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B0688 CO2 Corrosion control in oil and gas production by M. B. Kermani, L. M. Smith PDF

By M. B. Kermani, L. M. Smith

ISBN-10: 1861250525

ISBN-13: 9781861250520

Addresses the stairs essential to layout oil and gasoline dealing with amenities contemplating key surroundings parameters which impression CO2 corrosion possibility in several components of the amenities. It considers corrosion keep an eye on by using corrosion allowance on metal and deployment of inhibitors. this can be the 1st rfile which tackles all facets important to deal with CO2 corrosion layout of all goods of oil box apparatus and amenities incorporating creation, processing and transportation

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Additional info for B0688 CO2 Corrosion control in oil and gas production

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A positive effect of molybdenum [49], silicon [44,49] and cobalt [39,49] has been reported, but a more systematic study is required to confirm this. 2. Effect of G l y c o l a n d M e t h a n o l Large quantities of glycol or methanol are often introduced into wet gas-producing systems to prevent and control hydrate formation which can cause plugging problems. Both of these chemicals, if present in sufficient concentrations can inhibit CO 2 corrosion. Of the two, glycol is much more effective and a correction can be made to the predicted corrosion rate to take this into account.

It is much higher for OS than WS, and it is i m p r o v e d by chemisorption and film polymerisation. It is a major feature for OS and batch treatments. Mechanical persistency expresses the ability to resist a peeling effect by the fluid flow. It is traditionally measured in flow channels or on rotating devices, at increasing shear stresses or mass transfer coefficients, and on bare surfaces. The relevance of this experimental method to field conditions is explained below. High shear stresses are invariably present in the field, at least locally.

E. reboil) the glycol/methanol after use in a system. Over time, the glycol may be partially decomposed and the pH value may decrease. In such a case, pH stabilising to obtain a system pH > 6 is necessary. Possible agents are MDEA or TEA. A combination of glycol and corrosion inhibitors is sometimes used. As many of the data available on corrosion predictions are laboratory data, a total risk evaluation can result in the need to plan for corrosion inhibitor injection and even implement this from start-up.

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B0688 CO2 Corrosion control in oil and gas production by M. B. Kermani, L. M. Smith


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