API 6A Material Classes: How Nickel Alloys Meet HH-NL Requirements

Jul 17, 2026

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Lucy Yang
Lucy Yang
International Business Developer at Jinie Technology, focusing on expanding global markets for stainless steel and nickel alloy products. Skilled in cross-cultural communication and strategic partnerships.

Why API 6A Material Classes Matter for Oil & Gas Equipment

 

API 6A material classes (AA through HH) define the temperature-environment envelope and required material group for wellhead and Christmas tree equipment. Class HH is the highest rating, requiring nickel-based corrosion-resistant alloys (CRA) such as Inconel 625 and Hastelloy C276 to withstand the most aggressive sour gas conditions, including high H₂S concentrations, elevated temperatures up to 180 °C, and high chloride content. The suffixes "L" (low temperature, to −46 °C) and "N" (normalized) further define the operating envelope. Specifying the correct material class is not optional - it is a safety-critical engineering and regulatory requirement.

 

API 6A Material for Oil Gas Equipment

 

In sour gas and high-pressure oilfield applications, a single wrong material choice can cause catastrophic equipment failure: sulfide stress cracking (SSC), stress corrosion cracking (SCC), pitting, or hydrogen-induced cracking (HIC) can lead to well blowouts, environmental spills, and loss of life. API 6A (ISO 10423) provides the definitive framework for specifying wellhead equipment, and its material class system is the primary tool for matching material capability to service environment.

[Source] API Specification 6A, 21st Edition (2018), "Specification for Wellhead and Christmas Tree Equipment," Annex F - Material Requirements.

 

What Are the API 6A Material Classes and What Do They Cover?

 
Seven Material Classes: AA to HH
 

API 6A defines seven material classes - AA, BB, CC, DD, EE, FF, and HH - ordered from lowest to highest corrosion resistance and temperature rating. Classes AA through FF are based on carbon and low-alloy steels with progressively stricter controls on chemistry, hardness, and heat treatment. Class HH is exclusively for nickel-based corrosion-resistant alloys (CRA) and represents the most severe service conditions. The suffix "L" (as in "DD-L", "EE-L", "FF-L", "HH-L") denotes low-temperature service down to −46 °C (−51 °F).

 

Material Class

Material Group

Max Temperature

Typical Application / Environment

AA

Carbon Steel (min. S, P control)

-29°C to +121°C

Non-sour, low-pressure conventional wells

BB

Carbon Steel (tighter chemistry)

-29°C to +121°C

Non-sour, moderate-pressure wells

CC

Carbon / Low Alloy Steel

-29°C to +121°C

Non-sour, higher-pressure service

DD

Carbon / Low Alloy Steel + SSC req.

-46°C to +121°C

Mild sour gas, low H₂S (<3%), CO₂

DD-L

Carbon / Low Alloy Steel (L-suffix)

−46°C to +121°C

Mild sour gas, low-temperature service

EE

Carbon / Low Alloy Steel (higher class)

-29°C to +180°C

Moderate sour gas, higher temperature

EE-L

Carbon / Low Alloy Steel (L-suffix)

−46°C to +180°C

Moderate sour gas, cold environments

FF

Carbon / Low Alloy Steel + NACE MR0175

-29°C to +180°C

Severe sour gas, H₂S up to 10%, NACE-qualified

FF-L

Carbon / Low Alloy Steel (L-suffix)

−46°C to +180°C

Severe sour gas, cold environments

HH

Nickel-Based CRA (Inconel 625, C-276)

-29°C to +180°C

Most severe sour gas, high H₂S, high Cl⁻, high temp

HH-L

Nickel-Based CRA (L-suffix)

−46°C to +180°C

Most severe sour gas, cryogenic to 180°C range

NN

Normalized / N&T Carbon Steel

-29°C to +121°C

Non-sour, conventional wells (legacy designation)

[Source] API 6A, 21st Edition, Annex F, Table F.1 - Material classes and service conditions. Temperature ratings per Annex F; actual limits depend on specific PSL and material group.

