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Technical Guide for Drill Pipe Corrosion Protection: From Sulfide-Resistant Steel Grades to Internal Coatings

Author:

WHH

Source:

LONGWAY

Published:

2026-09-18


Corrosion is one of the primary failure modes of drill pipes. Statistical data indicate that, in oil and gas wells containing H₂S and CO₂, corrosion accounts for more than 40% of drill‑pipe failures. Corrosion not only directly thins the pipe wall and reduces its load‑carrying capacity but also interacts with cyclic fatigue loading, thereby accelerating drill‑pipe fracture. This paper systematically reviews the types, mechanisms, influencing factors, and protective strategies of drill‑pipe corrosion, providing technical guidance for material selection, procurement, and field management.

I. Main Types of Drill Pipe Corrosion

Corrosion TypeMechanismTypical environmentConsequences
Uniform corrosionUniform thinning of the entire surfaceAcidic drilling fluid, high salinityWall thickness reduction leads to a decrease in strength.
Pitting corrosionLocalized deep pits form.Contains Cl⁻ and dissolved oxygenStress concentration, fatigue crack initiation
Crevice corrosionMedium stagnation within the gapThreaded joints, shoulder surfacesSeal failure, tripping
Galvanic corrosionDissimilar metal contactDrill pipe and drill collar jointAccelerated corrosion on the anode side
Corrosion fatigueCorrosion + Cyclic StressAll downhole conditionsCrack propagation is rapid, leading to fracture.
Sulfide Stress Cracking (SSC)H₂S + tensile stressH₂S-containing wet environmentBrittle fracture suddenly occurring
Hydrogen-Induced Cracking (HIC)Hydrogen atoms permeate into steel.H₂S-containing environmentInternal cracks, step-like fracturing
CO₂ corrosionCarbonic acid corrosionCO₂-containing condensate gas wellLocal deep pit, wall thickness reduction

Corrosion fatigue is the most hazardous failure mode in drill pipes: corrosive media induce pitting on the surface, with the pit bottoms serving as stress concentration points; under cyclic loading, fatigue cracks initiate at these sites and propagate rapidly.

II. Key Factors Affecting Drill Pipe Corrosion

1. Corrosive medium

H₂S: It can induce SSC and HIC, with increasing risk at higher concentrations. NACE MR0175/ISO 15156 specifies material suitability under different partial pressures.

CO₂: Dissolves in water to form carbonic acid, lowering the pH and accelerating both uniform corrosion and pitting corrosion.

Cl⁻: Destroys the passive film, initiating pitting and crevice corrosion.

Dissolved oxygen: significantly accelerates corrosion, particularly in drilling fluid circulation systems.

2. Environmental Conditions

factorImpact
TemperatureIncreased temperature accelerates corrosion reactions, but it also affects SSC susceptibility (with a peak around 80°C).
pHLow pH accelerates uniform corrosion; high pH reduces the risk of SSC.
Flow rateHigh flow velocity exacerbates erosion, but reduces the risk of pitting corrosion.
PressureIt affects gas solubility, thereby indirectly influencing the corrosion rate.

3. Material Factors

Steel grade: High-strength steel is more susceptible to SSC; S135 > G105 > E75.

Chemical composition: Alloying elements such as Cr, Mo, and Ni enhance corrosion resistance.

Microstructure: Tempered martensitic microstructure exhibits superior SSC resistance compared to the untempered microstructure.

Hardness: The higher the hardness, the greater the susceptibility to SSC (API 5DP specifies that the hardness of SS steel grades shall not exceed HRC 32).

III. Corrosion Protection Strategies for Drill Pipes

1. Material Selection: Sulfur-Resistant Drill Pipe

For environments containing H₂S, the SS series should be selected. Sulfur-resistant drill pipe (SS95/SS105/SS135), designed in compliance with NACE MR0175/ISO 15156 requirements. In 2025, Supplement No. 1 to API 5DP will introduce a new requirement: for SS steel grades, grain size shall be ≥ ASTM Grade 6, and the martensite transformation rate after quenching shall exceed 90%.

Selection Principles:

H₂S partial pressure < 0.3 kPa: Standard steel grade with internal coating may be selected.

H₂S partial pressure of 0.3–10 kPa: Select SS95 or SS105.

H₂S partial pressure > 10 kPa: Select SS135 and strictly limit hardness.

2. Internal Coating Protection

Internal coating (LPC3000P/LPC5000P series) Form an isolation layer on the inner wall of the pipe, effectively preventing corrosive media from coming into contact with the steel. Technical specifications:

ParameterLPC3000PLPC5000P
Temperature-resistant≤180℃≤204℃
pH range2-12.53-13
H₂S-resistant<4%<10%
Life extension1-2 times3-4 times

Applicable scenarios: condensate gas wells containing CO₂/H₂S, high-salinity water wells, water injection wells, and others.

3. Drilling Fluid Treatment

pH Control: Maintain the pH between 9.5 and 11.5 to reduce the risk of SSC.

Corrosion inhibitor: Add a film-forming or adsorptive corrosion inhibitor.

