A computational procedure for predicting CO2 corrosion rates of carbon steels given the field conditions (e.g. CO2 partial pressure, temperature, velocity, solution composition, gas/liquid ratio) is desirable for use by the oil and gas industry. A model based on the current understanding of the mechanism and kinetics of the CO2 corrosion process has been developed. Starting from first principles, a computer program based on this model has been developed for predicting uniform CO2 corrosion rates in single phase flow in pipes in the absence of scale formation. An overview of the CO2 corrosion model and mechanistic aspects involved in this procedure are provided. CO2 corrosion rate predictions obtained using this program for various conditions (of velocity, CO2 partial pressure, pH and geometry) compare well with experimental data for similar conditions. This procedure provides a foundation which can be generalized to more complicated systems involving multiphase flows containing water, oil and gas. The computer program involves solving highly coupled non-linear equations. Program outputs include surface concentrations of the various chemical species at the given conditions which can be used to predict corrosion scale formation on the surface.

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