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Modelling of Bitumen-and-Solvent-Mixture Viscosity Data Using Thermodynamic Perturbation Theory 用热力学摄动理论模拟沥青-溶剂混合物粘度数据
Pub Date : 2014-01-01 DOI: 10.2118/157930-PA
Mohsen Zirrahi, H. Hassanzadeh, J. Abedi
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引用次数: 7
Rescaled Exponential and Density-Based Decline Models: Extension toVariable Rate/Pressure-Drawdown Conditions 缩放指数和基于密度的下降模型:扩展到可变速率/压降条件
Pub Date : 2013-11-01 DOI: 10.2118/168223-PA
L. Ayala, Miao Zhang
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引用次数: 12
Effect of Completion Heterogeneity in a Horizontal Well With Multiple Fractures on the Long-Term Forecast in Shale-Gas Reservoirs 多裂缝水平井完井非均质性对页岩气藏长期预测的影响
Pub Date : 2013-11-01 DOI: 10.2118/149400-PA
M. Nobakht, R. Ambrose, C. Clarkson, J. E. Youngblood, R. Adams
Shale gas reservoirs have become a significant source of gas supply in North America because of the advancement of drilling and stimulation techniques enabling commercial development. The most popular method for exploiting shale gas reservoirs today is the use of long horizontal wells completed with multiple-fracturing stages [multifractured horizontal wells (MFHW)]. The stimulation process may result in biwing fractures or a complex hydraulic-fracture network. However, there is no method to differentiate between these two scenarios with production data analysis alone, making accurate forecasting difficult. For simplicity, hydraulic fractures are often considered biwing when analyzing production data. A conceptual model that is often used for analyzing MFHWs is that of a homogeneous completion in which all fractures have the same length. However, fractures of equal length are rarely if ever observed (Ambrose et al. 2011). In this paper, production data from heterogeneous MFHWs (i.e., where all fracture lengths are not the same) is studied for reservoirs with extremely low permeability. First, the simplified forecasting method of Nobakht et al. (2012), developed for homogeneous completions, is extended to heterogeneous completions. For one specific case, the Arps' decline exponent is correlated to the heterogeneity of the completion. It is found that, as expected, Arps' decline exponent (used after the end of linear flow) increases with the heterogeneity of the completion. Finally, it is shown that ignoring the heterogeneity of the completion can have a material effect on the long-term forecast. We have assumed planar hydraulic-fracture geometries for our modelling in this work and discuss the implications of this when more-complex fracture geometries are created. This seems to be more common in shale gas reservoirs. We provide an example of low-complexity, planar fracture geometries created near an MFHW and observed on an image log at an offset well.
由于钻井和增产技术的进步,页岩气藏已成为北美地区重要的天然气供应来源。目前,开发页岩气藏最流行的方法是使用多级压裂的长水平井(MFHW)。增产过程可能会形成斜缝或复杂的水力裂缝网络。然而,没有办法单独通过生产数据分析来区分这两种情况,这使得准确预测变得困难。为了简单起见,在分析生产数据时,水力裂缝通常被认为是弯曲的。通常用于分析MFHWs的概念模型是均匀完井,其中所有裂缝都具有相同的长度。然而,相等长度的骨折很少被观察到(Ambrose et al. 2011)。本文研究了非均质MFHWs(即所有裂缝长度不相同)的极低渗透率储层的生产数据。首先,将Nobakht等人(2012)为均匀完井开发的简化预测方法推广到非均匀完井。在一个特定的情况下,Arps的下降指数与完井的异质性有关。研究发现,正如预期的那样,Arps的下降指数(线性流动结束后使用的指数)随着完井的非均质性而增加。最后,研究表明,忽略完井的异质性会对长期预测产生重大影响。在这项工作中,我们假设了平面水力裂缝的几何形状,并讨论了在创建更复杂的裂缝几何形状时的意义。这似乎在页岩气藏中更为常见。我们提供了在MFHW附近创建的低复杂性平面裂缝几何形状的示例,并在邻井的图像测井中进行了观察。
