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Effect of Impurities on Depressurization of CO2 Pipeline Transport

机译:杂质对CO2管道输送减压的影响

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The objective of the present study is to gain an understanding on the effect of impurities during the depressurization of CO2 pipeline transport. In this study, experimental apparatus was built to simulate the transient behavior of CO2 pipeline transportation. The transient blowdown test was conducted at the initial conditions of 85 bar and 20 °C. To study the effect of impurities, N2 was added from 2% to 8% on mass fraction basis. The blowdown of CO2 pipeline transport system was numerically simulated. The dynamic multiphase flow simulator OLGA was used to model the depressurization of CO2 pipeline system. Comparisons of experimental data and numerical simulation results were carried out. Initial severe pressure drops during few seconds were well estimated by numerical simulation for both pure and mixture cases. On the other hand, the numerical simulation did not provide reliable temperature drop predictions. As the amount of N2 impurity increases the numerical simulation results showed better pressure drop predictions. But there were some difference between experimental data and numerical simulation results in gradual pressure drops as the amount of N2 impurity decreases. In conclusion, it is required to improve the phase change model of numerical simulator.
机译:本研究的目的是了解杂质在二氧化碳排水管道输送过程中杂质的影响。在该研究中,建立了实验装置以模拟CO2管道运输的瞬态行为。瞬时排污测试在85巴和20℃的初始条件下进行。为了研究杂质的作用,基于质量分数加入2%至8%。数值模拟CO2管道传输系统的排污。动态多相流动模拟器OLGA用于模拟CO2管道系统的减压。进行了实验数据和数值模拟结果的比较。在纯和混合案例的数值模拟中,初始严重的压降估计很少。另一方面,数值模拟没有提供可靠的温度降低预测。随着N2杂质的量增加,数值模拟结果显示出更好的压降预测。但是,实验数据与数值模拟之间存在一些差异导致逐渐压降随着N2杂质量的逐渐降低。总之,需要改善数值模拟器的相变模型。

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