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Evaluation of Viscosity Loss of Viscosified Brine Solutions Due to Shear Degradation in Distribution System Components

机译:粘性盐水溶液粘度损失引起的分布系统组分剪切劣化评价

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High molecular weight HPAM’s tend to be highly shear sensitive. Various components of polymer mixing and distribution systems pose risk to the integrity of HPAMs due to high shear experienced at valves, chokes and other flow control devices. At a minimum, this risk can severely impact chemical EOR operating cost due to polymer degradation and consequential viscosity loss of the injectate. Low-shear, low-cost polymer injection distribution systems have the potential to reduce polymer usage, maintain injection stream viscosity, and enable integration into brownfield facilities. Lower viscosity losses translate into optimized operating and capital cost for CEOR pilot and full field projects. The objective of this work was to determine the equipment (piping), process, and polymer parameters that affect viscosity loss due to shear degradation. In this work, polymers were evaluated from two different vendors. The effects of molecular weight, chemical concentration, and brine salinity on polymer sensitivity to viscosity loss due to shear degradation were investigated. Polymer solutions were either blended on site or purchased pre-blended in synthetic brine solutions. Pumped by a positive displacement, low-shear pump, the solutions flowed through a mass meter and were delivered to a distribution system component at various flow rates. For flow control devices, pressure differentials were adjusted at fixed flow rates. Polymer solution samples were collected upstream and downstream of the tested component. Samples were taken in no-shear sample collectors. Pressure upstream and downstream of the test component and flow rate were recorded during the flow test. Viscosity was measured with a Brookfield viscometer at ambient temperature. When higher concentration solutions were tested, viscosity was measured of diluted samples at target concentration to determine amount of shear degradation as evidenced by viscosity loss. Results indicate that viscosity degradation of polymer solutions does occur in flow control devices and is directly correlated to pressure differential across the pipe device. Internal geometry has little impact on the amount of degradation. Velocity has little impact on the amount of degradation. Polymer molecular weight and structure both affect the amount of degradation due to shear as does solution concentration. Generally, viscosified brine solutions will lose viscosity when flowed through devices with greater than 50 psi differential pressure in the range of 15-50% of initial viscosity. Using more concentrated polymer streams and diluting to target concentration after flow control will reduce the amount of viscosity loss. Based on the laboratory results, design and operating condition, recommendations can be made for polymer injection distribution systems to minimize shear degradation of the flowing viscosified brine stream.
机译:高分子量HPAM往往是高度剪切敏感性。由于阀门,扼流圈和其他流量控制装置的高剪切,聚合物混合和分配系统的各种组分对HPAM的完整性造成风险。至少,由于聚合物降解和后续粘度丧失,这种风险可能会严重影响化学EOR运营成本。低剪切,低成本的聚合物注射配电系统有可能降低聚合物使用,维持注射流粘度,并实现棕色地面设施。降低粘度损失转化为CEOR PILOT和全场项目的优化运营和资本成本。这项工作的目的是确定影响由于剪切劣化引起的粘度损失的设备(管道),方法和聚合物参数。在这项工作中,来自两个不同的供应商评估聚合物。研究了分子量,化学浓度和盐水对聚合物敏感性对抗剪切降解引起的粘度损失的影响。聚合物溶液在位点上混合或在合成盐水溶液中预先混合。由正排量,低剪切泵泵送,溶液流过质量计,并以各种流速输送到分配系统部件。对于流量控制装置,以固定流速调节压差。将聚合物溶液样品收集在测试组分的上游和下游。样品在无剪切样品收集器中拍摄。在流动试验期间记录了试验组分和流速的压力上游和下游。在环境温度下用Brookfield粘度计测量粘度。当测试更高浓度的溶液时,在靶浓度下测量稀释样品以测量抗粘度损失所证明的剪切降解量的粘度。结果表明,在流量控制装置中,在流量控制装置中发生聚合物溶液的粘度降解,并且与管道装置的压差直接相关。内部几何形状对降解量影响不大。速度对降解量影响不大。聚合物分子量和结构两者都会影响由于溶液浓度的剪切引起的降解量。通常,粘性盐水溶液将在流过初始粘度的15-50%范围内流过大于50psi差压的装置时失去粘度。在流量控制后,使用更多浓缩的聚合物流并稀释至靶浓度将减少粘度损失的量。基于实验室结果,设计和操作条件,可以对聚合物注射分配系统进行建议,以最大限度地减少流动的粘性盐水流的剪切劣化。

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