Prediction of corrosion inhibitor performance using simulated CO2/H2S environmental autoclave and flowloop tests

NACE - International Corrosion Conference Series

Volumn 1997-March, Issue , 1997, Pages

  Farquhar, G B ^a   Kane, R D ^b   Abayarathna, D ^b   Sanders, D H ^c  

^a Explor Technol 3901 Briarpark Dr   (United States)

^b CLI International Inc   (United States)

^c Texaco North Sea UK Co   (United Kingdom)

Author keywords

CO2 H2S corrosive environment; Corrosion inhibitor evaluation; Environmental flowloop testing; Laboratory testing of corrosion inhibitors

Indexed keywords

BLOOD VESSELS; CARBON DIOXIDE; CARBON STEEL; CORROSION RATE; LABORATORIES; PIPELINE CORROSION; PIPELINES; PRESSURE VESSELS; SEAWATER CORROSION; SHEAR FLOW; SHEAR STRESS; STEEL CORROSION;

CORROSIVE ENVIRONMENT; EVALUATION PROGRAM; FLOWLOOP; INHIBITOR FORMULATION; INHIBITOR PERFORMANCE; LABORATORY TESTING; LAMINAR AND TURBULENT FLOW; LINEAR POLARIZATION;

CORROSION INHIBITORS;

EID: 85046771598     PISSN: 03614409     EISSN: None     Source Type: Book Series    
DOI: None     Document Type: Conference Paper

References (4)

1. Simulation Sciences Inc. 1993, SimSci Pipephase, "Steady State Multiphase Simulator for Pipelines, Networks and Production Systems," Version 6.0, December 1993.
2. British Petroleum Company, 1994, B. P. Corrosion Inhibitor Selection Protocols, Flow Loop Protocol.
3. Personal Communication from Dr. Shi Liang Fu, Nalco Chemical Company, P. O. Box 87, Sugariand, Texas, U. S. A., 77014-1149.
4. G. B. Farquhar, 1994, Texaco EPTD TR 94-0276, "High Temperature-High Pressure Autoclave Evaluations of Corrosion Inhibitors for a North Sea Pipeline."