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Accurate Prediction of Dissociation Pressures of Natural Gas Hydrates Containing Carbon Dioxide and Hydrogen Sulfide for Efficient Flow Assurance Phenomena

机译:准确预测含二氧化碳和硫化氢的天然气水合物的解离压力,以实现有效的流量保证现象

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Information on the phase behavior of gas hydrate is vital for several mitigation techniques to control their formation in pipelines and surface facilities for efficient flow assurance during the production and transportation of natural gas and reservoir fluids. The pipeline environment (high pressure and low temperature) favors the formation of natural gas hydrate, which is one of the main elements in the flow assurance issues and this has to be taken in to account very seriously. Depending upon the composition of the gas produced, hydrates can form different physical structures and thus require careful attention whole modeling their phase behavior. The better thermodynamic models are necessary to design and understand the phase behavior of produced trapped natural gas from natural gas hydrates from subsea environments. Most of the models available in an open literature are primarily applicable at relatively low pressure condition. In this work, model of Chen and Guo along with the three famous Equation of States (EoS), namely, Peng-Robinson (PR), Peng-Robinson-Stryjek-Vera (PRSV) and Soave-Redlich-Kwong (SRK), are used to model the hydrate phase behavior at high pressure conditions. Their efficacy to model phase behavior for hydrates of pure natural gases and gas mixture containing H2S and CO2 is presented and tested against the experimental data available from open literature at high pressures conditions. The developed model uses the published Lennard-Jones cell potentials of typical gas species that form hydrates assuming the adsorption would be carried out in the cavities of hydrate structures. We optimized the computed phase diagrams based on three EoS with experimental phase diagram data from literature and determined the model parameters with less percentage average deviation. The present papers discusses about modeling of the phase behavior of binary gas mixture hydrates like CH4-C2H6, CH4-CO2 and CH4-H2S. Model predictions are validated against the experimental data from the literature, and observed to be in well agreement for high pressure range which helps in the flow assurance. Such models shows potential of their application in understanding flow assurance phenomena at higher pressure.
机译:有关天然气水合物的相位行为的信息对于多种减缓技术至关重要,以控制其在管道和表面设施中的形成,以便在生产和运输天然气和储层流体期间有效的流动保证。管道环境(高压和低温)有利于形成天然气水合物,这是流动保证问题中的主要元素之一,这必须非常认真地考虑。取决于所产生的气体的组成,水合物可以形成不同的物理结构,因此需要仔细注意整个模拟它们的相位行为。更好的热力学模型对于设计和理解来自海底环境的天然气水合物生产的被捕获的天然气的相位行为。开放文献中的大多数型号主要适用于相对低的压力条件。在这项工作中,陈和郭的模型以及各州的三个着名方程(EOS),即彭罗宾逊(PR),彭罗宾逊 - Stryjek-Vera(PRSV)和Soave-Redlich-Kwong(SRK),用于在高压条件下模拟水合物相行为。它们的效力为纯天然的气体和含有H 2 S和CO 2气体混合物的水合物模型相行为被呈现并且针对在高压条件下可从公开的文献中的实验数据进行测试。开发的模型使用出版的Lennard-Jones电池屏幕,其假设吸附在水合物结构的空腔中进行水合物的典型气体物种。我们基于三个EOS优化了计算的相图,其中具有来自文献的实验相图数据,并确定了平均偏差较少的模型参数。本文讨论了二元气体混合物水合物的阶段行为的建模,如CH 4 -C 2 H6,CH 4 -CO 2和CH 4 -H2s。根据来自文献的实验数据验证了模型预测,并且观察到高压范围内的一致性,有助于流动保证。这些模型显示其应用在理解在更高压力下的流动保证现象中的应用。

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