稳定分层二层流非湍流/湍流层无平均剪切密度界面处的湍流

采用湍流统计理论、谱分析和快速畸变理论研究稳定分层二层流非湍流/湍流层无平均剪切密度界面处的湍流.分别在密度界面厚度（h）可忽略和很薄两种情况下,推导出任意理查森数（Ri）Ri→∞时,湍流层中水平、垂直方向速度的欧拉频谱和水平、垂直方向均方根速度的积分表达式.在h可忽略情况下：（1）任意Ri,Ri→∞时,密度界面对大尺度涡的影响显著,而对小尺度涡几乎无影响;距离密度界面越近,湍流层中水平方向均方根速度增大而垂直方向均方根速度减小;（2）任意Ri且在无量纲频率较大时,密度界面处、湍流层中水平、垂直方向速度的欧拉频谱满足-5/3幂次律,但是,它们不收敛于同一直线,表明密度界面处部分湍流转化为内波.在h很薄的情况下：（1）在水平方向上密度界面对湍流无显著的影响;湍流层中垂直方向速度的欧拉频谱出现过渡区,不满足-5/3幂次律,其幂次律增大,表明湍流过渡区的能量减少,但是,密度界面对线性小尺度涡仍几乎无影响;（2）距离密度界面越远,密度界面厚度对湍流的影响减弱并且偏向于线性中尺度涡;当远离密度界面时,过渡区消失,表明考虑密度界面厚度后密度界面对湍流的影响范围有限;（3）密度界面处垂直方向速度的欧拉频谱的幂次律减小,表明密度界面处线性内波的能量向线性低频区集中;（4）随着密度界面厚度增加,密度界面处垂直方向速度的欧拉频谱在整个线性内波频域里等幅度减小,湍流层中垂直方向速度的欧拉频谱只在线性低频区域减小且减小的幅度随着频率增大而减小;密度界面对湍流层中水平、垂直方向均方根速度影响的垂向范围随Ri增大而减小.     

特低渗透油藏面积井网见水时间计算

特低渗透油藏在水驱开发过程中常表现出渗透率各向异性和流体非达西渗流特征,运用非达西渗流公式及流线积分法,得到特低渗透油藏五点井网、反九点井网和菱形反九点井网在油水两相非活塞式驱替条件下的油井见水时间.计算长庆鄂尔多斯盆地某特低渗透油藏井网见水时间,结果与实际动态符合较好.分析油水黏度比、渗透率各向异性及启动压力梯度对油井见水时间的影响,结果表明：油水黏度比越大,油井的见水时间越早;当菱形反九点井网长轴方向井距与短轴方向井距之比与渗透率各向异性强度大致相等时,长轴方向与短轴方向上的角井能实现均衡驱替;启动压力梯度延缓了油井的见水时间,且生产井距越大,启动压力梯度的影响越显著.     

聚焦光在单轴晶体中的感应磁化

运用矢量衍射理论,分析了高度聚焦的圆偏振激光脉冲在具有逆法拉第效应的单轴晶体中产生的感应磁化分布.详细研究了界面位置不同对磁化分布的影响,比较了小双折射效应的单轴晶体中的磁化分布与均匀介质中的磁化分布.计算结果发现:随着界面向透镜移动,磁化强度的最大值和磁化斑的最小值位置沿着光轴方向移动.在单轴晶体中的磁化强度大于在均...     

套管井声场合成波形及其时频特征分析

数值计算了点声源激励下套管井声场的声压波形。计算模型包括了实际中所有的三类岩石及两个界面的各种胶结情况,声源频率采用实际的测井频率。对合成波形进行了基于Wigner－Ville分布的时频分析。计算和分析结果说明,波列中的套管波、伪瑞利波在一、二界面不同的胶结情况下有明显的变化规律。二界面未胶结时,套管波模式的时频分布随管外水泥层厚度的变化而变化。它们与地层体波成分的特征可作为管外水泥胶结质量评价的重要依据;而中速地层时地层体波能量最强,有利于胶结质量评价。     

第一性原理研究3C-SiC/Mg复合材料界面的电子结构

基于密度泛函理论的第一性原理平面波赝势方法对4种3C-SiC(111)/Mg(0001)界面模型进行研究.界面间距和粘附功的计算表明,结构优化之后的界面模型只在z轴方向发生了移动,界面间距发生了不同程度的缩短;中心型模型的稳定性强于顶位型模型,C终端结构的稳定性强于Si终端结构,中心型C终端的界面模型具有最大的粘附功(2.5834 J/m~2)和最小的界面间距(1.7193?),是4种模型中最稳定的结构. Mulliken电荷、电荷密度分布、差分电荷密度和态密度的计算表明,中心性结构的Si终端和C终端模型界面处存在共价键、离子键和金属键.     

