Precision Forged Flanges & Fittings - Built for Global Markets

Forged Flanges & Fittings for Petrochemical Industry

Heat-resistant, hydrogen-service, and corrosion-resistant flanges for refineries, chemical plants, and LNG terminals. Full ASME B31.3 compliance, EN 10204 3.1 MTC, and complete material traceability.

Petrochemical Sector: Where Chemistry Meets Extreme Conditions

Petrochemical and refinery plants process crude oil, natural gas, and chemical feedstocks under a wide range of temperatures (-196°C to 650°C), pressures (vacuum to 300 bar+), and highly corrosive media — from concentrated acids to hydrogen-rich streams.

JIAJI FORGING has supplied flanges and fittings to refinery EPC projects, chemical plant turnarounds, and LNG infrastructure across Asia, the Middle East, and Europe. Our products comply with the most demanding process industry standards including ASME B31.3, PED 2014/68/EU, and NACE MR0175.

Unlike the oil & gas sector which focuses on API wellhead pressure ratings, petrochemical applications demand precise material compatibility with process fluids: sulfuric acid, hydrofluoric acid, amines, chlorides, and high-partial-pressure hydrogen. Material selection is often driven by corrosion allowance calculations to ASME B31.3 Appendix A.

Key Sectors Served

  • Crude Oil Refining (ADU / VDU / FCC / Hydrocracker)
  • Petrochemical Complexes (Ethylene, Propylene, Aromatics)
  • Fertilizer & Ammonia Plants (Urea, Nitric Acid)
  • LNG Import / Export Terminals
  • Specialty Chemical Plants (Acids, Polymers, Solvents)
  • Industrial Gas Separation Units (ASU / PSA)
-196°C
LNG Cryogenic Capability
650°C
High-Temp Alloy Range
ASME
B31.3 Process Piping
EN 3.1
MTC Traceability

Flanges Across Refinery & Chemical Process Units

Different process units impose unique demands on flange material, pressure class, and face type

🏭

Atmospheric & Vacuum Distillation

ADU / VDU / Crude Preheat Train

The primary crude distillation unit processes up to 400,000 BPD at temperatures up to 380°C. The vacuum distillation column operates at sub-atmospheric pressures, requiring tight flange sealing to prevent air ingress.

Process Conditions

  • Temperature: 260–380°C (ADU), up to 420°C (VDU)
  • Pressure: 1–35 bar (ADU), sub-atmospheric (VDU)
  • Naphthenic acid corrosion above 230°C
  • H₂S in overhead and sour water systems

Recommended Materials

  • 316L / 316Ti for naphthenic acid service
  • F51 duplex for overhead sour water
  • LF2 carbon steel for low-temp sections
⚗️

Hydroprocessing Units

Hydrocracker / Hydrotreater / Reformer

Hydrogen-rich, high-pressure service is among the most demanding for flanges. H₂ partial pressure above 7 bar requires materials qualified against Nelson Curves (API RP 941) to prevent hydrogen embrittlement and HTHA.

Process Conditions

  • Temperature: 300–450°C
  • H₂ partial pressure: 50–200 bar
  • High-pressure hydrogen embrittlement risk
  • HTHA (High Temperature Hydrogen Attack)

Recommended Materials

  • F22 (2¼Cr-1Mo) — Nelson Curve A/B
  • F91 (9Cr-1Mo-V) for high-temp high-H₂
  • 316 / 321H austenitic for hot piping
🧪

Amine Treatment & Sulfur Recovery

DEA / MDEA Absorbers, Claus Tail Gas

Amine treating units remove H₂S and CO₂ from hydrocarbon gas streams. Wet H₂S environments with amines create stress corrosion cracking (SCC) risk for carbon steel; austenitic stainless or duplex are preferred.

Process Conditions

  • H₂S + CO₂ + amine environment
  • NACE MR0175 / ISO 15156 requirements
  • Lean amine: 100–130°C, Rich amine: 40–60°C
  • Polythionic acid SCC risk during shutdown

Recommended Materials

  • 316L / 317L for amine units
  • F51 duplex for wet H₂S service
  • Inconel 825 for aggressive mixed environments
🧊

LNG & Cryogenic Service

LNG Terminals, ASU, NGL Fractionation

Liquefied natural gas at -162°C imposes severe toughness demands on flange materials. Charpy impact testing at -196°C is standard for austenitic grades; special attention to bolting material at low temperature is required.

