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How to Select the Right Casing Spool Tees and Crosses Frac Head for Sour Service?

Jianhu Yuxiang Machinery Manufacturing Co., Ltd. 2026.02.23
Jianhu Yuxiang Machinery Manufacturing Co., Ltd. Industry News

Selecting the Right Casing Spool, Tees, Crosses, and Frac Head for Sour Service

Hydraulic fracturing in wells containing Hydrogen Sulfide () is one of the most demanding tasks in oil and gas development. In these “sour service” environments, selecting the right Casing Spool, Tees, Crosses, and Frac Head assembly requires moving beyond basic pressure ratings. Without considering specific metallurgical properties, standard carbon steel equipment can suffer catastrophic Sulfide Stress Cracking (SSC) in a very short time. To ensure operational safety, minimize Non-Productive Time (NPT), and meet strict regulatory requirements, engineering teams must evaluate equipment based on material science, manufacturing standards, and advanced sealing technologies.

Assessing the Hidden Threats of Sour Service in Fracking

Hydrogen Sulfide is not only highly toxic; its corrosive effect on metal is uniquely deceptive. In a sour environment, moisture reacts with to release atomic hydrogen, which easily penetrates the lattice structure of high-strength steel, causing the material to become brittle.

  • The Physical Mechanism of SSC: Unlike uniform corrosion, which thins metal over time, SSC often occurs suddenly without any prior visual warning. For a Frac Head operating under 10,000 or 15,000 PSI, such a fracture leads to a catastrophic blowout. Therefore, selecting equipment for sour service focuses on sacrificing a degree of material hardness to gain higher toughness and resistance to hydrogen embrittlement.
  • The Synergistic Effect of Erosion and Corrosion: During fracturing, high-velocity proppants (sand) constantly scour the internal walls of Tees and Crosses. In a sour well, this abrasion strips away the protective films on the metal surface, accelerating the chemical attack of on the fresh metal substrate. This “erosion-corrosion” cycle necessitates the use of advanced internal bore protection, such as Inconel cladding, to balance crack resistance with wear resistance.


Core Selection Standards: Deep Integration of NACE MR0175 and API 6A

When selecting a Casing Spool Tees and Crosses Frac Head, it is mandatory to ensure the supplier provides material certifications compliant with top international specifications. If these two standards cannot be verified, the equipment poses an unacceptable operational risk.

1. NACE MR0175 / ISO 15156 Hardness Requirements

This is the globally recognized “gold standard” for material selection in sour environments. It defines the specific metallurgical indicators that metallic components must meet when in contact with -bearing fluids.

  • Hardness Limits: For most low-alloy steels used in manufacturing Frac Crosses (such as AISI 4130), NACE mandates a maximum hardness of 22 HRC (Rockwell C). Materials that are too hard may have high tensile strength but are extremely prone to brittle cracking in the presence of .
  • Chemical Composition Restrictions: The standard also strictly limits nickel content (typically to less than 1%), as high nickel concentrations can significantly increase sensitivity to hydrogen-induced cracking in certain alloys.

2. Precision Matching of API Spec 6A Material Classes

API 6A categorizes equipment into different material classes based on the corrosivity of the fluid. For sour fracturing operations, buyers should focus on the following:

  • Classes DD and EE: These are the entry-level classes for sour service, requiring all metallic parts to strictly follow NACE heat treatment and hardness requirements.
  • Classes FF and HH: For highly corrosive or long-term operations, Class HH equipment is considered the industry best practice. These units feature Inconel 625 or other high-performance alloy overlays on all wetted surfaces. While the initial procurement cost is higher, their superior lifespan in complex frac fluids and high concentrations significantly reduces the total lifecycle cost by preventing premature equipment replacement.


Selection Guide: Sour Service vs. Standard Service Equipment Parameters

To visually demonstrate the technical differences, we have compiled the following table as a reference for engineering selection:

Technical Feature Standard Service (General) Sour Service (H2S Environment) Selection Priority
Base Material AISI 4130 / 4140 Alloy Steel NACE Compliant 4130 Steel Chemical Stability
Max Hardness No strict limit (often >22 HRC) Strictly 22 HRC SSC Prevention
Bore Protection Standard Machined Surface Optional Inconel 625 Cladding Erosion/Corrosion Balance
Sealing Material Nitrile (NBR) Viton (FKM) / FFKM Gas Permeation Resistance
API PSL Level PSL 1 or PSL 2 PSL 3 or PSL 3G (Gas Tested) Enhanced NDT Testing


Advanced Design Features of Integrated Frac Head Assemblies

In ultra-high-pressure fracturing tasks, standard component stacking may not meet safety demands. Modern Frac Head designs have evolved toward integration and high-performance coatings.

CRA (Corrosion Resistant Alloy) Cladding Technology

In extremely aggressive sour wells, manufacturers utilize a “Weld Overlay” or “Cladding” process. A layer of nickel-based alloy, approximately 3mm thick, is welded into the seal pockets of the Casing Spool and the central flow path of the Frac Head.

  • Core Advantage: This gives the equipment the structural strength of low-alloy steel combined with the near-total corrosion resistance of pure nickel. For sealing areas, this effectively prevents micro-leaks caused by pitting corrosion—a matter of life and death when is present on site.

Integrated Frac Crosses and Connection Optimization

For sour service, the highest principle of engineering design is to minimize the number of potential leak paths.

  • Reducing Flanged Connections: Use a single-piece Integrated Frac Cross instead of multiple individual Tees. Every flange connection is a potential leak point. In a sour environment, if a flange gasket fails, the escaping gas poses an immediate threat to the lives of personnel on the rig floor.
  • Studded Connections: Compared to traditional long-bolt flanged connections, studded structures are more compact and less susceptible to external mechanical damage, offering a higher safety factor during sour wellhead operations.


Frequently Asked Questions (FAQ)

Q1: If the H2S concentration in the well is very low, can I use a standard Frac Head?

According to NACE MR0175, if the partial pressure of in the gas phase exceeds 0.05 psi, the well is defined as “Sour.” Even at low concentrations, high pressure allows hydrogen atoms to penetrate the steel, triggering SSC. To mitigate legal and safety risks, it is recommended to use NACE-compliant equipment whenever is detected.

Q2: Why do NACE-rated Frac Heads seem to wear out faster during fracturing?

This is a common observation. Because NACE-compliant steel is heat-treated to a lower hardness ( 22 HRC), its erosion resistance is slightly lower than that of harder standard steels. To resolve this, it is suggested to use thickened designs at high-turbulence flow turns or utilize wear-resistant coatings and Inconel cladding in the internal bore.

Q3: What does the “G” in PSL 3G stand for?

The “G” stands for Gas Testing. For a Casing Spool Tees and Crosses Frac Head in a sour environment, a hydrostatic (water) test is often insufficient. Since is a gas, gas testing more accurately simulates the molecular-level sealing integrity required in the field.


References and Citations

  1. NACE MR0175/ISO 15156: Petroleum and natural gas industries—Materials for use in H2S-containing environments.
  2. API Specification 6A: 21st Edition, Specification for Wellhead and Tree Equipment.
  3. Journal of Petroleum Technology: Managing Synergistic Erosion and Corrosion in Modern Fracking (2025).