深层高温高压气井临界产量计算模型

基于热膨胀效应和环空体积变化效应这两种环空带压机理,结合气井生产过程中井筒温度-压力分布计算方法,考虑油层套管和油管的许可压力值,建立一个深层高温高压气井临界产量计算模型.运用迭代法求解模型,编制相关程序.结果表明:环空压力与主要受温度的影响,气井产量越高,井口温度越高,环空压力越大,油套管安全系数越低,因此需要考虑管柱安全性确定临界流量.利用新疆某深层高温高压气井的实际数据进行实例计算,结果可为深层高温高压气井的合理配产提供依据.     

应力各向异性对铁磁/反铁磁双层薄膜磁性质的影响

 采用铁磁共振方法,研究了交换各向异性和应力各向异性对铁磁/反铁磁双层薄膜性质的影响。结果表明：界面交换作用导致单向各向异性,应力各向异性对材料的磁化难易程度有较大影响。在外磁场方向接近应力场方向时,共振频率向高值方向移动,其它区域共振频率则向低值方向移动。对频率线宽而言,接近应力场方向,频率线宽加宽,其它区域频率线宽则变窄。此外,当磁场变化时,应力的存在使得共振频率向低值方向移动,尤其在β＝π方向情况较为复杂,在弱场范围出现了两个区域：即在某磁场范围内,共振频率向高值方向移动,且频率线宽加宽;而其它范围的共振频率（线宽）是向高值方向移动（加宽）还是向低值方向移动（变窄）,取决于外磁场的相对强弱。     

应变纤锌矿ZnO/Mg_xZn_(1-x)O柱形量子点中离子受主束缚激子的光学性质

在有效质量近似下,考虑内建电场效应,采用变分法详细研究了受限于纤锌矿Mg_xZn_(1-x)O/ZnO/Mg_xZn_(1-x)O圆柱形应变量子点中离子受主束缚激子(A~-,X)的带间光跃迁吸收系数随量子点尺寸、Mg含量和离子受主杂质中心位置的变化情况,并和离子施主束缚激子(D~+,X)及自由激子进行了比较.结果表明:随着量子点尺寸的减小,(A~-,X)的光跃迁吸收强度增强,吸收曲线向高能方向移动,出现蓝移现象.随着Mg含量增加,(A~-,X)的光跃迁吸收曲线蓝移,且吸收强度减弱.随着离子受主杂质从量子点的左界面沿材料生长方向移至量子点的右界面,光跃迁吸收曲线向低能方向移动,出现红移现象.此外,与离子施主束缚激子(D~+,X)相比,随着沿材料生长方向掺入杂质位置的变化,光跃迁吸收曲线移动的方向相反.但不管是掺入离子受主杂质还是离子施主杂质,当离子杂质从量子点的左异质界面沿材料生长方向移至右异质界面时,光跃迁吸收峰的移动量大致相同.     

手征和运动介质界面异常光自旋霍尔效应

文章讨论了偏振高斯光束在空气-手征介质界面的反射和折射问题,发现了反射和折射光束的异常自旋霍尔效应.在某些特定的角度下,反射高斯光束重心的移动可以达到几十个波长的量级,通过调节手征参数,甚至会出现折射光重心移动方向由正到负的转变.文章还讨论了任意偏振高斯光束在空气-运动介质界面的反射和透射问题,当介质垂直于入射平面运动时,反射和透射光束的横向移动可以达到几个波长的量级,甚至在某些运动速度下可以实现移动方向正负的改变.这些研究对控制光的自旋霍尔效应提供了可能的途径.     

定时间步长变坐标步长差分求解单相Stefan问题

对单相Stefan问题提出了一种定时间步长、变坐标步长的差分求解方法.在固定时间步长内,以计算得到的移动界面位置作为网格节点的坐标,前后界面位置之差为空间步长,逐步地自动形成网格的划分,计算这些节点处的温度,从而获得下一时刻的移动界面的位置.     