Process Conditions

  • Design temperature: -162°C (LNG) to -196°C (N₂)
  • High purity service — no contamination
  • Thermal cycling: cryogenic to ambient
  • BS 6364 / EN 1089-3 cryogenic testing

Recommended Materials

  • F304L / F316L austenitic (Charpy at -196°C)
  • F304 / F316 for -162°C LNG service
  • Invar 36 for ultra-low temp expansion joints

Acid Alkylation & Chemical Reactors

HF Alkylation, H₂SO₄ Alkylation, Acid Plants

Hydrofluoric acid alkylation units require Monel 400 for HF resistance. Sulfuric acid plants operate with concentrated H₂SO₄ (95–98%) at temperatures up to 450°C in the SO₃ converter.

Process Conditions

  • HF acid: Monel mandatory (alloy K500 for valve trim)
  • H₂SO₄ (>70%): carbon steel acceptable
  • Dilute H₂SO₄ / wet SO₂: 316L or Hastelloy
  • Strict fugitive emission requirements (API 624)

Recommended Materials

  • Monel 400 (N04400) for HF service
  • Hastelloy C276 for wet SO₂ / mixed acids
  • 316L for dilute acid environment
🔬

Ethylene & Olefin Plants

Steam Crackers, Quench Towers, Compression

Steam cracker furnaces operate at 850–900°C with mixed steam/hydrocarbon feed. The quench section involves rapid cooling from 900°C to below 400°C with acidic condensate. Compression trains require fatigue-rated flanges.

Process Conditions

  • Cracking temperature: 850–900°C (furnace tubes)
  • Transfer Line Exchanger (TLE): severe thermal shock
  • Quench oil: 200–400°C with fouling
  • Cold section: ethylene / propylene to -104°C

Recommended Materials

  • F347H (321H) for quench oil headers
  • HP alloy for furnace coil flanges
  • F304L for cold section refrigerant lines

Materials for Petrochemical & Chemical Service

Material selection for petrochemical flanges is driven by process fluid chemistry, temperature, and relevant design codes

🔷

316L / 316Ti — General Chemical Service

ASTM A182 F316L / EN 1.4404 / 1.4571

  • Excellent resistance to dilute acids
  • Chloride environments up to ~60°C
  • Naphthenic acid corrosion resistance
  • 316L (L = low carbon) for weld-adjacent service

316Ti (1.4571) for sensitization-prone high-temp service

💎

Duplex 2205 / 2507 — Sour & Chloride

ASTM A182 F51 / F53 (EN 1.4462 / 1.4410)

  • PREN ≥ 35 (2205) / ≥ 43 (2507)
  • Wet H₂S + chloride environments
  • 3× the yield strength of 316L
  • Cost-effective vs. nickel alloys

2507 preferred for seawater cooling, offshore utilities

🔥

F321H / F347H — High-Temperature

ASTM A182 F321H / F347H (EN 1.4541 / 1.4550)

  • Stabilized austenitic for 400–650°C service
  • Prevents intergranular corrosion (sensitization)
  • Refinery furnace outlets, superheater piping
  • Polythionic acid SCC resistant

H grade (high carbon) for elevated temperature creep strength

Hastelloy C276 — Aggressive Corrosion

Alloy N10276 (EN 2.4819)

  • Best-in-class resistance: HCl, H₂SO₄, HF, chlorides
  • Wet SO₂, flue gas desulfurization
  • Organic acid, mixed-acid environments
  • Chloride-induced pitting and crevice corrosion

Hastelloy B3 (N10665) for HCl/reducing acid service

🛡️

Monel 400 — HF & Seawater

Alloy N04400 (EN NiCu30Fe)

  • Only alloy immune to HF acid stress corrosion
  • HF alkylation units (UOP / Stratco process)
  • Seawater heat exchangers, desalination
  • Caustic/alkali environments

