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Experimental study of hydrate dissociation in oil-dominated systems using a high-pressure visual cell

机译:利用高压视觉细胞对油管置系统水合物解离的实验研究

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摘要

To investigate hydrate dissociation process and manage hydrate risks efficiently in oil-dominated systems, a high-pressure cell equipped with visual windows was newly constructed where hydrates were firstly formed from natural gas + diesel + water systems for a water cut of 30% and then dissociated by heating, depressurization and methanol injection. Based on the experimental data of hydrate morphologies and thermodynamic parameters, hydrate macroscopic morphological evolvement together with dissociation rate and dissociation efficiency were analyzed for each dissociation method. The experimental results indicate that hydrates dissociate faster in strong shear areas and show shrinking core character when dissociating in oil-dominated systems. Macroscopic morphological evolvements are different for the three dissociation methods, which mainly include the way hydrates fall off the cell wall, the number and rate gas bubbles form and whether ice phase would appear. Gas migration pathway is firstly observed in depressurization dissociation and a macro physical model describing pipeline hydrate depressurization dissociation is proposed accordingly. A hydrate dissociation kinetic model with a good accuracy is established by using subcooling degree as the driving force. In experiments, dissociation rate and dissociation efficiency grow with the increase of heating temperature, depressurization rate and methanol concentration. However, self-preservation effect caused by ice formation would lead to a sharp decrease in dissociation rate and dissociation efficiency in depressurization processes. On experimental conditions, depressurization has the highest average dissociation rate while heating has the lowest average dissociation rate. The average dissociation rates in experiments are between 6.40 x 10(-4) similar to 2.09 x 10(-1) mol min(-1). (C) 2017 Elsevier B.V. All rights reserved.
机译:为了研究水合物解离过程并有效地在油束系统中有效地管理水合物风险,新建配备有视觉窗口的高压电池,其中首先由天然气+柴油+水系统形成水合物,用于30%,然后达到水通过加热,减压和甲醇注射分离。基于水合物形态学和热力学参数的实验数据,对每个解离方法分析了与解离率和解离效率的水合物宏观形态演化。实验结果表明,在强剪区域中的水合物在强剪区域中消失更快,并在解离灌木系统中分离时显示核心特征。对于三种解离方法的宏观形态演化是不同的,这主要包括水合物脱落细胞壁的方式,数量和速率气泡形式,以及是否会出现冰相。首先在减压解离中观察到气体迁移途径,并相应地提出描述管道水合物减压解离的宏观物理模型。通过使用过过冷却度作为驱动力来建立具有良好精度的水合物解离动力学模型。在实验中,解离率和解离效率随着加热温度,减压率和甲醇浓度的增加而生长。然而,由冰形成引起的自我保存效应将导致抑制率和减压过程中解离效率的急剧下降。在实验条件下,减压具有最高的平均解离速率,同时加热具有最低的平均离解率。实验中的平均解离速率在6.40×10(-4)之间,其与2.09×10(-1)mol min(-1)相似。 (c)2017 Elsevier B.v.保留所有权利。

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  • 作者单位

    China Univ Petr Shandong Key Lab Oil Gas Storage &

    Transportat Sa Qingdao 266580 Shandong Peoples R China;

    China Univ Petr Shandong Key Lab Oil Gas Storage &

    Transportat Sa Qingdao 266580 Shandong Peoples R China;

    China Univ Petr Shandong Key Lab Oil Gas Storage &

    Transportat Sa Qingdao 266580 Shandong Peoples R China;

    China Univ Petr Shandong Key Lab Oil Gas Storage &

    Transportat Sa Qingdao 266580 Shandong Peoples R China;

    China Univ Petr Shandong Key Lab Oil Gas Storage &

    Transportat Sa Qingdao 266580 Shandong Peoples R China;

    China Univ Petr Shandong Key Lab Oil Gas Storage &

    Transportat Sa Qingdao 266580 Shandong Peoples R China;

    China Univ Petr Shandong Key Lab Oil Gas Storage &

    Transportat Sa Qingdao 266580 Shandong Peoples R China;

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  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 石油、天然气工业;
  • 关键词

    Hydrate; Dissociation; Oil-dominated; Morphology; Model; Rate; Efficiency;

    机译:水合物;解离;油占状;形态;模型;率;效率;

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