CO2 corrosion prediction by use of the Norsok M-506 model Guidelines and limitations

NACE - International Corrosion Conference Series

Volumn 2003-April, Issue , 2003, Pages

  Olsen, Stein ^a  

^a STATOIL   (Norway)

Author keywords

Carbon dioxide; Carbon steel; Corrosion modeling

Indexed keywords

CARBON DIOXIDE; CARBON STEEL; CORROSIVE EFFECTS; FORECASTING;

CORROSION MODELING; CORROSION PREDICTION; INPUT PARAMETER; MATERIAL SELECTION; MODELING GUIDELINES; NORSOK STANDARD; OIL INDUSTRIES; PREDICTION MODEL;

STEEL CORROSION;

EID: 85044269284     PISSN: 03614409     EISSN: None     Source Type: Book Series    
DOI: None     Document Type: Conference Paper

References (7)

1. R. Nyborg, Overview of CO2 Corrosion Models for Wells and Pipelines, paper no 233, CORROSION/02, (Houston, TX; NACE International, 2002)
2. NORSOK Material Standards, http://www.nts.no/norsok/
3. NORSOK Standard M-506, CO2 Corrosion Rate Calculation Model, http://www.nts.no/norsok/m/m50601/m50601.htm
4. NORSOK Standard M-001, Materials Selection, http://www.nts.no/norsok/m/M-001r2.pdf
5. NORSOK Standard M-002, Materials Requirement Justification, private communication.
6. A. M. K. Halvorsen and T. Søntvedt, CO2 Corrosion Model for Carbon Steel Including aWall Shear Stress model for Multiphase Flow and Limits for Production Rate to Avoid Mesa Attack, paper no 42, CORROSION/99, (Houston, TX; NACE International, 1999)
7. C. DeWaard, U. Lotz, D.E. Milliams, Predictive Model for CO2 Corrosion Engineering in Wet Natural Gas Pipelines, paper no 577, CORROSION/91, (Houston, TX; NACE International, 1991)