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API 5CT Grade L80 is the industry baseline for controlled-yield OCTG in sour service and mild corrosive environments, yet it remains the most frequently misapplied specification in field operations. Unlike J55 or N80, where failure is usually mechanical (collapse/burst), L80 failures are predominantly environmental: Sulfide Stress Cracking (SSC) in Type 1 and localized pitting or galling in 13Cr. Success requires managing the delta between mill tolerances and downhole realities.
No. L80 Type 1 is carbon steel designed for H2S cracking resistance, not weight-loss corrosion. In wet CO2 environments without continuous inhibition, localized corrosion rates can exceed 50 mpy (mm/y), leading to rapid wall loss.
No. API 5CT permits a maximum hardness of 23.0 HRC. NACE MR0175 (Region 3) limits carbon steel to 22.0 HRC. A pipe stamped "L80" can be 22.8 HRC, legally passing API but failing NACE sour service audits.
1.5 psi (0.1 bar). Standard 13Cr is extremely susceptible to Sulfide Stress Cracking (SSC) if the partial pressure of H2S exceeds 1.5 psi. Above this threshold, you must upgrade to Super 13Cr or Duplex stainless steel.
Procurement teams often struggle with the price jump from N80 to L80. The economic logic relies entirely on the Sulfide Stress Cracking (SSC) threshold.
Cost-Effective Zone: L80 Type 1 is the mandatory selection when H2S partial pressure exceeds 0.05 psi (0.003 bar). Below this level, N80Q is sufficient. Using L80 in completely sweet wells is an over-engineered waste of capital (~15-20% premium over N80).
The 13Cr Breakpoint: L80 13Cr becomes economically viable when CO2 partial pressure exceeds 2-3 psi, making batch inhibition of carbon steel logistically impossible or OPEX-prohibitive. However, if water cut is low (<5%) and stable, inhibited carbon steel (L80 Type 1) remains the lower lifecycle cost option.
Above 300°F (149°C), the risk of Chloride Stress Corrosion Cracking (CSCC) in 13Cr increases exponentially, necessitating a move to 22Cr Duplex or Super 13Cr.
The most critical procurement failure regarding L80 Type 1 is the hardness discrepancy. We frequently see pipe rejected at the rig site because the Purchase Order specified "API 5CT L80" but the well plan required "NACE MR0175 Sour Service."
API 5CT technically allows a hardness up to 23 HRC (approx. 241 HBW). However, for Region 3 Sour Service (high H2S), NACE MR0175 mandates a maximum of 22 HRC (237 HBW). Material testing reports (MTRs) from the mill often show heat averages. If the average is 21.5 HRC, statistical variation means individual joints may test at 22.5 HRC, creating a "NACE Fail" condition during spot checks.
Both grades share a minimum yield of 80,000 psi (551 MPa), meaning their burst and collapse ratings are identical; the difference is purely metallurgical chemistry and heat treatment.
While L80 13Cr is selected for CO2 resistance, it is famously intolerant of oxygen and stagnant water. A passive chromium oxide film protects the steel, but this film is unstable in the presence of chlorides and oxygen.
If 13Cr pipe is stored in a humid yard with standard mill varnish that has been damaged, moisture traps chlorides against the metal. Without the flow conditions of a producing well to maintain the passive film, rapid pitting occurs. We recommend climate-controlled storage or specialized UV-cured heavy storage compounds for 13Cr inventory held longer than 6 months.
Using raw seawater or untreated brine for hydro-testing 13Cr tubing is a catastrophic error. The dissolved oxygen in the surface water (approx. 8 ppm) combined with chlorides will initiate pitting within 24 hours. If seawater must be used, it must be treated with an oxygen scavenger (to <10 ppb) and a biocide immediately.
Trust is built by knowing when not to sell or use a product. L80 (Type 1 or 13Cr) must be disqualified under these conditions:
pH < 3.5: In extremely acidic environments, L80 Type 1 corrosion rates become unmanageable even with inhibition.
H2S > 1.5 psi (for 13Cr): Standard 13Cr will suffer SSC. Do not attempt to "push" this limit with inhibitors; the cracking mechanism is instantaneous.
Dissolved Oxygen > 10 ppb: Any continuous oxygen ingress (e.g., leaking surface seals, water injection) will destroy L80 13Cr via pitting corrosion.
| Feature | L80 Type 1 | L80 13Cr | T95 Type 1 |
|---|---|---|---|
| Primary Hazard | H2S (Sour Gas) | CO2 (Sweet Gas) | High Pressure Sour |
| Yield Strength | 80-95 ksi | 80-95 ksi | 95-110 ksi |
| Max Hardness | 22 HRC (NACE) | 23 HRC | 25.4 HRC (Special Process) |
| Cost Index | 1.2x | 3.5x | 2.0x |
Operational Takeaway: T95 provides higher collapse resistance for deep wells but requires extremely long lead times for mill qualification. L80 Type 1 is the "off-the-shelf" standard, but stock availability rarely guarantees NACE-compliant hardness without supplementary testing.
Yes. Elemental sulfur acts as a catastrophic oxidant. In L80 Type 1, it accelerates sulfide stress cracking; in L80 13Cr, it causes massive localized pitting at temperatures >150°F (65°C), regardless of H2S levels.
Conditional. For L80 Type 1, standard API Modified (containing lead/zinc) is acceptable. For L80 13Cr, "Yellow" API Modified can be used, but many operators prefer metal-free/environmentally friendly dope to avoid bi-metallic corrosion within the thread roots, which can compromise the seal.
If L80 13Cr fails due to pitting (usually indicating H2S or O2 presence), the immediate upgrade is Super 13Cr (S13Cr-95 or S13Cr-110). Super 13Cr contains Molybdenum (1-2%), which stabilizes the passive film and raises the H2S limit to approx. 4.0 psi.