskets is the dominant risk.
Yes. Dissimilar welds between the two alloys are routine and are made with ERNiCrMo-3 (Inconel 625 filler) or ERNiCrMo-4 (C276 filler). ERNiCrMo-3 is the more common choice because it is over-alloyed relative to both base metals and tolerates dilution. Preheat is normally not required, but control interpass temperature and qualify the procedure under ASME Section IX for the actual combination.
Hastelloy C276 is generally preferred for pharmaceutical applications involving halogenated solvents, aggressive intermediates and multi-product reactors, because the campaign chemistry is often unknown in advance. Inconel 625 may be specified where elevated process temperatures are involved or where an existing regulatory filing already qualifies 625. Both alloys can be polished to cGMP surface-finish requirements.
Under ASME Section VIII Division 1, Inconel 625 (SB-443/444/446) is listed to 649 C (1200 F) and Hastelloy C276 (SB-575/622/574) to 677 C (1250 F). For load-bearing and creep-limited service above roughly 650 C, however, Inconel 625 is the correct choice because it retains far more creep-rupture strength and oxidation resistance, while C276 loses strength rapidly. Treat the code temperature as a documentation limit, not as a creep-strength endorsement.
Neither is easy. Both work-harden rapidly and need carbide tooling, positive rake angles, rigid setups and flood coolant. In practice Hastelloy C276 is marginally friendlier in cold forming thanks to its higher elongation, while Inconel 625 needs more forming force and often benefits from warm forming at 150-260 C. Machining cost is comparable and should not drive the selection.
Normally no. Inconel 625 avoids sensitisation through niobium stabilisation and Hastelloy C276 avoids it through ultra-low carbon (0.010% maximum), so neither needs the post-weld heat treatment that would risk sensitisation. A post-weld solution anneal is nonetheless recommended for C276 in the most severe acid service. Neither alloy requires the stress-relief cycles that can damage 316L weldments.
Hastelloy C276. FGD absorber towers, scrubber ductwork, dampers and outlet ducts operate at low pH with high chloride levels and wet-dry cycling, which is exactly the envelope C276 was developed to handle. Inconel 625 is used in FGD systems only where the temperature is high and the environment is oxidising, such as certain reheater and stack-liner locations, or as an ERNiCrMo-3 overlay on carbon steel.
Both are compliant, so the decision is made on mechanical grounds. Inconel 625 and Hastelloy C276 are both listed under NACE MR0175 / ISO 15156 for sour service and both resist sulfide stress cracking within their qualified limits. 625 is more commonly chosen for high-stress downhole and subsea hardware; C276 is chosen when the sour stream is also acidic, chloride-bearing or subject to acidising. Always confirm limits against the current standard edition.
No. Both Inconel 625 and Hastelloy C276 are austenitic nickel-base alloys and are essentially non-magnetic in the annealed condition. This matters for certain nuclear, instrumentation and non-magnetic tooling applications, and it is also a quick field check to distinguish nickel alloys from ferritic or martensitic steels.
Use ERNiCrMo-3 / ENiCrMo-3 for Inconel 625 and ERNiCrMo-4 / ENiCrMo-4 for Hastelloy C276, per AWS A5.14 and A5.11. ERNiCrMo-3 is also the default filler for dissimilar-metal joints and for cladding or buttering carbon steel, because it is over-alloyed and tolerates dilution. Match the filler to the more severe service condition when welding the two alloys together.
Mainly because of molybdenum. C276 contains 15-17 percent Mo plus 3-4.5 percent tungsten against 625's 8-10 percent Mo, and molybdenum is one of the more expensive and more volatile alloying elements. C276 also has a somewhat narrower mill base. In the market this typically shows up as a 15-20 percent premium per kilogram, and slightly more on a per-metre pipe basis because C276 is about 5 percent denser.
Generally not. Nitric acid is strongly oxidising, and molybdenum-rich alloys such as C276 perform poorly in oxidising media because molybdenum dissolves rather than contributing to the passive film. Inconel 625, with 20-23 percent chromium, is the better choice in nitric acid and other strongly oxidising environments. The same caution applies to chromic acid and to streams containing Fe3+ or Cu2+ contamination.
Inconel 625, by a wide margin. ERNiCrMo-3 is the industry-standard filler metal for overlaying carbon-steel pressure vessels, pipelines and FGD absorbers, because it tolerates dilution, resists hot cracking and delivers a corrosion-resistant surface at a fraction of the cost of solid alloy construction. C276 overlays are used where the service chemistry demands it, typically as a second layer over a 625 buttering pass to control dilution.
Using PREN = %Cr + 3.3 x %Mo + 16 x %N, Inconel 625 is roughly 48-52 and Hastelloy C276 roughly 68-73. Including the tungsten term commonly used for C-type alloys pushes C276 to about 72-76. That roughly 40 percent advantage is why C276 is the default for chloride pitting and crevice service, though PREN ranks pitting only and is not a substitute for acid corrosion data.
