Tubing Hanger: Definition, Types, and Wellhead Integration
What Is a Tubing Hanger?
A tubing hanger suspends the entire production tubing string from the tubing head spool inside the wellhead, bearing the full mechanical load of the tubing while simultaneously providing a pressure-tight annular seal between the tubing and the surrounding wellhead bore. Precision-machined from alloy steel, the hanger locates in a machined seat within the tubing head and incorporates a central flow bore through which produced fluids travel to surface.
Key Takeaways
- A tubing hanger performs two simultaneous functions: it bears the full tensile load of the production tubing string (which can range from 50,000 lb / 22,680 kg in shallow wells to over 500,000 lb / 226,796 kg in deep, heavy-wall completions) and it provides a gas-tight annular seal that isolates the tubing-casing annulus from the wellhead bore above.
- Three principal hanger designs are used in the field: the mandrel hanger (smooth machined OD, seats on a machined shoulder in the tubing head), the slip hanger (cone-and-slip segments that grip the tubing OD mechanically without requiring a threaded shoulder), and the polished bore receptacle integral hanger (used in thermal completions such as SAGD where axial expansion must be accommodated).
- API 6A / ISO 10423 governs tubing hanger design, material, pressure rating, and test requirements; hangers must match the wellhead's rated working pressure, which runs from 5,000 PSI (345 bar) for shallow conventional gas wells to 15,000 PSI (1,034 bar) for HPHT applications.
- Metal-to-metal (MXM) annular seals are the preferred configuration for sour-service (H2S-containing) wells and all offshore and HPHT applications; elastomeric pack-off seals are acceptable for lower-pressure, non-sour land wells where temperature excursions remain modest.
- In directional-flow wellheads, tubing hangers incorporate an orientation pin that aligns chemical-injection and hydraulic-control-line penetrations in the hanger body with matching ports in the christmas tree above, enabling stab-in connections during tree installation.
How a Tubing Hanger Works
The tubing hanger is the last component made up on the bottom of the tubing head adapter (THA) or tubing head spool assembly before the production string is landed. During completion operations, the tubing string is run in the hole as individual joints or stands and is assembled according to the designed completion program. When the production packer has been set at the intended depth and the tubing has been tensioned or slackened off to the design load, the top of the string is made up into the hanger mandrel or slips. The hanger assembly is then lowered on the running tool until it contacts and locks into the machined profile or bowl in the tubing head.
Once landed, a pack-off or metal-to-metal seal assembly is energized either mechanically (by rotating or setting down weight) or hydraulically to create the annular seal. This seal isolates the A-annulus (tubing-casing annulus) from the wellbore below and from the wellhead-Christmas-tree connection above. The seal must withstand full wellhead working pressure from below (shut-in tubing pressure) and, in gas-lift completions, injection pressure from above. API 6A requires a minimum of two independent seals on offshore and HPHT hangers, typically designated as primary and secondary, with the secondary acting as a backup if the primary degrades over the well's producing life.
Load ratings are calculated using Lame's equation for thick-walled cylinders, accounting for the tubing string weight in fluid (buoyed weight), thermal elongation due to produced-fluid temperature, and packer-induced compression or tension. For a 3.5-inch (88.9 mm) tubing string run to 15,000 ft (4,572 m) in a deep gas well, the combined mechanical and pressure-induced load on the hanger can exceed 300,000 lb (136,078 kg). The hanger body, running threads, and load-bearing shoulder are all designed to a minimum safety factor of 1.25 against yield under the maximum combined loading per API 6A Annex F.
Tubing Hanger Across International Jurisdictions
While the fundamental mechanics of the tubing hanger are universal, each major oil-producing jurisdiction overlays its own regulatory requirements on materials, testing, documentation, and sour-service certification.
Canada (Alberta): Alberta Energy Regulator (AER) Directive 036 (Drilling Blind Zones) and Directive 059 (Well Completion Requirements) specify wellhead component ratings for the Montney, Duvernay, and Deep Basin HPHT plays. Sour wells with partial H2S pressures above 0.34 kPa (0.05 psi) must use tubing hangers in NACE MR0175 / ISO 15156 compliant material grades, typically EE or FF designation per API 6A Annex F. The AER requires a documented wellhead-assembly pressure test before placing a well on production, and tubing hanger records must be retained for the life of the well and submitted as part of the completion report. In the Peace River oil sands, tubing hangers used on cyclic steam stimulation (CSS) wells must be rated for temperatures up to 340 degrees C (644 degrees F) and must accommodate the large axial displacement caused by repeated thermal cycles.