古油层和残余油层的定量颗粒荧光响应

利用定量颗粒荧光(QGF和QGF-E)技术研究了古油层和残余油层的定量颗粒荧光响应。结果表明,古油层与现今油层具有很强的QGF荧光响应,利用QGF荧光响应识别出TZ421井存在100 m古油层,表明早期油气充注规模大,但后期发生泄漏,导致油水界面上升到现今的3 620 m。利用QGF-E荧光响应识别出60m残余油层,说明发生多期古油层泄漏,第一期泄漏使油水界面上升到残余油水界面(3 680 m),第二期泄漏发生在近期,形成现今油水界面。现今凝析气层中的强QGF荧光响应表明凝析气顶形成于最后一期天然气充注。     

凝析气相变微观孔隙模型实验研究

凝析油气体系相平衡是在储层多孔介质中进行,多孔介质中凝析油气相变是凝析气藏开发研究者关注的主题。应用二维刻蚀玻璃微观孔隙模型,通过可视化技术,对凝析气微观气液两相相变特征进行了研究,并对多孔介质吸附和毛细凝聚对凝析气相变的影响进行了分析。     

Study on Hydrate Production Behaviors by Depressurization Combined with Brine Injection in the Excess-Water Hydrate Reservoir

Depressurization combined with brine injection is a potential method for field production of natural gas hydrate, which can significantly improve production efficiency and avoid secondary formation of hydrate. In this work, the experiments of hydrate production using depressurization combined with brine injection from a simulated excess-water hydrate reservoir were performed, and the effects of NaCl concentration on hydrate decomposition, temperature change, and heat transfer in the reservoir were investigated. The experimental results indicate that there is little gas production during depressurization in a excess-water hydrate reservoir, and the gas dissociated from hydrate is trapped in pores of sediments. The high-water production reduces the final gas recovery, which is lower than 70% in the experiments. The increasing NaCl concentration only effectively promotes gas production rate in the early stage. The final cumulative gas production and average gas production rate have little difference in different experiments. The NaCl concentration of the produced water is significantly higher than that which is in contact with hydrate in the sediments because the water produced by hydrate decomposition exists on the surface of undissociated hydrate. The high concentration of NaCl in the produced water from the reactor significantly reduces the promoting effect and efficiency of NaCl solution on hydrate decomposition. The injection of NaCl solution decreases the lowest temperature in sediments during hydrate production, and increases the sensible heat and heat transfer from environment for hydrate decomposition. The changes of temperature and resistance effectively reflect the distribution of the injected NaCl solution in the hydrate reservoir.     

气力提升系统气液两相流数值模拟分析

污水处理、油田采油、液态金属冷却反应堆和磁流体动力转换器等领域采用气力提升系统有其显著优势.由于不同液体介质与气体介质密度对气力提升系统性能影响较大,因此本文基于Fluent仿真软件,采用欧拉模型、k-ω剪切应力输运湍流模型数值模拟了氮气-水、氮气-煤油、氮气-水银及空气-水、氩气-水、氮气-水下气力提升系统内气液两相流动行为,分析了系统稳定时提升立管内气相体积分数、提升液体流量、提升效率、提升管出口处液体径向速度的变化规律.研究结果表明:1)氮气-水、氮气-煤油、氮气-水银系统中,提升管内液体介质密度越大,提升管内气相体积分数越小、提升液体流量越大、提升效率越高;2)空气-水、氩气-水、氮气-水系统中,提升管内气体介质密度越大,提升管内气相体积分数越小、提升液体流量越大、提升效率峰值越小;3)提升管出口处提升液体径向速度随气体充入量的不断增加而整体波动升高,最终管轴中心附近液体速度较大,管壁附近液体速度较小.本文研究成果为污水处理、气举采油、液态重金属冷却核反应堆和磁流体动力转换器等应用领域的气力提升技术的优化提供科学的理论基础.     

一种新的凝析气藏气液相变实验方法研究

凝析油气体系和储层岩石是一个相互作用的系统,必然对孔隙介质中凝析气的相态特征产生影响。本文利用气 相色谱分析技术,建立了一种新的凝析气藏气液相变实验方法。实验研究表明:低渗透凝析气藏中孔隙介质对凝析气相态 有较大影响。因此,考虑孔隙介质对凝析气相态的影响对于高效经济开发低渗透凝析气藏具有指导意义。     

Investigation of Gas-Water-Sand Fluid Resistivity Property as Potential Application for Marine Gas Hydrate Production

The phase fraction measurement of gas-water-sand fluid in downhole is an important premise for safe and stable exploitation of natural gas hydrates, but the existing phase fraction measurement device for oil and natural gas exploitation can’t be directly applied to hydrate exploitation. In this work, the electrical resistivity properties of different gas-water-sand fluid were experimentally investigated using the multiphase flow loop and static solution experiments. The effect of gas phase fraction and gas bubbles distribution, sand fraction and sand particle size on the relative resistivity of the multiphase fluid were systematically studied. The measurement devices and operating parameters were also optimized. A novel combined resistivity method was developed, which demonstrated a good effect for the measurement of phase fractions of gas-water-sand fluid, and will have a good application potential in marine natural gas hydrates exploitation.     