Both perform excellently at cryogenic temperatures and retain toughness down to -196 C, so either is technically viable. Inconel 625 is more commonly specified for LNG tanks, transfer lines and cryogenic piping because of its higher strength, proven toughness and broader code coverage for structural cryogenic components. C276 is chosen when the cryogenic stream is also corrosive, for example in acid-gas or chloride-bearing low-temperature processes.
Both alloys are already protected by design: 625 through niobium stabilisation and C276 through 0.010 percent maximum carbon. To keep that protection intact, control heat input and interpass temperature, avoid prolonged exposure in the 550-1050 C range, use low-heat-input stringer beads rather than wide weave passes, and buy material with a verified solution anneal and rapid quench on the mill certificate. For severe acid service, verify the welded condition with ASTM G28.
Specify UNS N06625 for Inconel 625 with ASTM B443 (plate/sheet), B444 (seamless pipe/tube), B446 (bar), B564 (forgings/flanges) or B366 (fittings), and the ASME SB- equivalent where code construction applies. Specify UNS N10276 for Hastelloy C276 with ASTM B575 (plate/sheet), B622 (seamless pipe/tube), B574 (bar), B564 (forgings/flanges), B626/B619 (welded pipe) or B366 (fittings). Add EN 10204 3.1 or 3.2 certification, full chemistry including Nb+Ta or Mo+W, solution-anneal records and PMI on every heat.
JN Alloy supplies Inconel 625 and Hastelloy C276 in plate, sheet, bar, pipe, tube, flange and fittings, with EN 10204 3.1 / 3.2 certification, full chemistry and mechanical test reports, solution-anneal records and PMI. Send your medium, concentration range, temperature, chloride content and design code and our materials engineers will return a side-by-side recommendation with a firm quotation.
| Term | Definition |
|---|---|
| PREN | Pitting Resistance Equivalent Number. PREN = %Cr + 3.3 x %Mo + 16 x %N; a tungsten-bearing variant adds half the tungsten to the molybdenum term. It ranks chloride pitting resistance only and says nothing about acid performance or strength. |
| CPT / CCT | Critical Pitting Temperature and Critical Crevice Temperature, measured per ASTM G48 in ferric chloride. CCT is typically 15-30 C lower than CPT and is the number that matters when gaskets, deposits or tube joints create crevices. |
| Niobium stabilisation | Adding niobium (3.15-4.15% in Inconel 625) so niobium carbides form instead of chromium carbides at grain boundaries. This suppresses sensitisation in the weld heat-affected zone and enables 625 to be used as a cladding and dissimilar-metal filler. |
| Sensitisation | Precipitation of chromium or molybdenum-rich phases at grain boundaries after exposure to roughly 550-1050 C, which depletes the adjacent matrix and causes intergranular corrosion. C276 avoids it with ultra-low carbon (<= 0.01%). |
| Weld overlay / cladding | Depositing a corrosion-resistant alloy onto a cheaper structural base metal by welding. ERNiCrMo-3 (Inconel 625) is the standard filler for overlaying carbon steel in refineries, chemical plants and FGD absorbers. |
| ASME allowable stress | The maximum stress permitted by ASME BPVC Section II Part D for a given alloy, product form and metal temperature. Always far below room-temperature tensile strength, and the real driver of wall thickness. |
| P-Number | An ASME Section IX grouping of base metals with similar weldability that reduces the number of welding procedure qualifications required. Inconel 625 is P-No. 43; Hastelloy C276 is also in the nickel P-No. 43 family. |
| Solution anneal | Heating into the single-phase region to dissolve secondary precipitates, then rapid cooling. Inconel 625: 1093-1177 C (2000-2150 F). Hastelloy C276: 1121-1177 C (2050-2150 F), water quench. |
| Sour service | Oil and gas service containing hydrogen sulfide above NACE MR0175 / ISO 15156 thresholds, requiring materials qualified against sulfide stress cracking. Both 625 and C276 are listed for sour service. |
| FGD | Flue Gas Desulfurization. The scrubbing system that removes SO2 from boiler exhaust; a low-pH, high-chloride, wet-dry cycling environment where Hastelloy C276 is the long-standing benchmark material. |
| Dilution (in overlay) | The fraction of base metal melted into the first weld layer. Uncontrolled dilution can pull the deposit chemistry out of specification, which is why many overlay procedures specify a first layer of 625 followed by the service alloy. |
| EN 10204 3.1 / 3.2 | Mill test certificate levels. 3.1 gives measured values validated by the manufacturer's independent inspection representative; 3.2 adds third-party or purchaser-representative validation. |
| PMI | Positive Material Identification. Portable XRF or optical emission spectroscopy used on received material to confirm grade before it enters fabrication. |
| ASTM G28 | Standard test methods for detecting susceptibility to intergranular corrosion in wrought nickel-rich chromium-bearing alloys. Method A uses ferric sulfate-sulfuric acid; Method B uses a mixed oxidising acid salt solution. |
| ASTM G48 | Standard test methods for pitting and crevice corrosion resistance in ferric chloride; used to report CPT and CCT. |
| ASTM G31 | Standard guide for laboratory immersion corrosion testing of metals; the basis of plant-specific coupon programmes. |