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The selection of a coating for suitable use on the exterior of a pipeline is an important consideration due to the safety and cost consequences of potential corrosion. Because there are numerous fusion bonded epoxy (FBE) mainline and field joint coating systems available, the selection of the optimum coating system is as much an art as a science.
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Corrosion rates in model oil sands coarse tailing slurries were investigated using a linear polarization resistance probe. Pilot-scale horizontal slurry flow loop of either unimodal (sand) or bimodal (sand and rocks) solid particles distribution mixed with municipal water.
With the success of the SSPC painting contractor certification programs (PCCP) and increasing Owner requirements for both quality control (QC) by the contractor and quality assurance (QA) by third party inspectors, there is more confusion than ever over which types of inspections, and to what level of detail, should be performed by whom.
Producing quality work on time and within budget is the key to a profitable paint job. This presentation details a systematic approach for painting contractors on the key elements of profitability ― everything from managing labor and job cost to selecting quality products for better productivity is examined.
The construction industry has struggled to fully embrace the philosophy of defect prevention rather than detection as a quality objective. Quality is more often discussed in sales presentations and marketing literature than in strategic plans or board meetings. This paper explores quality principles and methodologies employed in the manufacturing industry over the past twenty years that have resulted in measurable performance improvements yet are not adopted by the construction industry.
MIC-causing microorganisms were investigated in a 16” diameter and 9.6 km long injection water pipeline. Nitrate was added to the water and pigging debris from the pipeline showed that both sulfate-reducing bacteria (SRB), nitrate-utilizing bacteria, and methanogens were present in numbers of 105 – 106 cells/g.
In Corrosion/2021, the authors introduced a molecular mechanistic model that quantifies and predicts simultaneous naphthenic acid and sulfidation (SNAPS) corrosion rates. During Corrosion/2022, we presented the mechanistic corrosion prediction framework describing the molecular basis of the model’s reactions, kinetics, and mass transport of reactive organic sulfur compounds (ROSC) to vessel walls. In this molecular model, sulfidation corrosion is calculated for direct heterolytic reaction of ROSC with solid surfaces.
Underground natural gas storage (UGS) is an important component of the overall natural gas transportation and distribution system. It enables the utilities to supply natural gas during high seasonal demand periods and store gas during periods of lower demand. There are approximately 627 underground gas storage sites worldwide with a working gas capacity of 319.3 Billion m3 ( about 11.8 Trillion Cubic feet). The U.S. has a total of 414 natural gas storage fields, out of which 25 are inactive.
Time tested and proven methods to control corrosion are use of appropriate materials coating cathodic protection (CP) and corrosion inhibitors. All these methods must of selected based on rigorous and quantitative evaluation in the laboratory i.e. laboratory evaluation is the first step and it includes:<ol><li>Establishment of appropriate laboratory methodologies </li><li>Establishment of step by step procedures to conduct evaluation using the appropriate laboratory methodologies identified</li><li>Comparison of the test results obtained with standard reference test results (published by Standards making organizations such as NACE International ASTM International and CSA International based on inter-laboratory tests carried out under standard conditions)</li></ol>The above three steps are religiously and routinely carried out in the evaluation of materials coatings and CP and such requirements are incorporated in the regulations. Some common standards used for this purpose are:<ul><li>ISO15151/NACE MRO175 “Petroleum and Natural Gas Industries – Materials for Use in H2S-Containing Environments in Oil and Gas Production”</li><li>NACE SP169 “Control of External Corrosion on Underground or Submerged Metallic Piping Systems” – See Criteria for CP (On-potential OFF-potential and 100-mV criteria)</li><li>CSA Z245.30 “Field-Applied External Coatings for Steel Pipeline Systems” – See for example one acceptance criteria: of cathodic disbondment: 24-hour cathodic disbondment test at 65oC producing less than 6.5 mm radius disbondment.</li></ul>The operators (e.g. laboratory technicians or field technologists) equipment and materials are qualified based on these criteria and these criteria are used as regulatory requirements in various countries. However such quantitative fundamental first step was not religiously followed in the evaluation corrosion inhibitors for oil field application. To address this several standards have been published over the past decade including ASTM G170 G184 G185 G202 G205 and G208 and NACE Technical Report 31215 (Laboratory Evaluation of Corrosion Inhibitors Used in Oil and Gas Industry) and some standards are being developed including NACE TG 550 “Standard Recommended Practice on Corrosion Inhibition Management for Oil and Gas Fields”.This paper:<ul><li>Presents tools techniques and data currently available to establish quantitative evaluation of corrosion inhibitors in the laboratory</li><li>Deliberates the responsibilities of oil and gas owners/operators tool developers inhibitor supplying companies inhibitor testing laboratories and regulatory body in establishing quantitative evaluation of corrosion inhibitors in the laboratory</li><li>Presents steps to effective and economically control internal corrosion using corrosion inhibitors in the oil and gas production transmission storage and distribution environments.</li></ul>