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引用次数: 24
Short-Term Testing Method for Stimulated Wells--Field Examples 模拟井短期测试方法——现场实例
Pub Date : 2013-11-01 DOI: 10.2118/168219-PA
I. Kutasov
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引用次数: 0
Impact Map for Assessment of New Delineation-Well Locations 评估新圈定井位的影响图
Pub Date : 2013-11-01 DOI: 10.2118/168222-PA
Yevgeniy Zagayevskiy, C. Deutsch
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引用次数: 1
Effect of Temperature on VAPEX Performance 温度对VAPEX性能的影响
Pub Date : 2013-11-01 DOI: 10.2118/157799-PA
P. Haghighat, B. Maini
Incorporating some heat injection along with solvent injection appears to be the most viable option for improving the oil-drainage rate of vapour-assisted petroleum extraction (VAPEX) in extraheavy-oil formations. This study was intended to quantify the maximum possible increase in VAPEX drainage rate that can be obtained by heating the formation to a target temperature. The experimental phase of this study involved conducting VAPEX experiments in a large high-pressure physical model, packed with 250-darcy sand, using propane as the solvent. The physical model was preheated to 40, 50 and 60 C, and propane was injected at the same test temperature but different injection pressures to observe how injection pressure affects oil-drainage rate at elevated temperatures. In the experiments at elevated temperatures, but without increasing the injection pressure, higher rate of oil production was achieved in the early stages of the process. However, a stabilized rate of oil production did not show pronounced improvement caused by a lower solubility of propane in the oil at higher temperatures. Increasing injection pressure along with increasing the test temperatures was successful in accelerating the oil production. The oil used in these experiments was found to become mobile with the increase in temperature even without solvent dissolution. As a result, the total rate of oil production appeared to be controlled by two mechanisms: (1) by solvent dissolution and oil mobilization at the boundaries of the vapour chamber and (2) by pure free-fall gravity drainage beyond the vapour chamber wherever gravity head was sufficient to push the mobile oil toward the production well. The results of this these tests define the upper limit of oil rates achievable with heated solvent injection. They can also be used to assess the applicability of VAPEX to warm reservoirs naturally (e.g., in Venezuela) and reservoirs with mobile oil in place.
在注入溶剂的同时加入一些热注入似乎是提高超稠油地层蒸汽辅助石油开采(VAPEX)排油速率的最可行选择。该研究旨在量化通过将地层加热到目标温度可以获得的VAPEX泄油速率的最大可能增加。本研究的实验阶段包括在一个大型高压物理模型中进行VAPEX实验,该模型中填充了250达西的砂,使用丙烷作为溶剂。将物理模型预热至40、50、60℃,在相同的测试温度、不同的注入压力下注入丙烷,观察在高温下注入压力对排油速率的影响。在实验中,在不增加注入压力的情况下,在该过程的早期阶段获得了更高的产油量。然而,在较高温度下,丙烷在油中的溶解度降低并没有显著改善稳定的产油量。随着测试温度的升高,注入压力的增加成功地加速了原油的开采。在这些实验中使用的油,即使没有溶剂溶解,也会随着温度的升高而变得流动。因此,总产油量似乎受到两种机制的控制:(1)蒸汽室边界的溶剂溶解和油的动员;(2)蒸汽室以外的纯自由落体重力排水,只要重力头足以将可移动的油推向生产井。这些测试的结果确定了热溶剂注入可达到的油率上限。它们还可用于评估VAPEX在自然加热储层(例如委内瑞拉)和具有流动油的储层中的适用性。
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引用次数: 13
Viscosity Prediction for Solvent-Diluted Live Bitumen and Heavy Oil at Temperatures Up to 175-deg-C 粘度预测溶剂稀释活沥青和重油在温度高达175℃
Pub Date : 2013-09-01 DOI: 10.2118/149405-PA
H. Motahhari, F. Schoeggl, M. Satyro, H. Yarranton
