不同高黏度减阻剂对支撑剂输运效果的分析

C. Aften
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引用次数: 10

摘要

摩擦减速器(FRs)用于降低水力压裂液在固定流速下通过地层所需的马力。虽然在滑溜水作业中,在射孔前使用FR粘度并不是支撑剂输送的关键考虑因素,但在支撑剂从射孔输送到地层时,FR粘度成为了一个更重要的考虑因素,随着高粘度减阻剂(HVFR)系统的出现,FR粘度成为了一个重要的确定标准,HVFR系统比传统的FR需要更高的载荷。例如温度、水化方法、聚合物浓度、卤水组成和添加剂的相互作用。开展并实施了一项研究,以确定浓缩颗粒和颗粒沉降对HVFR的影响。本研究采用响应面法,应用8个变量对5个hvrs的黏度进行了研究。最初的研究标准是通过独特的装置设计和粘度测量验证建立一致的水化作用。一旦建立,该方法检查了1:1,2:1和2:2盐的影响,单独或在不同浓度和组合。淡水条件下的实验设计也进行了不同的HVFR负荷(1.0至6.0gpt),搅拌器转速(600至12,000)和搅拌器搅拌时间(0.5至8.7分钟)。粘度测量范围为200 ~ 6000(1/秒)。在0 ~ 140,000总溶解固体(TDS)盐水中进行了0.87 ~ 3.50磅/加仑的静态沉降测试。在淡水和API盐水中进行了单头沉降测量。特定的HVFR和盐基质组合测试导致高度相关的响应面表现出一致的趋势。根据测试的具体HVFR, TDS和硬度对粘度有小到大的影响。在粘度方面,卤水主要具有拮抗作用,协同作用很少。HVFR用量和混合的影响与所有HVFR的粘度高度相关,延长混合时间对某些HVFR组合没有影响,表明粘度降低极限。在设计空间的某些区域,沉降速率与粘度有关。选择针对特定卤水成分精确定制的HVFR系统,确保最大限度地减少摩擦和支撑剂运输性能至关重要。泵送和管状输送对HVFR粘度的影响是连续的、可量化的。此外,HVFR在井下盐水环境中的粘度为评估远端井眼支撑剂运移和潜在损害提供了可识别的数据。本研究建立了一种可靠的方法来测量HVFR系统的性能和检查可测量的场变量。
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Analysis of Various High Viscosity Friction Reducers and Brine Ranges Effectiveness on Proppant Transport
Friction reducers (FRs) are used to decrease the amount of horsepower required to move a hydraulic fracturing fluid through a formation at a fixed flow rate. Though FR viscosity is not a crucial consideration in proppant transport when used before the perforations in slick water applications, FR viscosity becomes a greater consideration in proppant transport from the perforations into the formation and an important qualifying criterion with the advent of High Viscosity Friction Reducer (HVFR) systems that require higher loadings than traditional FRs. Consistent viscosity measurement can vary greatly depending upon a number of factors, for example temperature, hydration approach, polymer concentration, brine composition, and additive interaction. A study was developed and implemented to determine the influence of HVFR by concentrated particulate and bead settling. This study investigated the viscosities of five HVFRs applying eight variables using response surface methodology. Initial study criteria were establishing consistent hydration with unique apparatus design and viscosity measurement verification. Once established, this method examined the effects of 1:1, 2:1, and 2:2 salts, singularly or in various concentrations and combinations. Experimental designs under fresh water conditions were also conducted with varied HVFR loadings (1.0 to 6.0gpt), blender RPM (600 to 12,000), and blender mixing times (0.5 to 8.7 minutes). Viscosities were measured from 200 to 6000 (1/sec). Static settlement testing in ranges of 0.87 to 3.50 pounds per gallon in 0 to 140,000 total dissolved solids (TDS) brines was conducted. Single bead settling measurements were performed in fresh water and API brine. Specific HVFR and salt matrix combinations tested resulted in highly correlated response surfaces exhibiting consistent trends. The TDS and hardness had a minor to major influence on viscosity based upon the specific HVFR examined. Brines were predominately antagonistic with respect to viscosity with few synergistic results. The influences of HVFR dosage and mixing correlated highly to the viscosity of all HVFRs, and extended mixing time durations had no influence on some HVFR combinations indicating a viscosity reduction limit. In certain regions of the design space, settling rates were related to viscosity. Selection of an HVFR system precisely tailored for a specific brine composition guaranteeing maximum friction reduction and proppant transportation performance was vital. The influence of pumping and tubular transport on the HVFR viscosity is continuous and quantifiable. Additionally, the viscosity of the HVFR in a downhole brine environment provides discernable data for assessing far end well bore proppant transport and damage potential. This study established a reliable method for gauging performance and examining measurable field variables of HVFR systems.
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