 

How the Temperature-Environment Matrix Works

 

The material class is selected by matching the service conditions to the class requirements. The two key variables are:

 

  • Temperature: Temperature: ambient conditions and fluid temperature at the wellhead
  • Environment: H₂S concentration (partial pressure), CO₂ concentration, and chloride (Cl⁻) content

 

As temperature rises or H₂S/CO₂ concentration increases, the required material class steps up from AA toward HH. Once temperature exceeds 121 °C (250 °F), only EE, EE-L, FF, FF-L, HH, and HH-L are eligible. For the most aggressive sour gas environments - particularly those with high chloride content and temperatures above 150 °C - Class HH nickel alloys become the only technically valid choice.

 

[Source] API 6A, 21st Edition, Annex F, Clause F.2 - Service condition limits for material classes.

 

What Makes Sour Gas Environments So Aggressive?

 

Hydrogen sulfide (H₂S) dissolves in produced water to form weak acid, which dissociates into H⁺ and HS⁻ ions. The H⁺ atoms diffuse into steel lattice, recombine as H₂ gas at internal defects, and generate massive internal pressure that causes hydrogen-induced cracking (HIC) and sulfide stress cracking (SSC). CO₂ dissolves to form carbonic acid (H₂CO₃), which aggressively attacks steel, causing uniform thinning, pitting, and galvanic corrosion at weld seams. Nickel alloys resist these mechanisms because their high Ni content (≥58%) is immune to SSC and their high Cr/Mo/W content passivates the surface against acid attack.

 

What Makes Sour Gas Environments So Aggressive

 

Failure Mechanism

Primary Driver

Affected Materials

Nickel Alloy Advantage

Sulfide Stress Cracking (SSC)

H₂S + tensile stress + susceptible microstructure

Carbon/Low Alloy steel >HRC 22

Ni≥58% = immune to SSC

Hydrogen-Induced Cracking (HIC)

H₂S + pressure + inclusions/microstructure

Carbon steel with MnS inclusions

Austenitic structure = no HIC

Stress Corrosion Cracking (SCC)

Chloride + tensile stress + temperature

316L SS at >60°C in seawater

Ni≥58% = immune to chloride SCC

Pitting Corrosion

Cl⁻ + oxidizer + temperature

All stainless steels below CPT

PREN >48 = no pitting in most oilfield conditions

Uniform Acid Attack

H₂SO₄ / HCl / H₂CO₃

Carbon steel, 316L

Cr-Mo passivation = negligible uniform rate

Galvanic Corrosion

Dissimilar metals + electrolyte

Carbon steel in contact with SS

CRA selected for full wetted components

[Source] NACE MR0175 / ISO 15156-1:2020, Clause 4 - Failure mechanisms in H₂S-containing environments. Haynes International, "Corrosion in Oil and Gas Production."

 

What Is the H₂S Threshold for Requiring Class HH?

 

There is no single H₂S threshold that universally triggers Class HH. The material class is determined by the combined effect of H₂S partial pressure, CO₂ partial pressure, chloride concentration, temperature, and in-situ pH - as defined in NACE MR0175 / ISO 15156-3. In general, Class HH nickel alloys are specified when: (1) H₂S partial pressure exceeds the limits for FF-class materials, (2) temperature exceeds 150 °C in sour service, (3) chloride concentration exceeds 50,000 ppm in sour service, or (4) the environment contains elemental sulfur (which accelerates SSC even at low H₂S levels).

 

API 6A does not provide a direct lookup table from H₂S% to material class. Instead, engineers use the ISO 15156-3 Annex A methodology, which plots the combination of H₂S partial pressure, CO₂ partial pressure, chloride concentration, and in-situ pH on an environmental severity diagram. For design reference, the following table provides approximate service conditions typically associated with Class HH:

 

Parameter

Typical Class HH Trigger Condition

Notes

H₂S Concentration

>5% (v/v) in gas phase

Or H₂S partial pressure > 0.05 bar

CO₂ Concentration

>3% (v/v) in gas phase

Or CO₂ partial pressure > 0.5 bar

Chloride (Cl⁻)

>50,000 ppm in produced water

Accelerates SCC and pitting

Temperature

>150 °C at wellhead Christmas tree

Exceeds FF-class limits

Elemental Sulfur (S₀)

Present in formation fluid

Severely lowers SSC threshold

pH (in-situ)

< 4.0 in aqueous phase

Increases general acid corrosion rate

Stress Level

Near-yield strength (weld residual + applied)

Critical for SSC initiation

Combined Severity

Any two or more of above at high levels

ISO 15156-3 severity diagram

[Source] NACE MR0175 / ISO 15156-3:2020, Annex A - Environmental severity boundaries. API 6A, 21st Edition, Annex F.

