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02253 USE OF CORROSION & FLOW MODELING FOR CORROSION ASSESSMENT OF AN OIL & GAS FIELD

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Product Number: 51300-02253-SG
ISBN: 02253 2002 CP
Author: Dr. Ali N Moosavi and Dr. Gareth John
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As part of a recent planning stage for a new oil and gas field development in North East Abu Dhabi (NEAD) a major corrosion risk assessment and material selection review has been carried out. This review covered corrosion predictions, material selection and corrosion control planning for production tubulars, flow lines and trunklines as well as corrosion risk assessment for the downhole injection tubulars. This oil and gas field is somewhat unique in being designed for secondary recovery based on water alternating gas (WAG) injection. The corrosion review used two different corrosion modeling systems as well as flow prediction software. The differences in the outcome of the two packages and the overall conclusions for the corrosion risk assessment are outlined in this paper.
As part of a recent planning stage for a new oil and gas field development in North East Abu Dhabi (NEAD) a major corrosion risk assessment and material selection review has been carried out. This review covered corrosion predictions, material selection and corrosion control planning for production tubulars, flow lines and trunklines as well as corrosion risk assessment for the downhole injection tubulars. This oil and gas field is somewhat unique in being designed for secondary recovery based on water alternating gas (WAG) injection. The corrosion review used two different corrosion modeling systems as well as flow prediction software. The differences in the outcome of the two packages and the overall conclusions for the corrosion risk assessment are outlined in this paper.
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02274 EFFECTIVENESS OF CORROSION INHIBITORS IN RETARDING PROPAGATION OF LOCALISED CORROSION

Product Number: 51300-02274-SG
ISBN: 02274 2002 CP
Author: A. Turnbull, D. Coleman, A.J. Griffiths, P.E. Francis, and L. Orkney
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In many service applications excursions in solution chemistry, temporary loss of inhibitor, or transient increases in temperature may give rise to localised corrosion. To test the return of inhibition when the loss is remedied, the use of an artificial pit has been investigated using simulations of cooling water and of of oil production formation water.
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