Monel K500 for higher strength HF service (valve spindles)

🧊

304L / 316L (Cryogenic) — LNG Service

ASTM A182 F304L / F316L (EN 1.4307 / 1.4404)

  • Austenitic FCC structure remains ductile at -196°C
  • Charpy impact test at design temperature
  • BS 6364 and EN 1092-1 Annex E cryogenic qualification
  • LNG, LOX, LN₂, LAr cryogenic service

Min. Charpy at -196°C: 27 J avg / 20 J individual

Petrochemical Material Quick Reference (EN Designations)

EN Designation Mat. No. ASTM Grade Petrochemical Application
X2CrNiMo17-12-2 1.4404 316L General chemical service, welds, ADU overhead
X6CrNiMoTi17-12-2 1.4571 316Ti Naphthenic acid, high-temp process piping
X6CrNiTi18-10 1.4541 321H Refinery furnace outlets, sensitization protection
X6CrNiNb18-10 1.4550 347H High-temp steam cracker outlets, quench headers
X2CrNiMoN22-5-3 1.4462 F51 (2205) Sour gas, H₂S + chlorides, amine units
X2CrNiMoN25-7-4 1.4410 F53 (2507) Aggressive chloride, seawater cooling, offshore
NiMo16Cr15W 2.4819 Hastelloy C276 Wet SO₂, mixed acids, FGD systems
NiCu30Fe 2.4360 Monel 400 HF alkylation, seawater, caustic

Petrochemical Design Codes & Compliance

JIAJI FORGING products are manufactured and documented to meet the standards demanded by EPC contractors and plant operators

📐

ASME B31.3

Process Piping Code. The dominant standard for refinery and chemical plant piping design and fabrication worldwide.

📐

ASME B16.5 / B16.47

Pipe Flanges and Flanged Fittings, NPS 1/2 to 60". Classes 150–2500 LB. Dimensional and pressure-temperature rating standard.

🇪🇺

PED 2014/68/EU

EU Pressure Equipment Directive. CE marking available for European refinery and chemical plant projects.

🏅

ISO 9001:2015

Quality Management System. Documented process control from raw material receipt through final inspection and dispatch.

🧪

NACE MR0175 / ISO 15156

Sour Service Qualification. Materials tested and approved for H₂S-containing environments in refinery and gas treatment units.

📜

EN 10204 3.1 / 3.2

Material Test Certificates. Type 3.1 (mill) or 3.2 (independent notified body) certification supplied with every order.

🔬

API RP 941

Nelson Curves for hydrogen service. Flange materials selected to avoid HTHA (High Temperature Hydrogen Attack) in hydroprocessing units.

🛢️

BS 6364 / EN 1089-3

Cryogenic Valve and Equipment Testing. Required for LNG terminal, ASU, and cryogenic separation plant flanges.

Frequently Asked Questions

ASME B31.3 and ASME B16.5 specify several face types for different service conditions:

  • Raised Face (RF): Standard for Class 150–2500 LB, most process piping service. Gasket confined to raised face bore area. Most common in refineries.
  • Ring Type Joint (RTJ): Preferred for Class 900 LB and above, high-pressure, high-temperature service (>300°C / 100 bar+). Metal ring seal, superior leak integrity.
  • Flat Face (FF): Used with cast iron or non-metallic flanges and low-pressure utility systems. Rarely used in process piping.
  • Tongue & Groove (T&G): Used in heat exchanger nozzles and where full gasket confinement is required.

For cryogenic service (LNG), RTJ or double-jacketed spiral-wound gaskets in RTJ grooves are preferred to maintain sealing integrity during thermal cycling.

API RP 941 (Nelson Curves) defines the boundary conditions above which carbon and low-alloy steels are susceptible to HTHA (High Temperature Hydrogen Attack — irreversible decarburization and fissuring). Selection process:

  1. Determine the H₂ partial pressure (bar) and operating temperature (°C)
  2. Plot on the Nelson Curve chart for the target material. The operating point must be below the curve by the required safety margin.
  3. Carbon steel: typically safe below 230°C / H₂ PP <7 bar
  4. 1¼Cr-½Mo (F11): extends safe zone to ~310°C
  5. 2¼Cr-1Mo (F22): extends to ~370°C — standard for hydrocrackers
  6. 9Cr-1Mo-V (F91): for the most severe HTHA conditions to ~450°C

Note: Austenitic stainless steels (316, 321H, 347H) are not subject to HTHA and are used in hot H₂ piping above the Nelson Curve boundaries for alloy steels.