Deoxygenation: Use a deoxidizer to maintain dissolved oxygen levels below 20 ppb.

Biocides: Control of sulfate-reducing bacteria (SRB)

4. Operation and Maintenance

Before entering the well, inspect the threads and shoulder surfaces to ensure there is no corrosion or damage.

Use the correct thread compound to prevent crevice corrosion.

After pulling out of the hole, promptly clean to remove any residual drilling fluid.

Apply anti-rust grease for long-term storage and install thread protectors.

IV. Corrosion Monitoring and Inspection

MethodApplicable ScenariosTest Content
Corrosion couponDrilling fluid circulation systemUniform corrosion rate
Resistance probeOnline monitoringReal-time corrosion rate
Ultrasonic thickness measurementDrill pipe bodyWall thickness reduction
Magnetic Flux Leakage (MFL) InspectionOverall tube lengthCorrosion pits, pitting corrosion
Magnetic Particle Testing (MT)Thread, shoulderSurface Cracking (SSC/HIC)

Recommended inspection intervals: For wells containing H₂S, MT inspections should be performed after each well is pulled out of the hole; for wells containing CO₂, MFL inspections should be conducted every 3 to 5 wells.

V. Procurement and Selection Recommendations

When procuring drill pipes, the following requirements should be clearly specified for corrosive environments:

ProjectTechnical Requirements
Steel gradeSelect SS95, SS105, SS135, or a standard steel grade with an internal coating based on the H₂S/CO₂ partial pressure.
Internal coatingLPC3000P/LPC5000P: clearly specified temperature resistance, pH range, and sulfur resistance.
HardnessSS steel grade ≤ HRC 32, standard steel grade ≤ HRC 37
Nondestructive testingMT+UT+MFL, with a focus on threads and the pipe body.
Quality DocumentThe MTC shall include grain size, martensite transformation fraction, hardness, and SSC/HIC test results.
Standard complianceNACE MR0175/ISO 15156, API 5DP Supplement No. 1, 2025

VI. Frequently Asked Questions (FAQ)

Q1: Must all wells containing H₂S use sulfur‑resistant drill pipe?

Not necessarily. An assessment must be conducted in accordance with NACE MR0175/ISO 15156, taking into account parameters such as H₂S partial pressure, pH, and temperature. Under low‑partial‑pressure conditions, a standard steel grade combined with an internal coating and a corrosion inhibitor may be sufficient.

Q2: Can an internal coating completely replace sulfur‑resistant drill pipe?

No. The internal coating primarily protects the inner wall of the pipe, while the threads and shoulder surfaces still rely on the material’s inherent resistance to sulfidation. At higher H₂S partial pressures, an SS steel grade should be selected.

Q3: How can you determine whether a drill pipe has experienced corrosion fatigue?

Corrosion fatigue manifests as cracks that initiate from pitting defects, typically originating at the pipe body surface or at the thread roots. Magnetic particle testing (MT) and ultrasonic testing (UT) can detect cracks, while magnetic flux leakage (MFL) can detect pitting defects.

Q4: Can drill pipes be repaired after corrosion?

Minor corrosion can be removed by grinding, but drill pipes with wall‑thickness reduction exceeding the allowable limit should be downgraded or scrapped. Thread‑corrosion damage typically requires re‑threading for repair, though this is constrained by the amount of material that can be removed.

Q5: How can the service life of drill pipes used in corrosive environments be extended?

Comprehensive measures: select sulfur‑resistant steel grades with internal coatings, control drilling fluid pH and corrosion inhibitors, conduct regular inspections, perform timely repairs, and ensure proper storage.

VII. Summary

Key pointsCore content
Major Types of CorrosionUniform corrosion, pitting corrosion, SSC, HIC, CO₂ corrosion, corrosion fatigue
Key influencing factorsH₂S/CO₂ partial pressure, pH, temperature, Cl⁻, dissolved oxygen
Protection StrategySulfur-resistant steel grade + internal coating + drilling fluid treatment + operation and maintenance
Detection methodMT for crack detection, MFL for corrosion pit inspection, UT for wall thickness measurement.
Procurement HighlightsMaterial selection shall comply with NACE MR0175/ISO 15156; internal coating parameters must be clearly defined, and a complete MTC is required.

Corrosion protection for drill pipes is a systems‑level endeavor that requires multidimensional coordination, spanning material selection, coating-based protection, drilling fluid management, and on‑site operational practices. A thorough understanding of corrosion mechanisms and influencing factors, coupled with appropriate material selection and rigorous inspection and maintenance protocols, is essential for extending drill pipe service life and ensuring drilling safety.

Do you need to procure sulfur‑resistant drill pipes or internally coated drill pipes for drilling projects in H₂S/CO₂ environments?

Contact Hebei Longway Petroleum Equipment Co., Ltd.

Obtain professional technical consulting

Hebei Longway offers sulfur‑resistant drill pipes SS95, SS105, and SS135, as well as internal coating services for LPC3000P and LPC5000P, and holds international certifications including API 5DP and API 7‑1.


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