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Experimental Study and Modeling of Sand Erosion in the Gas-Liquid Cylindrical Cyclone GLCC Separators

机译:煤气圆柱旋风旋风直升机砂腐蚀的实验研究与建模

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Gas-Liquid Cylindrical Cyclone (GLCC) separators have been widely accepted as an alternative to conventional vessel-type separator during recent years. The operators are using GLCCs at flow rates higher than the normal recommended operational envelope in applications where the increased liquid carry-over and gas carry-under can be tolerated. Experience gained from production of hydrocarbons with entrained sand has shown that severe degradation of production equipment may occur due to solid particle erosion at high productions rates. However, there are no data and no field feedback on erosion in the inlet region of a GLCC. Thus, the goal of this work is to evaluate the erosion condition in the Gas-Liquid Cylindrical Cyclone (GLCC) separator under gas production and low-liquid loading flow condition. Erosion experiments are conducted with gas-sand and gas-liquid-sand flow conditions in a laboratory scale GLCC with two particle sizes and gas velocities. An ultrasonic thickness measurement system is employed to monitor the erosion rates at the inlet region of the GLCC. Several cases are simulated with commercially available Computational Fluid Dynamics (CFD) software. Based on the experimental data and CFD simulations, a mechanistic one-dimensional model is proposed to calculate maximum thickness loss inside the GLCC. It is observed that the location of maximum erosion is not varying significantly with the flow condition with or without the presence of liquid and particle size, while the liquid entrainment can reduce the value of maximum erosion (in mm/kg) by one order of magnitude. The erosion increases with the flow velocity as expected but not with particle size for the particles used in current experiments. CFD simulation results that are obtained by utilizing the mechanistic erosion equations provided fair agreement with experimental measurements for gas-sand condition, and the simplified model showed consistency with the data in both gas-sand and gas-liquid-sand flow conditions.
机译:近年来,燃气液圆柱形旋风分离器(GLCC)隔膜被广泛接受作为常规血管型分离器的替代品。操作员正在使用GLCC,其流速高于普通推荐的操作包络在增加的液体携带和气体携带的应用中的正常推荐的操作包络。由夹带砂的生产中烃生产的经验表明,由于高效率的固体颗粒腐蚀,可能发生生产设备的严重降解。但是,在GLCC的入口区域中没有数据和没有现场反馈。因此,这项工作的目的是在气体生产和低液体加载流动条件下评估气液圆柱形旋风分离器(GLCC)分离器中的腐蚀条件。侵蚀实验用具有两个粒度和气体速度的实验室测量GLCC中的气囊和气体砂流动条件进行。采用超声厚度测量系统监测GLCC的入口区域的侵蚀速率。用市售的计算流体动力学(CFD)软件模拟几种情况。基于实验数据和CFD仿真,提出了一种机械一维模型来计算GLCC内的最大厚度损耗。观察到最大侵蚀的位置与具有液体和粒度的存在或不存在的流动条件没有显着变化,而液体夹带可以减少最大腐蚀(以mm / kg)的一个级别。侵蚀随着预期的流速而增加,但不具有当前实验中使用的颗粒的粒度。通过利用机械侵蚀方程获得的CFD仿真结果提供了与天然气 - 砂条件的实验测量进行公平的一致性,简化模型显示了与气砂和气液砂流动条件中的数据的一致性。

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