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07562 AN INTEGRATED TOOL TO SELECT OCTG MATERIALS

Picture for 07562 AN INTEGRATED TOOL TO SELECT OCTG MATERIALS
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Product Number: 51300-07562-SG
ISBN: 07562 2007 CP
Author: Teresa E. Perez, Claudio Morales, Sergio Ferro, and Marcela Goldschmit
Publication Date: 2007
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The aim of the present paper is to describe an application developed to address the selection of materials to be used as tubing and casing in oil and gas field production facilities, based on corrosion performance. The first step is the prediction of the flow pattern and its characteristics, using a numerical model developed in house. These results are used as input to predict the corrosion rate of carbon and low alloy steels in CO2 rich environments. Additionally, the carbon and low alloy steel selection from the sour resistance point of view is carried out by following NACE MR0175/ISO 15156 part 2. The behavior of different CRAs is estimated through working windows information.
The aim of the present paper is to describe an application developed to address the selection of materials to be used as tubing and casing in oil and gas field production facilities, based on corrosion performance. The first step is the prediction of the flow pattern and its characteristics, using a numerical model developed in house. These results are used as input to predict the corrosion rate of carbon and low alloy steels in CO2 rich environments. Additionally, the carbon and low alloy steel selection from the sour resistance point of view is carried out by following NACE MR0175/ISO 15156 part 2. The behavior of different CRAs is estimated through working windows information.
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07565 Effect of Mercaptans and Other Organic Sulfur Species on High Temperature Corrosion in Crude and Condensate Distillation Units

Product Number: 51300-07565-SG
ISBN: 07565 2007 CP
Author: J. D. Jong, A. Saunders-Tack, M. Sargent, A. M. Etheridge, W. C. Fort, and N. Dowling
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The corrosivity of four mercaptans and selected crude oil fractions were measured in lab tests. Conclusion: Mercaptan corrosion can contribute significantly to the total sulfur related corrosion in the temperature range 235–300°C, which agrees with observations of elevated temperature corrosion in refinery distillation equipment.
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