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Cesium formate (CsFo) brines have been used as the drilling and/or completion fluids in oil and gas wells in need of high-density fluids.1,2 Multiple studies on corrosion of steels and corrosion resistance alloys (CRA) in formate environments have been reported in the literature.2-8 It was known that the formate brines could undergo significant decomposition to form hydrogen when in contact with catalytic surfaces which CRA can act as. Therefore, there have been concerns that the CRA may catalyze the decomposition of formate brines to accelerate the generation of hydrogen which in turn may embrittle certain CRAs and endanger the relevant well equipment.
Because of hydrogen generation from thermal decomposition of cesium formate, there were concerns that the use of cesium formate in certain applications may induce hydrogen embrittlement to CRA equipment after extensive exposure to elevated temperatures followed by cooling to low temperature under stress. This study focused on evaluating the severity of hydrogen embrittlement of seven nickelbased alloys at room temperature following exposure at elevated temperature to cesium formate of H2S/CO2 acid gases and consequently reduced pH. Unstressed slow strain rate (SSR) test specimens were previously exposed in an autoclave of cesium formate saturated with H2S/CO2 at an elevated temperature of 275 °F for 90 days. After exposure, significant hydrogen uptakes were observed under the tested conditions by measurement of total hydrogen concentration. The hydrogen-charged SSR specimens were then tested in air with 1 x 10-6 in./in./s strain rate at room temperature and compared with performance of the pristine specimens. In addition, three charged CRA alloys were also heated in furnace to release dissolved hydrogen and then tested in air. Two of the seven CRAs were also strained in situ in cesium formate at 275 °F.
Offshore oil production facilities are subject to internal corrosion, potentially leading to human and environmental risk and significant economic losses. Microbiologically influenced corrosion (MIC) and reservoir souring are important factors for corrosion-related maintenance costs in the petroleum industry.1 MIC is caused by sulfate-reducing prokaryotes (SRP), which can be Bacteria (SRB) or Archaea (SRA), with the main focus in literature being on SRB.2–5 The microorganisms most frequently reported in literature to be responsible for MIC are the SRB; Desulfovibrio, Desulfobacter, Desulfomonas, Desulfotomaculum, Desulfobacterium, Desulfobotulus, and Desulfotignum, and methanogens.2,5
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Carbon and low alloy steels (CS and LAS, respectively) used for exploration and production in the oil and gas (O&G) industry are normally exposed to environments that may contain H2S in a wide range of concentrations. In aqueous solutions, H2S acts as a cathodic poison.1,2 A cathodic poison inhibits the recombination of atomic hydrogen to H2, and as a result, favors its absorption by the metal.1,2 In the presence of a susceptible microstructure and the simultaneous effect of applied or residual tensile stress, a crack can nucleate and propagate, when a critical concentration of hydrogen is reached in the metal.3 This environmentally assisted cracking (EAC) phenomenon is known as Sulfide Stress Cracking (SSC).2 SSC is commonly addressed as a case of hydrogen embrittlement (HE) damage.2
The crude oil produced by fracking or hydraulic fracturing method are high in sulfur content (0.5%)1. The vast majority of vessels that are used in the petrochemical industry to store and transport materials are constructed using Carbon steel. Coating linings used for corrosion protection inside of vessels and tanks must perform under severe conditions such as an exposure to corrosive gasses ( H2S) and carbon dioxide as well as high temperatures, high pressures and often must withstand the cold wall effect and rapid decompression.