 

What Exactly Does API 6A Require for Class HH Materials?

 
What Exactly Does API 6A Require for Class HH Materials
 

Material Group and Alloy Requirements

 

API 6A Class HH mandates nickel-based corrosion-resistant alloys (CRA) as the primary material group. The most widely accepted and stocked alloys are Inconel 625 (UNS N06625 / W.Nr. 2.4856) and Hastelloy C276 (UNS N10276 / W.Nr. 2.4819). Both alloys must comply with the relevant ASTM product specifications (ASTM B564 for forgings, B443 for plate/sheet, B622 for seamless pipe, B574 for bar) and must be qualified for sour service per NACE MR0175 / ISO 15156-3. Carbon and low-alloy steels are explicitly prohibited for HH-class components in sour service.

 

Requirement

Inconel 625 (N06625)

Hastelloy C-276 (N10276)

Standard / Method

Min. Nickel Content

58–63%

57% (balance)

ASTM B443 / B564

Min. Chromium

20.0%

14.5%

ASTM B443 / B564

Min. Molybdenum

8.0%

15.0%

ASTM B443 / B564

Max. Carbon (≤)

0.10% (Gr1), 0.15% (Gr2)

0.01%

ASTM B443 / B564

Max. Silicon (≤)

0.50%

0.08%

ASTM B443 / B564

PREN (calculated)

≈42 (Cr + 3.3×Mo + 16×N)

≈48–52 (incl. W)

ASTM G48

Max. Hardness

HRC 40 (forgings)

HRC 40 (forgings)

ASTM E18

Sour Service Qualification

ISO 15156-3 qualified

ISO 15156-3 qualified

NACE MR0175 / ISO 15156-3

Charpy Impact (min)

54 J at RT (transverse)

54 J at RT (transverse)

ASTM E23

Solution Annealing

1093–1171 °C, WQ or AC

1121–1171 °C, WQ

ASTM B443 / B564

PMI Verification

Mandatory (XRF)

Mandatory (XRF)

API 6A PSL3 requirement

[Source] ASTM B443-22 (Inconel 625 plate/sheet), B564-22 (Nickel alloy forgings), B574-22 (Nickel alloy bar), B622-22 (Seamless pipe); NACE MR0175 / ISO 15156-3:2020.

 

Temperature Ratings: HH vs HH-L

 

Class HH: Standard temperature rating from −29 °C to +180 °C (the maximum rating in API 6A).

 

Class HH-L: Extended low-temperature rating from −46 °C to +180 °C, required for Arctic and offshore subsea applications where ambient temperatures drop below −29 °C. The "L" suffix imposes additional impact testing requirements (Charpy V-notch at −46 °C, minimum 54 J transverse) and may require special heat treatment to achieve the required toughness at cryogenic temperatures while maintaining corrosion resistance at the upper end of the range.

 

Class

Temp. Min

Temp. Max

Low-Temp Impact Test

Typical Use Case

HH

−29°C (−20°F)

+180°C (356°F)

54 J at RT (transverse)

Onshore sour gas, high-temp wells

HH-L

−46°C (−51°F)

+180°C (356°F)

54 J at −46°C (transverse)

Arctic onshore, offshore subsea Xmas trees

[Source] API 6A, 21st Edition, Annex F, Clause F.4 - Low-temperature service ratings.

 

Which Nickel Alloys Qualify for API 6A Class HH?

 

Which Nickel Alloys Qualify for API 6A Class HH

 

Inconel 625 vs Hastelloy C-276: Which Should You Choose?

 

Both Inconel 625 (UNS N06625) and Hastelloy C-276 (UNS N10276) are API 6A Class HH-qualified and NACE MR0175 / ISO 15156-3 compliant. Inconel 625 is the default choice for most API 6A wellhead and Christmas tree applications due to its superior fabricability, established track record, and excellent strength at high temperature (up to 980 °C).

 

Hastelloy C276 is preferred when the environment contains concentrated hydrochloric acid (HCl), high chloride at elevated temperature, or elemental sulfur - conditions where Inconel 625's molybdenum content (8–10%) is insufficient and C-276's higher Mo+W (up to 19.5%) provides additional resistance. JN Alloy stocks both alloys and can supply full API 6A-compliant forgings, pipe, and fittings.

