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The multicomponents of the produced water often results in the formation of the solid solution, such as BaxSr1-xSO4. The suspended solids collected from industry often show the presence of Sr2+ in the BaSO4 scale, indicating the formation of BaxSr1-xSO4 solid solution. Thus, it is important to study the solubility, kinetics and inhibition of the solid solution to have a better prediction of the sulfate scale deposition rate and amount. In this research, we will mainly focus on the effect of the incorporation of Sr2+ on the deposition rate of BaxSr1-xSO4 solid solution scale. The flow through system with two different reactors was used in the experiments. From the experimental results, we can find that the deposition rate of the BaxSr1-xSO4 solid solution decreased significantly with the increase of strontium concentration at a constant barium sulfate supersaturation. The deposition rate decreased up to six times when strontium concentration in aqueous phase increased from [Sr2+] = 0.5[Ba2+] to [Sr2+] = 8[Ba2+], all with SIBarite = 0.9. The decrease of the SI of the BaxSr1-xSO4 solid solution was found with the increase of Sr2+ in the aqueous phase. This might be the reason for the retardation of Sr2+ on BaxSr1-xSO4 deposition rate.
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Offshore projects today are demanding ever more reductions in both CapEx and OpEx. Tertiary structural products (eg handrails, gratings, ladders and platforms) made in steel may at first seem to be the lowest cost option, but steel is heavy and eventually suffers from corrosion which can be a significant drain on budgets and resources.The benefits of FRP (fiber reinforced polymer) tertiary structural products for offshore oil and gas projects can be very significant, with substantial weight reduction, lower installation costs and minimal maintenance. But how can these recognized FRP benefits against steel be translated into actual CapEx and OpEx savings when used in oil and gas projects?This aim of this paper is to offer answer to this question, by presenting a study of the projected Whole Life Cost and Value Proposition for the MARRS Offshore FRP Handrail using data drawn from the recent BP Clair Ridge Project.
Opportunity crudes are generally defined as petroleum crudes bearing a high level of sulfur, metals, or total acid number (TAN). These crudes are typically offered at a discounted value. Thus, refining such crudes carries with it a lucrative incentive. However, due to the above-mentioned characteristics, processing such crudes presents numerous operational challenges as well, such as naphthenic acid corrosion, which is commonly associated with the high TAN content in these crudes. In refinery units such as the crude distillation tower, these carboxylic acids react with the iron atoms of the metal surfaces to produce oil soluble iron carboxylates.1,2 The continued formation of such complexes would then erode the metal surface. Equipment failure due to such corrosion results in shutting down a large segment or the entire refinery. Therefore, establishing a means for mitigating this type of corrosion is paramount for processing crude oils with an elevated TAN due to naphthenic acids.
In this paper, a detailed analysis was performed on weld longitudinal cracks (Weld Bond Cracks can be mistaken for Hydrogen Induced (HIC) cracks.) appeared after HIC testing of Electric Resistance Weld pipes (ERW) 8”-16” NPS 0.375”-0.5” WT carbon steel grade X60 which was welded using a 150-hertz induction heating has been studied in relation the development of hydrogen induced cracking. A comprehensive experiment and testing was done to evaluate both mechanical and microstructural properties of the cracks. The result of the study indicates that raw material failure to meet HIC resistance requirements may appear on the ERW welded pipes due to Steel re-oxidation, Low tundish level, and Double calcium treatment during steel making
Top of the line corrosion (TLC) is a phenomenon encountered in the transportation of wet gas, where temperature differences between the pipelines and the surroundings lead to condensation of water and subsequent metal degradation. This kind of corrosion occurs due to the condensation of saturated vapors present in the unprocessed gas stream which collects on the internal surface of the cold pipe wall. The condensed liquid contains hydrocarbons and water. It forms a thin film and/or droplets of liquid on the pipeline. The condensed water phase can be, at least initially, very corrosive to typical pipeline (made of carbon steel), because it contains dissolved acid gases (such as carbon dioxide [CO2] and hydrogen sulfide [H2S]) and organic acids (such as acetic acid [CH₃COOH]).1
Black Powder is a phenomenon that all oil and gas companies are facing and presenting a variety of problems in associated processing equipment and pipelines, such as flow inefficiency, product contamination, wear, plugging and under deposit corrosion, among others. Another major concern is the possible formation of elemental Sulfur (S8), which could be produced as a by-product of oxidation of iron sulfides. It also can be produced from H2S dissociation at elevated temperatures or by microbiological reactions, involving the reduction of sulfate.