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引用次数: 14
Subcool, Fluid Productivity, and Liquid Level Above a SAGD Producer 过冷、流体生产力和SAGD生产者以上的液位
Pub Date : 2013-09-01 DOI: 10.2118/157899-PA
J. Yuan, Daniel Nugent
Thermodynamic steam-trap control, or subcool control, in a typical steam-assisted gravity-drainage (SAGD) production is essential to the stability and longevity of the operation. It is achieved commonly through the control of fluid production. The goal of such control is to maintain a steady and healthy liquid production without allowing steam from the injector to bypass to the producer. Therefore, it is effectively a control of the liquid level above the producer. Unfortunately, it is not practical to monitor this liquid level. A rule-of-thumb subcool-per-metre estimation of 10°C/m of liquid level is popular in the industry; however it does not prove to hold in many situations. This paper presents a study of the dynamics of SAGD-production control with a resulting algebraic equation that relates subcool, fluid productivity, and wellbore drawdown to the liquid level above a producer. The main conclusions of this study include • There is no minimum subcool value for a pure-gravity-drainage scenario; however, as the wellbore drawdown is considered, there is a minimum subcool value in order to maintain the stability of fluid flow. • For a given productivity, the liquid level increases as subcool increases or as wellbore drawdown decreases. • For each given set of operating parameters, there exists a critical productivity below which SAGD operation would halt. • Before the steam chamber reaches the top of the reservoir, the fluid productivity is limited by the vertical distance between the injector and the producer; the larger the distance, the higher the fluid-production rate can be. A verification of this analysis was conducted by a series of numerical reservoir simulations. Although limited to two dimensions, we expect that this analysis captures the main physics amid the dynamic complexity of SAGD-production control. The resulting algebraic equation can be used for better understanding of the dynamics of subcool control and for determining operation strategies.
在典型的蒸汽辅助重力排水(SAGD)生产中,热力蒸汽疏水阀控制或过冷控制对作业的稳定性和寿命至关重要。通常通过控制流体产量来实现。这种控制的目标是保持稳定和健康的产液,而不允许蒸汽从注入器旁路到生产者。因此,它有效地控制了生产者以上的液位。不幸的是,监测这个液位是不实际的。10°C/m的液位的每米过冷度估计的经验法则在工业中很流行;然而,它在许多情况下并不成立。本文对sagd生产控制动力学进行了研究,并得出了一个代数方程,该方程将过冷度、流体产能和井筒降与生产商上方的液位联系起来。本研究的主要结论包括:•在纯重力排水的情况下,没有最小过冷值;然而,考虑到井筒压降,为了保持流体流动的稳定性,存在一个最小过冷值。对于给定的产能,随着过冷度的增加或井筒压降的减小,液面会增加。•对于每一组给定的作业参数,存在一个临界产能,低于该产能,SAGD作业将停止。在蒸汽室到达储层顶部之前,流体产能受到注入器和采油器之间垂直距离的限制;距离越大,产液率越高。通过一系列油藏数值模拟验证了这一分析。虽然限于两个维度,但我们希望该分析能够捕捉sagd生产控制动态复杂性中的主要物理特性。所得到的代数方程可用于更好地理解过冷控制动力学和确定操作策略。
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引用次数: 18
Stability of In-Situ-Combustion Process to Stoppage of Air Injection 就地燃烧过程对停止喷射空气的稳定性
Pub Date : 2013-09-01 DOI: 10.2118/158258-PA
A. Turta
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引用次数: 2
Field Results for Recovering Oil From a Steam-Project Pressure-Isolation Wall 蒸汽工程隔压墙采油的现场效果
Pub Date : 2013-09-01 DOI: 10.2118/158262-PA
K. A. Miller, Yi Xiao
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引用次数: 1
期刊
Journal of Canadian Petroleum Technology
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