 

Property

Inconel 625 (N06625)

Hastelloy C-276 (N10276)

Winner for HH

Ni / Cr / Mo

58-63% / 20-23% / 8-10%

57% / 14.5-16.5% / 15-17%

625: higher Cr; 276: higher Mo+W

PREN

≈42 (Cr + 3.3×Mo + 16×N)

≈48–52 (incl. W)

C-276: higher PREN

Max. Service Temp.

980°C continuous

900°C continuous

625: slightly higher temp

HCl Resistance

Good (<15% at RT)

Excellent (all concentrations)

C-276

H₂SO₄ Resistance

Good (<50% at 80°C)

Excellent (<80% at 80°C)

C-276

Chloride SCC Immunity

Yes, at all temps

Yes, at all temps

Tie

Weldability

Excellent (ERNiCrMo-3)

Very Good (ERNiCrMo-4)

625 (easier to weld)

API 6A Wellhead Use

Most common; default choice

Used for most aggressive environments

625 (default)

Cost

Moderate (baseline for HH)

High (premium for severe environments)

625 (cost advantage)

Stock Availability

Widely stocked (plate, pipe, bar)

Available but less common

625 (stock advantage)

[Source] Haynes International Inconel 625 datasheet; Haynes International Hastelloy C-276 datasheet; Special Metals Corporation technical data. PREN calculated per NACE TM0177 / ASTM G48 methodology.

 

Why Nickel Content Above 58% Is Critical for Sour Gas

 

The nickel content of ≥58% (Inconel 625) and ≥57% (Hastelloy C-276) is not an accident - it is the structural basis for their SSC immunity. In austenitic nickel alloys, the FCC (face-centered cubic) crystal structure has a much lower hydrogen diffusivity than BCC carbon steel, meaning fewer hydrogen atoms can penetrate the lattice. Additionally, nickel actively recombines nascent hydrogen at the surface before it can diffuse inward. Carbon steel (Ni < 0.5%) and even standard austenitic stainless steel (Ni 8–12%) cannot provide this protection, which is why they are limited to Class DD or FF at best in sour service.

 

How Do PSL 1, PSL 2, and PSL 3 Affect Material Requirements?

 

PSL (Product Specification Level) defines the documentation, inspection, testing, and traceability requirements - not the material itself. Class HH applies regardless of PSL; however, PSL 3 (mandatory for sour service per API 6A) imposes additional requirements on material verification that directly affect how you specify and accept nickel alloy components. For Class HH in sour service, PSL 3 is effectively required by most operators and regulatory bodies worldwide.

 

Requirement

PSL 1

PSL 2

PSL 3 (Required for HH Sour Service)

Material Traceability

Heat number per lot

Heat to component traceability

Heat + lot + heat treatment batch traceability

Chemical Analysis

Cast analysis reported

Cast + product analysis reported

Cast + product analysis + PMI verification

Mechanical Testing

Tensile + hardness per lot

Tensile + hardness + impact per lot

Tensile + hardness + impact + SSC test (NACE TM0177)

Hydrostatic Test

Required

Required

Required + documented

Visual & Dimensional

Required

Required

Required + NDE (MPI / DPI, UT)

Sour Service Qualification

Not required

May be specified

Mandatory for HH in H₂S service

Mill Test Report

EN 10204 2.2 or 3.1

EN 10204 3.1

EN 10204 3.1 + material datasheet

Third-Party Inspection

Optional

Optional

Usually required by operator

Low-temp impact for HH-L

Not required

Not required

54 J transverse at −46°C

[Source] API 6A, 21st Edition, Clause 7 - Inspection and examination requirements by PSL. NACE TM0177-2016 - SSC testing of metals.

 

How to Specify API 6A Class HH Materials: A Procurement Checklist

 
A correctly specified Class HH purchase order must include: (1) API 6A as the governing standard with edition number (e.g., 21st Edition, 2018), (2) the exact material class (HH or HH-L), (3) PSL level (PSL 3 for sour service), (4) alloy designation (Inconel 625 or Hastelloy C-276) with UNS number, (5) NACE MR0175 / ISO 15156-3 qualification reference, (6) ASTM product specification and grade, and (7) required test reports (EN 10204 3.1, PMI, Charpy). Ambiguity in any of these fields can result in non-conforming material at site - a costly and dangerous outcome.
 
