Rao Yongchao, Wang Yunxiao, Wang Shuli, Gong Zijia, Zhang Chenglong
Jiangsu Key Laboratory of Oil-Gas Storage and Transportation Technology, Changzhou University, Changzhou, 213164, Jiangsu, China.
School of Petroleum and Nature Gas Engineering, School of Energy, Changzhou University, Changzhou, 213164, China.
Sci Rep. 2024 Dec 30;14(1):31604. doi: 10.1038/s41598-024-77890-w.
Bend pipe is a common part of long distance pipeline. There is very important to study the flow law of hydrate particles in the bend pipe, and pipeline design will be optimized. In addition, the efficiency and safety of pipeline gas transmission will be improved. With the flow of hydrate particles in a curved pipe as the object of study, the effects of Bend diameter rate and Reynolds number on the velocity distribution, turbulent kinetic energy change, wall shear force, particle motion and pressure drop distribution of the spiral flow carrying hydrate particles were investigated by numerical simulation method. The results show that bend diameter rate is the smaller, and the high speed zone is easier to appear inside the bend. Moreover, the uniformity of the velocity distribution of the fluid flowing through the bend is slower with the smaller the rate of the bend to the diameter. When Re = 20,000, the curve fluctuates more, and the peak speed reaches 4 times that of Re = 10,000. Increasing the Reynolds number of the initial transport can maintain the helical flow strength of the fluid after passing through the bend pipe, so that the flow can obtain higher tangential force. Because the fluid flows into the pipe by spiral flow, the shear force inside the pipe is higher under the combined action of its tangential velocity at the pipe wall and the high speed zone inside the pipe wall. The presence of the twisted tape leads to greater flow resistance, which makes the pressure drop increase at the position of the twisted tape different. At the same position, the Reynolds number is larger, and the pressure drop increases larger, and the Bend diameter rate is larger, and the fluid speed recovers faster, and the velocity is smaller, and the unit pressure drop is smaller, and Unit pressure drop is down 72.9%. The increase of Reynolds number can reduce the resistance coefficient of the Bend part, but the increase of the Bend diameter rate makes the resistance coefficient decrease first and then increase.
弯管是长距离管道的常见部件。研究水合物颗粒在弯管中的流动规律对于优化管道设计非常重要,此外,还能提高管道气体输送的效率和安全性。以水合物颗粒在弯管中的流动为研究对象,采用数值模拟方法研究了弯径比和雷诺数对携带水合物颗粒的螺旋流速度分布、湍动能变化、壁面剪切力、颗粒运动及压降分布的影响。结果表明,弯径比越小,弯管内越易出现高速区,且弯径比越小,流经弯管的流体速度分布均匀性越差。当Re = 20000时,曲线波动更大,峰值速度达到Re = 10000时的4倍。增大初始输送的雷诺数可维持流体通过弯管后的螺旋流强度,使流体获得更高的切向力。由于流体以螺旋流形式流入管道,在管壁切向速度和管内壁高速区的共同作用下,管内剪切力较高。扭带的存在导致流动阻力增大,使得扭带位置处的压降增大,在相同位置,雷诺数越大,压降增大越大,弯径比越大,流体速度恢复越快,速度越小,单位压降越小,单位压降下降72.9%。雷诺数的增加可降低弯管部分的阻力系数,但弯径比的增大使阻力系数先减小后增大。