稠油掺稀多相流动规律及生产参数设计

研究了塔河超深稠油掺稀井多相流动规律。根据不同的掺稀方式给出了超深井稠油掺稀井井筒中流体温度梯度的计算方法。结合掺稀特点,给出了超深井稠油原油物性模拟的修正模型,其结果与PVT曲线具有良好的相关性。通过引入井眼轨迹的描述与计算技术,解决了超深井弯曲井段的多相流计算问题。在此基础上,根据能量平衡及多相流体力学原理建立了稠油掺稀生产动态分析模型,实现了对超深井稠油掺稀生产动态的模拟和分析,并据此可对稠油掺稀比例及生产参数进行优化设计,现场应用收到了良好的效果。     

在封闭地层中非牛顿幂律流体压降特征分析

研究非牛顿流体压降特征有助于提高聚合物驱油或常规稠油开采效果.本文首先用Laplace变换方法给出了封闭地层中非牛顿幂律流体不稳定渗流数学模型的解析解式,然后通过渐近分析给出了比较完整的压降流动期表现公式,其中晚期拟稳态表达式是一个新的结果,而通过流动期渐近公式可以对非牛顿幂律流体压降测试数据进行简洁分析,文中给出了具体应用方法和步骤.     

The viscoelastic effects on thermal convection of an Oldroyd-B fluid in open-top porous media

The effects of two viscoelastic parameters on the thermal convection of a viscoelastic Oldroyd-B fluid in an open-top porous square box with constant heat flux are investigated. The results show that the increase of relaxation time is able to destabilize the fluid flow leading to a higher heat transfer rate, while the increase of retardation time tends to stabilize the flow and suppress the heat transfer. The flow bifurcation appears earlier with the increase of the relaxation time and the decrease of the retardation time, resulting in more complicated flow patterns in the porous medium.     

煤层气井井筒煤粉运移规律研究

煤层气井排采过程中由于储层析出煤粉,现场经常遇到煤粉沉降堵塞井筒及煤粉卡泵问题,急需针对井筒内煤粉运移的分析预测方法。该研究建立了井筒内垂向和径向煤粉运移数学模型及求解方法,在此基础上分析了煤层气井井筒流体煤粉携出能力及煤粉径向浓度分布规律。研究结果表明,排水速度越快井筒流体携出煤粉能力越强,对于直径200μm以内的煤粉,排水速度超过3 m3/d (3.48×10^-5m³/s)便可将煤粉全部携出。煤粉呈现向井筒中线聚集现象,距离井筒中线越近煤粉浓度越高,并且排水速度越快煤粉聚集现象越显著,当排水速度达到5 m3/d(5.79×10^-5m³/s)时井筒中线煤粉浓度是壁面附近的10倍。相同排水速度下,颗粒粒径增大会使得煤粉在井筒中线附近浓度略微降低。     

稠油输送新工艺方法探索及现场试验

本文介绍一种可应用于高粘度稠油管输的新工艺。即用自行研制的蒸汽引射器采用无界引射方式，将蒸汽直接注入到输油管道中，利用蒸汽释放的热量提高稠油温度降低粘度，从而达到降低稠油输送压降的目的，它比间接加热输送工艺所用的蒸汽量或耗煤量大大减少。本方法在辽河油田输油管线上进行了工业现场试验，取得了很好的效果。     

Numerical simulation of thermal convection of viscoelastic fluids in an open-top porous medium with constant heat flux

This paper makes a numerical study of the buoyancy-driven convection of a viscoelastic fluid saturated in an open-top porous square box under the constant heat flux boundary condition. The effects of the relaxation and retardation times on the onset of the oscillatory convection, the convection heat transfer rate and the flow pattern transition are investigated. It is shown that a large relaxation time can destabilize the fluid flow leading to an early onset of the thermal convection and a high heat transfer rate, while a large retardation time tends to stabilize the flow and suppress the convection onset and the heat transfer. After the convection sets in, the flow bifurcation appears earlier with the increase of the relaxation time and the decrease of the retardation time, resulting in more complicated flow patterns in the porous medium. Furthermore, with the increase of the ratio of the relaxation time to the retardation time, the fluid may be blocked from flowing through the open-top boundary, which may be caused by the viscoelastic effect. Finally, the comparison of our results with those under isothermal heating boundary conditions reveals that the heat transfer rate corresponding to a constant heat flux boundary is always higher.