Corrosion at high CO2 pressure

NACE - International Corrosion Conference Series

Volumn 2003-April, Issue , 2003, Pages

  Hesjevik, S M ^a   Olsen, S ^a   Seiersten, Marion ^b  

^a STATOIL   (Norway)

^b INSTITUTE FOR ENERGY TECHNOLOGY   (Norway)

Author keywords

Carbon steel; Inhibitor; Liquid CO2; pH regulation

Indexed keywords

ALLOY STEEL; CARBON DIOXIDE; CARBON STEEL; CORROSION RATE; PH; PIPELINE CORROSION;

ADDITIONAL EQUIPMENT; CORROSION PROBLEMS; EFFECT OF PH; FILM-FORMING; HANDLING COSTS; INHIBITOR; OFFSHORE INSTALLATIONS; PH REGULATION;

STEEL CORROSION;

EID: 85021229278     PISSN: 03614409     EISSN: None     Source Type: Book Series    
DOI: None     Document Type: Conference Paper

References (6)

1. IEA Greenhouse Gas R&D Programme (IEAGH), www. ieagreen. org. uk
2. Wildenborg T., Cost of CO2 Sequestration by Underground Storage, Greenhouse Issues, 47, 2000
3. Skovholt, O., CO2 Transportation System, Energy Conversion and Management, 34(9-11) 1993, 1095-1103
4. M-506, CO2 Corrosion Rate Calculation Model, Rev. 1, June 1998
5. King, M. B. et al., Journal of Supercritical Fluids, 1995, 5, 296-302
6. Seiersten M., CORROSION/2001, paper No. 1042 (Houston, NACE International)