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The current paper presents a study on corrosivity of produced water and make-up water on UNS G10180 carbon steel in simulated in-situ thermal operations.
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Corrosion of ESPs in oil production from downhole well fluids (CO2, H2S, Cl-). Materials and their performance are also discussed. Selection of ESP materials in different applications is examined.
A study on the corrosivity of field produced water obtained from in-situ oil sands operators to UNS G10180 carbon steel. Rotating cylinder electrode (RCE) and rotating cage autoclave (RCA) systems were used as test methods. The susceptibility of the carbon steel to pitting was also evaluated.
Water-handling oil producing facilities often become target for microbial contamination because treated waters are not sterile – they are inhabited by various microorganisms and contain sufficient inorganic and organic nutrients to support microbial growth. The bacterial contamination and bioburden are to extravagate easily if environmental conditions in the facilities, for instance, moderate temperature (<45C) and salinity (<50 g/l TDS), favor microorganisms. Growing bacterial population distributes along the system and forms biofilms on the surfaces of pipelines, valves, vessels, tanks, etc. Such spreading of free-floating (planktonic) and sessile (biofilm) bacteria in industrial systems is referred to as biofouling.
In this paper we describe a case study in which we compared several available methods including viabilitypolymerase chain reactionfor measuring the effectiveness of biocide treatment.
Crevice corrosion is a geometrical-dependent type of localized attack that occurs in occluded regions where a stagnant and corrosive electrolyte is in contact with the surface of a passive metal1,2. Crevices are present in all industrial designs and can lead to major failure since their detection is often challenging3,4. Main strategies for the prevention and mitigation of crevice corrosion include design awareness and adequate materials selection5.
Waterflooding is a common secondary recovery technique where injection water (IW) is used to maintain reservoir pressure and improve oil recovery. During such operations, the mobile hydrocarbon phase is displaced along with formation water (FW) toward producing wells. The resulting produced water stream is a blend of FW and IW; these waters can be incompatible resulting in dissolved ions to precipitate out of solution as mineral scale.
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.
Coiled tubing is defined as a continuous tubular product that is used for oil and gas well interventions. Its popularity continues to grow due to its versatility and speed of operation. Though superior grades of metal alloys exist in terms of corrosion resistance, coiled tubing operations primarily employ high-strength low-alloy steels because of their availability, lower cost and weldability. The low-alloy steel can also be thermo-mechanically controlled to elicit specific material properties, such as yield strength and ductility. These coiled tubing steels are often introduced into potentially corrosive downhole conditions, therefore proper testing must be completed to ensure adequate corrosion protection prior to job execution. Downhole corrosive conditions often encountered include; oxygen saturated fluids, elevated temperatures, exposure to oxidizing agents, hydrochloric acid and highly concentrated brines. Often these fluids will be recirculated in a closed loop system, consistently re-exposing equipment to potentially damaging conditions. Frequently, these challenging conditions faced are tested individually with pressurized mass loss coupon testing at bottom hole conditions. However, due to a recent coiled tubing incident in which the coiled tubing pipe had completely parted downhole, the post-job incident investigation involving SEM and metallographic analysis revealed pitting corrosion throughout the tubing, despite the pre-job testing performed indicating adequate acid corrosion protection for the entirety of the job. A literature review indicated very little research was available involving the possible interaction of brine solutions and diluted acid on coiled tubing carbon steels. This paper aims to investigate the possible corrosive interactions between salt brines and inhibited acid blends at elevated temperatures on high grade coiled tubing coupon samples through metallographic examinations and mass loss tests in pressurized heated cells. Coiled tubing coupons will be exposed to a variety of acid blends diluted with a 10% brine (8% wt NaCl and 2% wt CaCl2) or fresh water to investigate the possibility of corrosion enhancement between saline fluids in a diluted acid system.
Produced water recycling for hydraulic fracturing (fracking) operations has been an increasingly common practice to support oil and gas development in the Permian Basin. Aside from the economic benefits associated with reusing the water produced which is a byproduct of oil and gas operations, recycling reduces both the need for sourcing water (brackish or fresh) from the environment as well as the volume of produced water requiring disposal. Produced water ponds support successful recycling by providing temporary storage of recycled water and volume buffer for fracking. Raw produced water is usually treated in recycling facilities before being stored in the ponds.