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A leak suddenly occurred at the 24-inch common crude piping from the separators heading to the degassing boot inlets and the wet crude tanks in an oil gathering center. The initial observations showed the leak was due to a deep isolated pit and localized corrosion. Additional inspections by manual ultrasonic thickness (UT) and long range ultrasonic thickness (LRUT) measurements for the 24” common crude line showed similar deep isolated pits (up to 70% thickness reduction) scattered across the length of the 1100 meter piping.
A leak suddenly occurred at the 24-inch common crude piping from the separators heading to the degassing boot inlets and the wet crude tanks at an oil gathering center in Kuwait Oil Company. The initial observations showed the leak was due to a deep isolated pit and localized corrosion. Consequently, the piping spool was opened, deposits were collected for analysis and an action report was issued recommending replacing the leaky spool. Additional inspection by manual and long range ultrasonic thickness measurements for the 24” common crude line showed similar deep isolated pits (up to 70% thickness reduction) scattered across the length of the 1100 meter piping. This was extremely concerning since the facility has just been commissioned and been in service for 1.5 - 2 years only. Subsequently, an investigation was carried to determine the root causes for the failure concluded that an active Microbiologically Influenced Corrosion (MIC) possibly was taking place due to the influence of sulfate & iron reducing bacteria and methanogens. These different bacteria types formed biofilms at different pockets leading to deep isolated pitting, and the formation of iron sulfide layer found adhered at the 6 o’clock position along the length of the piping. The iron sulfide layer observed was confirmed to be present due to the activities of sulfate reducing bacteria and influenced by iron reducing bacteria and methanogens, since H2S was found in the crude stream at extremely low content in gas (1 ppm). Additionally, other factors such as flow velocity have contributed to the MIC and pitting / localized corrosion as it was found to be below 1 m/s, which promoted stagnation and stagnant conditions in the process stream. Further, calcium carbonates (CaCO3) played a major part in the observed damages, since it was formed non-uniformly across the length of the piping, promoting exposed pockets for biofilm formation, tubercles and under deposit corrosion. The results of this interesting investigation is presented in this paper.
Metal and its structures corrosion is a natural process. The process started and accelerated in the presence of electrolytes [1, 2]. Thus, it's highly encouraged to stop this electrolyte passage. One of the ways to resist the passage of electrolytes is by making a barrier. The most popular method of such a barrier is an organic coating which mainly comes from polymer resin along with pigments, and additives. Different organic coatings are being used to make a barrier that can ultimately protect the metals and their structures. Epoxy, polyurethane (PU), and acrylate coatings are widely being used for this purpose.
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Fusion bonded epoxy (FBE) is the primary coating used in North America for new pipeline construction and is strongly featured in the Middle East1. Pre-coated FBE pipe is routinely stockpiled and stored in large quantities at several locations close to pipeline right-of-ways. Once stockpiled, most of the pipesremain un-used until an inspection and remediation program is initiated2. Integrity projects purchase FBE coated pipe in advance and stockpile it until it is required. In addition, project delays and left-over pipe from completed projects can cause stockpiling for future use for undetermined periods of time. Under ultraviolet (UV) exposure in the presence of air, photooxidative degradation of FBE coatings occurs due to photometrical reactions arising from UV absorption.
Heater Treaters are designed for the removal of emulsifies and unwanted salts from crude oil. They purpose is to facilitate the oil and water separation by breaking emulsions by means of increasing the temperature of the oil, reducing its density and viscosity. A heater treater is a 3-phase separator vessel, equipped with fire tubes, that utilizes heat and mechanical separation devices to facilitate the separation of oil-water emulsions.