Now Hiring:
Are you a driven and motivated to join us?

CO2 pipelines risk assessment. Brittle fracture

Brittle Fracture in Dense Phase CO₂ Pipelines

The aim of this publication is to provide an overview on the problematic of assessing dense phase CO2 pipelines against brittle fracture. If you want to know more about it, contact us.

In a previous publication we made an introduction to the aspects to be accounted when assessing fracture control of dense-phase co2 carrying pipelines. As mentioned, one of the mechanism to be analysed is the named brittle fracture.

The brittle fracture mechanism arises as the result of the concurrence of an operating temperature below the ductile to brittle transition temperature of the material with a stress situation greater than the threshold stress for brittle fracture

To prevent brittle fracture, it is essential that the pipeline steel exhibits a ductile to brittle transition temperature lower than the specified Minimum Design Metal Temperature (MDMT) and that the pipeline is operating on the upper shelf of the ductile to brittle transition curve.

In order to avoid the occurrence of this phenomena it is necessary to ensure a correct material selection giving special attention to mentioned MDMT.

Minimum Temperatures Without Impact Testing for Carbon Steel Materials
Figure 1. Minimum Temperatures Without Impact Testing for Carbon Steel Materials. Source: ASME B31.3-2020

CO₂ Depressurization

The materials employed in the dense phase CO2 transportation and injection system may be exposed to low temperatures due to process events (e.g. depressurisation) and/or atmospheric conditions. Low temperatures can cause embrittlement in susceptible materials, resulting in brittle fracture. Materials shall be selected suitable for service at Minimum Design Metal Temperature (MDMT).

Potentially very low temperatures can result from unintended dense phase CO2 blowdown scenarios such as pinhole leaks or flange leaks.

Some certainly complex physical phenomena take place once this occurs:

  • CO₂ liquid flashing
  • Joule-Thomson effect in the produced CO₂ vapour downstream the leak hole
  • CO₂ real gas behaviour
  • Supersonic CO₂ vapour expansion downstream of the leak hole
  • Conversion of CO₂ gas internal energy into kinetic energy when flowing with high velocity as per fundamental law of conservation of energy
  • Conjugate heat transfer between flowing/expanding gas and the metal upstream, inside and downstream of the leak hole, friction is accounted for
  • A dilution with ambient medium downstream of the leak depending on the location of a leaked flange

The expansion of CO₂ from a high pressure cylinder to atmospheric pressure through a nozzle is ideally a constant enthalpy process, so the pressure decreases along a constant enthalpy line as the CO₂ passes through an orifice.

The discharge and dispersion of high-pressure CO₂ pipelines differs from the hydrocarbons pipelines in involving complex physics including cool temperature, phase transition, sonic multiphase flow, and heavy gas dispersion.

A schematic of the highly under-expanded jet is shown in figure below. An expansion barrel structure is generated at the nozzle lip as the flow expands into the atmosphere.

The schematic of the under-expanded jet
Figure 2. The schematic of the under-expanded jet. Source: B. J. L. Y. W. C. Teng Lin, “An Experiment on Flashing-Spray Jet Characteristics of Supercritical CO₂ from Various Orifice Geometries,” Frontiers in Energy Research, vol. 9, 2021.

The ratio Stagnation Pressure/Ambient Pressure is an important parameter to describe the expansion level. When this ratio is above 15, the shock waves diamond pattern will form.

Except for the intercepting shock in the interior of the jet, the Mach disc normal to the flow and it is unique for under-expanded jet. The flow front the Mach disc is supersonic, whereas the flow behind the Mach disc is obviously subsonic.

The flashing-spray jet structure has a significant impact on the cooling process that takes place on the metal in conditioning the extension of the low temperature fluid in contact with the pipe wall.

There are some other cases in which the shockwave system shows a fan-shaped structure instead of the mentioned barrel-shape. The Mach disc is unobserved in this cases the CO₂ flows radially after shock wave.

All the above mention applies to a multispecies fluid with the addition of the proper complexity that arise from the different species involved. Moreover, in the event of having a strong interaction between then it would be necessary to account it.

CFD analysis results from SDEA
Figure 3. Example of velocity field (left) and temperature (right) results from a previous CFD analysis performed by SDEA. Contour legend intentionally not included.
Tip: CFD assessments are essential to estimate MDMT under real depressurization and leakage scenarios, especially with non-linear phase transitions and supersonic expansions.
Aspect Consideration
Failure Mode Brittle fracture due to low temp + high stress
Prevention Proper MDMT selection, materials testing
Physical Mechanisms Flashing, Joule-Thomson, supersonic CO₂, phase shift
Analysis Tools CFD for velocity/temperature mapping
Standard ASME B31.3, figure used from 2020 edition

Let’s Talk Engineering

If your project involves dense phase CO₂ transport, SDEA can help you mitigate brittle fracture risks through CFD, MDMT assessment, and design consulting.

Contact our engineering team
Checkout Category Related Articles

More articles