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Decomposition characteristics of natural gas hydrates in hydraulic lifting pipelines

机译:液压提升管道中天然气水合物的分解特性

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For the sake of guiding parameter setting of the hydraulic lifting pipeline system for cutter-suction mining of natural gas hydrates (“hydrates” for short) on the seabed, the decomposition characteristics of hydrates in hydraulic lifting pipelines and the effects of flow parameters on decomposition characteristics were studied in this paper. A temperature–pressure model for the hydrate hydraulic lifting pipeline, a hydrate decomposition mass transfer model and a pipeline multiphase flow model were established using mathematical modeling method according to thermodynamics and fluid mechanics. Then, the relationships of the temperature and pressure of pipeline fluid, the amount of hydrate particulate matter and the decomposition surface vs. the underwater depth under the effect of different influencing factors during the transformation from solid–liquid two-phase flow to solid–liquid–gas three-phase flow were analyzed. And the following research results were obtained. First, the decomposition of hydrate slows down and the decomposition surface moves upward slightly with the increase of flow rate in the pipeline. Second, particle size basically has no effects on the temperature and pressure of pipeline fluid, the hydrate phase equilibrium pressure and hydrate decomposition surface. However, only the hydrate particles whose diameter is smaller than 0.2?mm can be completely decomposed in the pipeline while the decomposition of those whose particles size is greater than 2.0?mm is negligible. Third, if the back pressure at the outlet is positive, the decomposition surface moves upward and the decomposition of hydrate slows down with the increase of the back pressure. And if the back pressure at the outlet is negative, the decomposition surface moves downward and the decomposition of hydrate speeds up with the increase of the back pressure. Fourth, the decomposition of hydrate slows down and the decomposition surface moves upward with the increase of mineral depth. However, the decomposition rate and decomposition surface are basically unchanged when the mineral depth is below 1500?m under water. Fifth, the experimental results are basically consistent with the numerical simulation results, and it is indicated that the newly established models are of high reliability. In conclusion, decomposition surface height and decomposition rate can be adjusted by controlling flow rate and outlet back pressure rationally during the cutter-suction mining of hydrates while the influences of particle diameter and mining depth on gas production need not be taken into consideration.
机译:为了指导海底天然气水合物(简称“水合物”)的刀吸开采液压起重管道系统的参数设置,液压起重管道中水合物的分解特性以及流量参数对分解的影响对本文的特点进行了研究。根据热力学和流体力学,采用数学建模方法,建立了水合物水力举升管道的温度压力模型,水合物分解传质模型和管道多相流模型。然后,在固液两相流向固液转化的过程中,在不同影响因素的作用下,管道流体的温度和压力,水合物颗粒物的数量和分解表面与水下深度的关系。 -气体三相流进行了分析。并获得了以下研究结果。首先,随着管道中流速的增加,水合物的分解变慢,分解表面略微向上移动。其次,粒径基本上对管道流体的温度和压力,水合物相平衡压力和水合物分解表面没有影响。但是,只有直径小于0.2?mm的水合物颗粒才能在管道中完全分解,而粒径大于2.0?mm的水合物颗粒的分解则可以忽略不计。第三,如果出口处的背压为正,则分解表面会向上移动,并且水合物的分解会随着背压的增加而减慢。并且,如果出口处的背压为负,则分解表面会向下移动,并且水合物的分解会随着背压的增加而加速。第四,随着矿物深度的增加,水合物的分解变慢,分解表面向上移动。但是,当水中的矿物深度低于1500μm时,分解速率和分解表面基本不变。第五,实验结果与数值模拟结果基本吻合,表明所建立的模型具有较高的可靠性。综上所述,在水合物的刀吸开采过程中,可通过合理控制流量和出口背压来调节分解表面的高度和分解速率,而不必考虑粒径和开采深度对产气量的影响。

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