United States: Offshore wells on the Outer Continental Shelf are governed by the Bureau of Safety and Environmental Enforcement (BSEE) under 30 CFR Part 250. Subpart E (Oil and Gas Well-Completion Operations) requires that all wellhead components, including tubing hangers, comply with API Specification 6A. For deepwater wells in the Gulf of Mexico, the tubing hanger is typically a subsea component run inside the subsea christmas tree or tubing head spool, and BSEE requires documented traceability for all pressure-containing parts. Onshore wells in Texas, New Mexico, and Wyoming fall under Railroad Commission of Texas (RRC), New Mexico Oil Conservation Division (NMOCD), and Wyoming Oil and Gas Conservation Commission (WOGCC) regulations respectively; all reference API 6A for wellhead equipment.
Australia: The National Offshore Petroleum Safety and Environmental Management Authority (NOPSEMA) regulates offshore completions in the Browse, Carnarvon, and Gippsland basins. Well operators are required to submit a Well Operations Management Plan (WOMP) that includes tubing hanger specifications, pressure rating, seal type, and material certification. NOPSEMA guidance notes reference API 6A and ISO 10423 and require that hanger selection be justified in the completion engineering basis. The high-CO2 wells in the Carnarvon Basin (some above 70% CO2) drive selection of exotic corrosion-resistant alloys (CRA) such as 825 or 625 for hanger bodies, with special attention to crevice corrosion at seal interfaces.
Norway / North Sea: NORSOK Standard D-010 (Well Integrity in Drilling and Well Operations) defines the tubing hanger as a well barrier element (WBE) in the primary well barrier for producing wells. Norwegian Continental Shelf (NCS) operators must verify that the tubing hanger provides a tested, documented seal before the well barrier schematic (WBS) can be signed off. Equinor, Aker BP, and TotalEnergies Norway typically require dual MXM seals on all NCS completions regardless of pressure class, and annual well barrier verification testing is mandatory under the Petroleum Safety Authority Norway (PSA) facility regulations.
Middle East: Saudi Aramco Engineering Standard SAES-D-008 (Wellhead Equipment) mandates that all wellheads on Ghawar, Safaniya, and Khurais fields use tubing hangers with dual metal-to-metal seals regardless of H2S content, citing the high formation pressures and long well-life targets of 30 to 50 years. Abu Dhabi National Oil Company (ADNOC) references API 6A and additionally imposes internal qualification testing at the company's technical standards committee level. Kuwait Oil Company (KOC) Engineering Standards reference API 6A and require third-party inspection and material traceability certificates for all wellhead components including tubing hangers.
Fast Facts
- Typical tubing hanger bore size: 1.995 inches to 4.0 inches (50.7 mm to 101.6 mm) depending on tubing OD (1.900-inch to 3.500-inch OD tubing is most common)
- Maximum load bearing: Standard API 6A mandrel hangers are rated from 200,000 lb (90,718 kg) to 1,000,000 lb (453,592 kg) in the heaviest-duty designs for deep, large-bore wells
- Pressure classes: API 6A designates 2,000 / 3,000 / 5,000 / 10,000 / 15,000 / 20,000 PSI working pressure classes (138 / 207 / 345 / 690 / 1,034 / 1,379 bar)
- Temperature classes: API 6A K (to -60 degrees F / -51 degrees C), L (-50 degrees F / -46 degrees C), P (-20 degrees F / -29 degrees C), R (60 degrees F / 16 degrees C), S (140 degrees F / 60 degrees C), T (180 degrees F / 82 degrees C), U (250 degrees F / 121 degrees C), V (350 degrees F / 177 degrees C)
- Lead time for specialty hangers: HPHT or CRA-alloy tubing hangers typically carry 12 to 20 week manufacturing lead times from specialty shops such as Cameron (SLB), Baker Hughes, and Dril-Quip