How to Specify API 6A Class HH Materials
 

PO Field

Required Entry for Class HH

Example

Governing Standard

API Spec 6A + ISO 10423

API 6A 21st Edition (2018)

Material Class

HH or HH-L

HH-L

PSL

PSL 3 (sour service)

PSL 3

Alloy / UNS

Inconel 625 / N06625; or Hastelloy C-276 / N10276

Inconel 625 UNS N06625

Product Form

Forging / Plate / Seamless Pipe / Bar

ASTM B564 Forging, NPS 4– 12

ASTM Grade

Gr 1 (low-C) or Gr 2 (standard)

ASTM B443 Gr 1

Sour Service Qual.

ISO 15156-3 reference

ISO 15156-3:2020 compliant

Hardness Max

HRC 40

HRC 40 max

Impact Requirement

54 J transverse at RT (HH) or −46°C (HH-L)

54 J at −46°C transverse

Mill Test Report

EN 10204 3.1

EN 10204 3.1 TC

PMI Verification

XRF mandatory

PMI 100% on receipt

Special Requirements

NACE TM0177 SSC test, UWQA

NACE TM0177 Method A required

[Source] API 6A, 21st Edition, Annex F and Clause 7; NACE MR0175 / ISO 15156-3:2020; EN 10204:2004 Metallic products - Types of inspection documents.

 

How to Verify Class HH Material on Receipt

 

Upon material receipt, always perform the following verification steps before releasing to the workshop:

 

Step 1 - PMI: Positive Material Identification (PMI): Use a handheld XRF analyzer to verify Ni, Cr, Mo, and W content against the C-276 or 625 specification range.

 

Step 2 - MTC Review: MTC (Mill Test Certificate): Verify heat number, chemical analysis, mechanical properties (tensile, yield, elongation, hardness), and heat treatment condition.

 

Step 3 - Impact Test: Charpy Impact Test Report: Confirm impact energy meets 54 J (transverse) at the required temperature (RT for HH, −46°C for HH-L).

 

Step 4 - Sour Service Qual.: NACE MR0175 / ISO 15156-3 Certificate: Confirm the material supplier's qualification documentation.

 

Step 5 - Visual & Dimensional: Visual Inspection: Check for surface defects, mis-machined dimensions, and correct markings.

 

Step 6 - NDE: ultrasonic testing (UT) or magnetic particle inspection (MPI) on critical welds

 

Where Is Class HH Nickel Alloy Equipment Used in the Oil & Gas Industry?

 

Typical Applications for API 6A Class HH Equipment

 

API 6A Class HH nickel alloy equipment is specified for the most demanding subsurface and surface applications where carbon and low-alloy steels fail within months. Key application areas include deep sour gas wells, high-pressure high-temperature (HPHT) reservoirs, offshore platforms with high-chloride produced water, and thermal EOR (enhanced oil recovery) projects with hot brine injection.

 

Application

Service Environment

Why Class HH Is Required

Christmas Tree (Xmas Tree) Valves

H₂S 5–15%, CO₂ 5–20%, Cl⁻ >50,000 ppm, 120–180°C

High H₂S + temp + chloride = FF class insufficient

Wellhead Connectors & Hangers

HPHT sour gas, near-yield stress levels, cyclic loading

SSC risk at high stress + H₂S requires nickel CRA

Tubing Head & Casing Hangers

Hot produced water with H₂S + CO₂ + Cl⁻

Galvanic + acid attack + SSC in same component

Choke Beans & Flow Beans

High-velocity erosive flow, sour gas + sand

Erosion + corrosion + SCC in one component

Safety Valve (SCSSV) Bodies

Subsurface, H₂S + high temp, pressure cycling

SSC risk + thermal fatigue in subsurface conditions

Surface Flow Lines (for Xmas tree outlet)

Sour gas + elemental sulfur, high temp

Elemental S dramatically lowers SSC threshold

Arctic Offshore Platform Xmas Trees

H₂S sour gas + ambient −46°C

HH-L required: cryogenic toughness + sour gas resistance

Thermal EOR Injection Lines

Hot brine (150–180°C) + H₂S + CO₂

High-temp sour brine exceeds FF-class temperature limit

[Source] Compiled from operator project specifications; Haynes International oil & gas application references; NACE International Publication 34100 - Review of H₂S field experience.

