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With changes in environmental regulations a number of operators have moved from seawater injection to produced water reinjection and others have used produced water reinjection as a way to reduce/mitigate the potential sulphate scale risk by reducing the amount of sulphate rich seawater being injected into their reservoirs. The paper will focus on three case study fields looking into the control of the scale risk within the topside process, water injector wells and the evolving scale risk within the production wells. Data from North Sea fields will be presented which shows the challenge experienced within the production wells as initial injected seawater (or low sulphate seawater) is displaced by injected produced water. The change in produced water composition with time showed a significant extension in the scale risk envelope due to produced water reinjection with respect to sulphate scale formation relative to what would have been expected with only seawater injection. The expected trend of reducing barium ion concentration with time was reversed with produced water breakthrough (enhancing the barium and strontium ion concentrations) leading to a much longer period over which scale squeeze treatments were required to be applied. Along with the prolonged scale risk envelope the tracking of scale squeeze treatments became a challenge due to production of degraded phosphonate scale inhibitor which was present in the produced water (topside scale inhibitor and re injected squeeze scale inhibitor) leading to uncertainty in the actual scale squeeze inhibitor concentration where phosphonate scale inhibitor was being utilised. The lessons learned from this study are that changes in scaling potential within a PWRI system require to be carefully assessed prior to the onset of PWRI. While control of scale issues within the topside process and water injector wells has proved easy to predict and manage, the extended scale risk and challenges of tracking squeeze treatment performance need to be considered as this may present a significantly higher operation cost for effective scale management.
With changes in environmental regulations a number of operators have moved from seawater injection to produced water reinjection and others have used produced water reinjection as a way to reduce/mitigate the potential sulphate scale risk by reducing the amount of sulphate rich seawater being injected into their reservoirs. The paper will focus on three case study fields looking into the control of the scale risk within the topside process, water injector wells and the evolving scale risk within the production wells. Data from North Sea fields will be presented which shows the challenge experienced within the production wells as initial injected seawater (or low sulphate seawater) is displaced by injected produced water. The change in produced water composition with time showed a significant extension in the scale risk envelope due to produced water reinjection with respect to sulphate scale formation relative to what would have been expected with only seawater injection. The expected trend of reducing barium ion concentration with time was reversed with produced water breakthrough (enhancing the barium and strontium ion concentrations) leading to a much longer period over which scale squeeze treatments were required to be applied. Along with the prolonged scale risk envelope the tracking of scale squeeze treatments became a challenge due to production of degraded phosphonate scale inhibitor which was present in the produced water (topside scale inhibitor and re injected squeeze scale inhibitor) leading to uncertainty in the actual scale squeeze inhibitor concentration where phosphonate scale inhibitor was being utilised. The lessons learned from this study are that changes in scaling potential within a PWRI system require to be carefully assessed prior to the onset of PWRI. While control of scale issues within the topside process and water injector wells has proved easy to predict and manage, the extended scale risk and challenges of tracking squeeze treatment performance need to be considered as this may present a significantly higher operation cost for effective scale management.
Despite the progress made on the expansion of scale inhibitor (SI) product selection over the years, significant challenges due to mineral scaling persist. Though multiple scale inhibitor chemistries are available for mild to moderately severe conditions, there are limited scale inhibitor options that can effectively manage mineral scaling for harsh production environments. Therefore, the purpose of this study was to develop a novel scale inhibitor for severe production conditions such as those encountered in Pre-Salt formations. A synthetic strategy was implemented to develop new scale inhibitors based on terpolymers. From the multiple polymers synthesized, the best candidates were pre-selected based on thermal stability, brine compatibility and static bottle tests at 70°C. Standard dynamic scale loop (DSL) tests were then conducted to evaluate the performance of the new polymers and their corresponding blends. Test conditions simulated various production environments for Pre-Salt development. Our studies indicated that the novel scale inhibitor showed temperature stability for upwards of 60°C for 7 days and 4°C and 40°C for 30 days and compatibility with very high TDS brine (> 200k mg/L) even at elevated temperature (130⁰C). Furthermore, the final synthesized polymer showed the best stability and overall performance under these conditions compared to that of a commercial product and other synthesized products tested. It was also demonstrated that a synergistic effect between the final polymer and phosphonate in the final blend was responsible for further improved performance.
Control of inorganic sulphate and carbonate scales with polymer and phosphonate based scale inhibitors is well established within the oilfield chemical industry. The potential for synergistic interactions with blends of these chemical types to give reduced treatment rates, lower chemical discharge volumes and potentially lower treatment cost specifically for carbonate scale control and better energy efficiency, is less well understood. This paper presents the selection and field trial application of such a synergistic blend designed to control severe scaling within produced fluid heaters on a North Sea platform, however this blend has the potential to be applied in other environments such as CO2 WAG production systems, heaters and heat exchangers, for example. Inhibitor performance tests were carried out to evaluate inhibition of a range of single component inhibitors before blends of these chemicals were evaluated to try to reduce the inhibitor concentration required to control both calcium carbonate (saturation ratio, SR 550, mass 1100mg/l) and barium sulphate (SR 55, mass 450mg/l) scale formation. For this challenging carbonate scale environment at high temperature (105°C), it was observed that a blend of a polymer (carboxylic acid functionalized polymer) and the currently applied phosphonate was more effective than either of the components by themselves, suggesting synergistic interaction. Results from the initial field trial of the synergistic blend are presented with monitoring methods outlined to confirm that the formulation is as effective as the laboratory evaluated tests suggested. The initial trial started at the incumbent product injection rate for 1 week with differential pressure across the topside heaters, fluid flow rate and fluid heating performance being trended to confirm scale control prior to a 20% reduction in treatment rate being applied for 1 week with a further reduction of 40% of the incumbent being applied for another 7 days prior to the full dose rate of the incumbent chemical being reinstated to allow full review of the trial results. The methods outlined in this study demonstrate the potential to reduce chemical treatment rate, cost and environmental impact by evaluating the synergistic interaction of the current range of commercially available scale inhibitors and therefore eliminating the high registration costs and time associated with bringing a new molecule to market. This study also offers the potential for synergistic blends to be utilized to inhibit severe carbonate scales in challenging environments including extreme calcite scaling environments such as CO2 WAG production, high temperature topside heaters, alkaline surfactant polymer flooding and heat exchangers.
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