李长俊,董森,贾文龙,等. 气主导体系下CO2水合物生长动力学试验[J]. 油气储运,2025,x(x):1−10.
引用本文: 李长俊,董森,贾文龙,等. 气主导体系下CO2水合物生长动力学试验[J]. 油气储运,2025,x(x):1−10.
LI Changjun, DONG Sen, JIA Wenlong, et al. Investigation of CO2 hydrate growth kinetics in gas-dominated systems[J]. Oil & Gas Storage and Transportation, 2025, x(x): 1−10.
Citation: LI Changjun, DONG Sen, JIA Wenlong, et al. Investigation of CO2 hydrate growth kinetics in gas-dominated systems[J]. Oil & Gas Storage and Transportation, 2025, x(x): 1−10.

气主导体系下CO2水合物生长动力学试验

Investigation of CO2 hydrate growth kinetics in gas-dominated systems

  • 摘要:
    目的 CO2在低温、高压环境下极易与液态水生成水合物,进而影响管道的安全运行,因此有必要深入了解气体主导体系下管道中CO2水合物的生长特性,揭示CO2水合物在管道中的生长动力学特征,为CO2输送管道水合物的预测防治提供理论基础。
    方法 采用高压低温多相流动环道试验装置,在压力4.00~4.50 MPa、环境温度1.0~3.0 ℃、流速2.20 m/s、含水量4%的工况下,开展16组CO2水合物生长分解试验测试。探究低流速低含水量下气主导体系水合物的生长分解动力学过程、形成黏附机理,分析CO2水合物生长速率的影响因素,并且在Turner动力学模型的基础上,提出与系统温度、压力相关的比例因子u的关联式,改善传质作用与过冷度对CO2水合物生长速率的影响,从而修正Turner动力学基本模型。
    结果 CO2水合物的生长分解动力学过程表现为水合物诱导、快速生长、缓慢生长以及分解4个典型阶段;CO2水合物的诱导时间整体随初始压力的升高而减少,随环境温度的升高而增加;在低流速工况下低温与管壁积液是水合物生长的必要条件,传质作用是水合物生长的主控机制之一;水合物生长速率受系统温度、压力的控制,压力越高温度越低生长速率越快。
    结论 修正后的模型对水合物生长速率的预测平均相对误差由82.55%降至10.74%,显著提高了计算低流速气主导体系下水合物生长速率的预测精度。

     

    Abstract:
    Objective CO2 is prone to form hydrates when in contact with liquid water under low-temperature, high-pressure conditions, impacting the safe operation of pipelines. Thus, it is essential to enhance the understanding of CO2 hydrate growth characteristics in gas-dominated systems within pipelines, elucidate the growth kinetics of these hydrates, and establish a theoretical framework for predicting and preventing hydrate formation in CO2 transmission pipelines.
    Methods A high-pressure, low-temperature multiphase flow loop test device was employed to conduct 16 groups of tests on CO2 hydrate growth and decomposition under conditions of 4.00–4.50 MPa pressure, 1.0–3.0 °C ambient temperature, 2.20 m/s flow rate, and 4% water content. The growth and decomposition kinetics of hydrates in gas-dominated systems at low flow rates and low water content were analyzed, along with the adhesion mechanism during formation and factors influencing the growth rate of CO2 hydrates. Additionally, a correlation equation for the proportionality factor u, related to system temperature and pressure, was proposed based on the Turner kinetic model to enhance the understanding of mass transfer and supercooling effects on CO2 hydrate growth rates, thereby refining the basic Turner kinetic model.
    Results The kinetics of CO2 hydrate growth and decomposition were observed in four distinct stages: induction, rapid growth, slow growth, and decomposition. The induction time decreased with increasing initial pressure and increased with higher ambient temperatures. Low temperatures and liquid accumulation on the pipe wall were essential for hydrate growth under low flow rate conditions, with mass transfer identified as a primary control mechanism. The growth rate was influenced by system temperature and pressure; higher pressures and lower temperatures resulted in faster growth rates.
    Conclusion The average relative error of the modified model in predicting hydrate growth rates decreased from 82.55% to 10.74%, significantly enhancing the accuracy of predictions in gas-dominated systems under low flow rates.

     

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