 

Frequently Asked Questions

 
Q1: Can stainless steel 316L be used for API 6A Class HH?

No. API 6A Class HH explicitly requires nickel-based CRA materials. While 316L stainless steel (UNS S31603) has good corrosion resistance in many environments, its nickel content (10–14%) is insufficient to provide immunity to sulfide stress cracking in H₂S-containing service. Its PREN of approximately 24 is far below the threshold required for severe sour gas environments. Only alloys meeting the nickel content and PREN requirements of Inconel 625 (UNS N06625) or Hastelloy C-276 (UNS N10276) - and qualified per NACE MR0175 / ISO 15156-3 - are acceptable for Class HH.

 

Q2: What is the difference between Class FF and Class HH?

Both FF and HH have the same temperature range (−29°C to +180°C), but they use fundamentally different materials. Class FF uses carbon and low-alloy steels (up to 13Cr martensitic stainless) qualified per NACE MR0175 / ISO 15156-3, with hardness limited to ≤22 HRC to reduce SSC susceptibility. Class HH uses nickel-based CRA (Inconel 625 or Hastelloy C-276), which are inherently immune to SSC regardless of hardness. HH is selected when FF-class materials cannot meet the corrosion rate, pitting, or temperature requirements of the service environment.

 

Q3: When is Class HH-L specified instead of Class HH?

Class HH-L is specified when the minimum operating temperature falls below −29°C (−20°F). This occurs in Arctic onshore gas fields and offshore subsea wellhead systems where ambient seawater temperatures can drop to −46°C or below. The L-suffix requires additional Charpy V-notch impact testing at −46°C (minimum 54 J transverse) to demonstrate that the nickel alloy retains adequate toughness at cryogenic temperatures without becoming brittle. The upper temperature limit (+180°C) remains the same as standard Class HH.

 

Q4: Does Class HH require post-weld heat treatment (PWHT)?

In most cases, NO. Both Inconel 625 and Hastelloy C-276 are used in the as-welded or solution-annealed condition for API 6A wellhead applications. Their ultra-low carbon and silicon content prevents carbide precipitation in the weld heat-affected zone (HAZ), eliminating the need for post-weld solution annealing. However, for the most severe services (concentrated HCl, elemental sulfur, or temperatures above 150°C in sour brine), solution annealing at 1093–1171°C followed by rapid water quench is recommended to restore maximum corrosion resistance. PWHT (post-weld heat treatment at lower temperatures) should be avoided as it does not improve and may degrade the corrosion resistance of these alloys.

 

Q5: What is the typical lead time for API 6A Class HH Inconel 625 wellhead components?

API 6A Class HH Inconel 625 forgings for wellhead bodies and bonnets typically require 16–26 weeks from order confirmation to delivery, as most are produced by specialist foundries and forge shops with API 6A monogram licenses (API 6A Q1 quality management system). Stock items such as Inconel 625 plate, bar, and seamless pipe (ASTM B443/B574/B622) may be available in 4–10 weeks from distributors. JN Alloy maintains inventory of Inconel 625 and Hastelloy C-276 plate, bar, and pipe for rapid response to inquiries. For urgent requirements, contact jnalloy123@gmail.com with your specific RFQ including size, quantity, pressure class, and delivery destination.

 

Q6: How does JN Alloy verify that Class HH material meets API 6A and NACE MR0175 requirements?

JN Alloy supplies Class HH nickel alloy materials with full API 6A and ISO 15156-3 compliance documentation. Every shipment includes: (1) EN 10204 3.1 Mill Test Certificate with heat chemistry, mechanical test results, and heat treatment record; (2) NACE MR0175 / ISO 15156-3 material qualification letter from the mill; (3) API 6A Q1 monogram license number (for finished components); (4) Charpy impact test results at the specified temperature; (5) optional PMI testing report and third-party inspection certificate (API 6A PSL 3). Upon receipt, buyers should perform independent PMI verification using a calibrated handheld XRF analyzer to confirm Ni, Cr, Mo, and W content matches the material specification before releasing material to fabrication.

 

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