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METHOD OF THE PIPELINE CHARACTERISTICS DETERMINATION (VARIANTS) AND COMPLEX FOR ITS IMPLEMENTATION AND PIPELINE DAMAGE DETECTION

机译:管道特性测定(变量)及其实现和管道损伤检测的方法

摘要

The complex contains two pairs of sensor 2 pressure in the pipeline 1, installed in pairs at a distance of 50-200 meters between neighboring sensors 2 in each pair, the local programmable logic controllers, 3 sensors timestamp in the form of GPS receivers 4, line 5 context, the central controller 6 and workstation operator 7 (PC 7). The sensors 2 are satisfied with the response time of less than 1 ms (milliseconds). A pair of sensors 2 are located on the borders of the control section of the pipeline I5 the distance between two pairs of sensors, i.e., length control region is 5000 - 50 000 m. Thus, the sensor 2 is installed at a distance between them at each end of the control region of between 0,001 to 0.04 the length of this section of the pipeline 1. One of the two sensors in each pair is internal to the control site, while another - the outside. Ratio of distances between sensors 2 in each pair and the length of the chosen from the condition of minimal influence of hydraulic losses along the length of the site on testing results. The technical result of the invention group combined with the unique invention idea lies in extension of the functional possibilities, increase of the technological effectiveness, simplification of the design, increase of accuracy, reliability and operation speed at the account of the efficient and online control of the wave parameters at the stage of its occurrence, control of the fluid medium parameters on a real-time basis, and leakage detection at the stage of its occurrence on a real-time basis.
机译:该综合体在管道1中包含两对压力传感器2,成对安装在每对中相邻传感器2之间的距离为50-200米,本地可编程逻辑控制器,3个以GPS接收器形式的传感器时间戳4,在第5行上下文中,中央控制器6和工作站操作员7(PC 7)。传感器2的响应时间小于1ms(毫秒)。一对传感器2位于管道15的控制部分的边界上,两对传感器之间的距离即长度控制区域为5000-50000m。因此,传感器2被安装在控制区域的每一端之间的距离处,该距离在管道1的该部分的长度的0.001至0.04之间。每对中的两个传感器之一在控制位置内部,而另一个-外面。每对传感器2之间的距离与长度的比值是从沿着站点的长度方向对水力损失影响最小的条件对测试结果进行选择的。发明组的技术成果与独特的发明思想相结合,在于功能的扩展,技术效力的提高,设计的简化,准确性和可靠性以及运行速度的提高,这要归功于高效的在线控制。发生阶段的波动参数,实时控制流体介质参数以及实时发生波动的泄漏检测。

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