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In the oil and gas industry, oil country tubular goods and linepipes are exposed to the wet H2S environment (sour environment) in some cases. The presence of H2S promotes hydrogen entry into steel due to the catalytic action of H2S. The absorbed hydrogen enhanced by H2S affects hydrogen embrittlement.
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Next generation concentrating solar power (CSP) plants may employ supercritical CO2 (sCO2) for the power block to achieve 50% electrical efficiency at 700°C. The goal of this project was to develop a long-term (100 kh) lifetime model for sCO2 compatibility using 10-15 kh laboratory exposures. Nickel-base alloys 740H 282 and 625 and Fe-base austenitic alloy 25 were evaluated in 500-h cycles at 1 and 300 bar and 1-h and 10-h cycles in 1 bar industrial grade CO2. All of the alloys have shown low mass gains in 500-h cycles after 10000 h exposures similar to exposures in laboratory air. However alloy 25 showed accelerated mass gain after ~1500 h of cumulative exposure in 10-h cycles at 700° and 750°C and 1-h cycles at 750°C. The Cr-rich oxide broke down allowing Fe-rich oxide formation. Characterization of the reaction products as a function of time will be presented. Research sponsored by the U.S. Department of Energy Office of Energy Efficiency and Renewable Energy Solar Energy Technology Office.
High-strength aerospace aluminum alloys, such as AA7075-T651, are susceptible to environmental assisted cracking (EAC) under the right combinations of stress, environment, and microstructure. EAC presents a serious risk to structures and equipment operated in corrosive conditions. Studies of EAC in aluminum alloys have highlighted the importance of both anodic dissolution and hydrogen embrittlement to EAC initiation and propagation.1–4 The EAC response of alloys under variable atmospheric conditions is of particular importance for assessing material performance for aerospace applications.
Carbon steel is the main construction material in HYDROFLUORIC ACID (HF) alkylation units. Carbon Steel has good corrosion resistance to anhydrous HF (AHF) below 160 degrees fahrenheit (71 C). The corrosion resistance is due to the formation of an inorganic iron fluoride scale on the carbon steel surface that protects the steel from futher corrosion. The presence of an adherent and continuous scale is essential in keeping the corrosion rate at a minimum.
Type 304 stainless steel is commonly used in pressurized water reactor (PWR) primary circuits, where it is exposed to high temperature, high pressure water. Combination of material and environment influence the oxidation behavior in these systems. In addition to oxidation of the surface, 304 is also susceptible to stress corrosion cracking and corrosion fatigue, which are both types of environmentally assisted cracking, or EAC. EAC is a function of prior material condition, environment, and stress induced during exposure.
Hydrocarbon extracted from oil and gas wells is typically accompanied by the production of brines. Salt concentration or salinity is a general characteristic of brines that can vary from 1000 to 400000 mg/l. The effect of salt concentration on uniform CO2 corrosion has been studied in the past however most of these studies have been performed at low salt concentrations usually between 1 to 3 wt.% NaCl. Moreover no true mechanistic study of corrosion has been done to cover the higher ranges of salt concentration. In this study CO2 uniform corrosion of an API X65 carbon steel was studied by weight loss (WL) linear polarization resistance (LPR) and potentiodynamic polarization methods in a range of NaCl concentration from 0 to 20 wt.%. The WL and LPR results both showed a maximum in the corrosion rate at 1 wt.% NaCl. The polarization curves showed that the key change due to higher salt concentrations was in the cathodic limiting current.Keywords: CO2 uniform corrosion carbon steel high salt concentration weight loss linear polarization resistance potentiodynamic polarization
Large amounts of water can be produced during extraction of hydrocarbons from underground reservoirs.1 It is well understood that produced waters usually contain high amounts of dissolved salts, up to 28 wt.%.2 In addition to salts, dissolved corrosive gases (CO2 and H2S) are present in produced water, which make the mixture a complex corrosive environment for metallic parts and equipment used throughout the production process.
Alloy UNS N08825 is a nickel-iron-chromium alloy with additions of molybdenum copper and titanium. The alloy was designed for applications in the chemical process industry as well as in oil and gas industry.UNSN08825 shows an excellent corrosion behavior in sour service environment and a high resistance to stress corrosion cracking and sulfide stress cracking. However due to its low molybdenum content of 3 wt.% alloy UNSN08825 has limited resistance to pitting and crevice corrosion in chloride containing environments.A new advanced version of UNS N08825 which will be called in this paper UNS N08825 CTP with higher molybdenum content was developed to improve its corrosion resistance. Previous corrosion tests showed an increased critical pitting temperature of the new alloy. Based on these data further corrosion tests were performed.An important factor that has a detrimental influence on the corrosion behavior is the sensitization of the material. To simulate the real life application of this alloy different heat treatments were performed especially under critical temperatures where detrimental phases occur. Pitting corrosion intergranular corrosion and susceptibility to hydrogen embrittlement were investigated within the testing program as well as stress corrosion cracking (SCC) resistance.This paper will present an overview of the corrosion behavior of this new and improved version of UNS N08825 which was called Alloy 825 CTP.
Nickel-Aluminum Bronze (NAB) and Copper-Nickel alloys (CuNi) are commonly used in seawater environment in raison of their strength combined with a good corrosion resistance and a high resistance to biofouling. However localized corrosion failures have been reported often attributed to abnormal service conditions. The effect of several service condition parameters on the localized corrosion of NAB and CuNi alloys 90/10 and 70/30 have been investigated in natural seawater. It includes flow conditions (flowing quiescent and stagnant) chlorination sulphide pollution and crevice geometries. Both indoor and outdoor exposures (biodeposit promoting conditions) have been tested in temperate and in tropical seawaters. The global stability of the protective oxide layer of the tested copper-based alloys was mainly affected by sulphide pollution in aerated seawater (general corrosion). Under the tested conditions localized corrosion under-biodeposit clearly appeared as the critical failure for the tested alloys. The conditions in which biodeposit appeared critical for copper-nickel alloys was investigated. The current for cathodic protection of NAB in natural seawater have also been investigated as function of flow rate.