New insights into the mechanisms of ultrasonic emulsification in the oil–water system and the role of gas bubbles

Ultrasonic emulsification (USE) assisted by cavitation is an effective method to produce emulsion droplets. However, the role of gas bubbles in the USE process still remains unclear. Hence, in the present paper, high-speed camera observations of bubble evolution and emulsion droplets formation in oil and water were used to capture in real-time the emulsification process, while experiments with different gas concentrations were carried out to investigate the effect of gas bubbles on droplet size. The results show that at the interface of oil and water, gas bubbles with a radius larger than the resonance radius collapse and sink into the water phase, inducing (oil–water) blended liquid jets across bubbles to generate oil-in-water-in-oil (O/W/O) and water-in-oil (W/O) droplets in the oil phase and oil-in-water (O/W) droplets in the water phase, respectively. Gas bubbles with a radius smaller than the resonance radius at the interface always move towards the oil phase, accompanied with the generation of water droplets in the oil phase. In the oil phase, gas bubbles, which can attract bubbles nearby the interface, migrate to the interface of oil and water due to acoustic streaming, and generate numerous droplets. As for the gas bubbles in the water phase, those can break neighboring droplets into numerous finer ones during bubble oscillation. With the increase in gas content, more bubbles undergo chaotic oscillation, leading to smaller and more stable emulsion droplets, which explains the beneficial role of gas bubbles in USE. Violently oscillating microbubbles are, therefore, found to be the governing cavitation regime for emulsification process. These results provide new insights to the mechanisms of gas bubbles in oil–water emulsions, which may be useful towards the optimization of USE process in industry.     

剪切应变下刃型位错的滑移机理的晶体相场模拟

针对刃型位错的滑移运动, 构建包含外力场与晶格原子密度耦合作用的体系自由能密度函数, 建立剪切应变作用体系的晶体相场模型. 模拟了双相双晶体系的位错攀移和滑移运动, 计算了位错滑移的Peierls势垒和滑移速度. 结果表明: 施加较大的剪切应变率作用, 体系能量变化为单调光滑曲线, 位错以恒定速度做连续运动, 具有刚性运动特征; 剪切应变率较小时, 体系能量变化出现周期波动特征, 位错运动是处于低速不连续运动状态, 运动出现周期“颠簸”式滑移运动, 具有黏滞运动特征; 位错启动运动, 存在临界的势垒. 位错启动攀移运动的Peierls势垒要比启动滑移Peierls势垒大几倍. 位错攀移和滑移运动特征与实验结果相符合.     

裂缝-孔隙型双重介质油藏渗吸机理的分形分析

低渗透油藏常常伴随裂缝发育,形成裂缝-基质双重介质.自发渗吸是低渗裂缝性水驱油藏的重要采油机理,有顺向和逆向两种渗吸方式.基于基质孔隙结构的分形特征,引入分形几何对裂缝性双重介质渗吸机理的判据进行了改进,建立了渗吸机理的分形判据模型,并进一步推导了结构常数的解析表达式.结果表明,渗吸机理的判别参数是基质孔隙度、高度、孔隙分形维数、流动迂曲度、最大孔隙直径、界面张力、油水密度差以及接触角的函数.改进后的判据模型与现有结果一致.最后绘制了判别渗吸机理的图版,为利用表面活性剂提高低渗透油藏采收率提供理论依据.     

The effect of astigmatism on the phase singularities of focused beams

The phase singularities of plane beams focused by an aperture lens with astigmatism are studied. Numerical calculation results are given to illustrate the dependence of phase singularities of focused plane beams on the astigmatic coefficient and the Fresnel number. It is shown that as the Fresnel number gradually increases, the phase singularities shift not only towards the z-axis but also towards the geometrical focal plane in the presence of astigmatism, whereas the phase singularities move along the focal plane and always line in the focal plane for the astigmatism-free case. With increasing astigmatic coefficient, the phase singularities shift not only towards the z-axis but also far away from the geometrical focal plane.