LNG service flanges require special qualification beyond standard mechanical testing:

  • Charpy V-notch impact test: at design minimum temperature (-162°C for LNG, -196°C for LOX/LN₂). Minimum 27 J average, 20 J individual (per EN 1092-1 / ASME requirements)
  • Cryogenic tensile test: Yield and tensile strength at design temperature. Austenitic steels gain strength at low temperature.
  • BS 6364 / EN 1089-3: Specifies testing conditions for cryogenic valves and accessories including flanges
  • Ferrite content measurement: For austenitic stainless, FN ≤ 8 per WRC-1992 diagram (excess delta ferrite can become magnetic and brittle at cryogenic temperatures)
  • Helium leak test: For LNG terminal flanged joints to API 598 or equivalent

All test records are traceable to heat / lot number and supplied as part of the EN 10204 3.1 documentation package.

Polythionic Acid Stress Corrosion Cracking (PTA-SCC) is a form of intergranular cracking that can occur in sensitized austenitic stainless steel exposed to polythionic acids (H₂SₓO₆) during shutdown and maintenance. The mechanism:

  • Sensitization occurs when austenitic steel operates between 425–850°C — chromium carbides precipitate at grain boundaries, depleting adjacent zones of Cr protection
  • During shutdown, moisture + residual sulfur deposits form polythionic acids that attack the sensitized grain boundaries
  • Susceptible grades: 304, 304H, 316, 316H — sensitized by service or welding
  • Resistant grades: 321, 321H, 347, 347H (Nb/Ti stabilized — prevent carbide precipitation)

JIAJI recommends F347H or F321H flanges for all refinery furnace outlet and high-temperature piping applications where sensitization is a risk. Per ASTM A262 Practice E / ASTM A193/A194 bolt material requirements for polythionic acid service.

Yes. JIAJI FORGING manufactures forged flanges in Hastelloy C276 (UNS N10276 / EN 2.4819) as both ASME B16.5 and EN 1092-1 configurations:

  • Standards: ASTM B564 (bar/forging stock), ASTM B574 (rod), ASTM B575 (plate)
  • Available types: Weld Neck, Blind, Slip-On, Threaded, Socket Weld (all ASME B16.5 classes)
  • Certification: EN 10204 3.1 MTC, PMI (XRF analysis), IGC test (ASTM G28 Method A/B)
  • Lead time: 6–12 weeks depending on stock availability and size

Typical applications include flue gas desulfurization (FGD), wet SO₂ scrubbers, chloride-containing chemical reactors, and organic acid service in specialty chemical plants.

For European projects under the Pressure Equipment Directive (PED 2014/68/EU), our standard documentation package includes:

  • CE Declaration of Conformity (DoC)
  • EN 10204 Type 3.1 Material Test Certificate (by notified body for 3.2)
  • Proof of conformity to EN 1092-1 (flanges) or ASME B16.5 with PED material equivalence
  • Certificate of conformance to PED Module H1 or D1 (as applicable)
  • Design calculation or documentation of pressure-temperature ratings
  • Quality plan and inspection test plan (ITP)
  • PMI certificates (XRF/OES analysis)
  • Weld procedure qualification record (WPS/PQR) if welded items

Additional documentation per Shell DEP, BP GIS, or Total GS standards available on request. We work with third-party inspection agencies (Bureau Veritas, Lloyd's, SGS, TÜV) as required by project specifications.

Flanges for Petrochemical Applications

The most commonly specified flange and fitting types for refinery and chemical plant projects

Need Petrochemical Flanges or Fittings?

Share your process conditions, design code, and material specification. We respond within 24 hours with a technical assessment and competitive quotation.

📞 +86-21-60708463  |  ✉️ market@jiajiforging.com  |  🌍 Export Office: Shanghai, China