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A generalized macroscopic kinetic model for description of gas hydrate formation processes in isothermal-isochoric systems

机译:用于描述等温-等渗体系中天然气水合物形成过程的广义宏观动力学模型

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摘要

A generalized macroscopic kinetic model based on the time variations of reaction chemical potential is presented for description of gas hydrate formation processes in isothermal-isochoric systems. Experimental gas hydrate formation data regarding different gas hydrate formers such as CH_4 (methane), C_2H_6 (ethane), C_3H_8 (propane), C0_2 (carbon dioxide), R-22 (hydrochlorofluorocarbon-22) and Xe (xylene) are employed to validate the proposed kinetic model. Different sets of experiments are carried out to assess the effects of different driving forces on the model accuracy. In a set of experiments, a constant pressure difference is applied and in the other set, a constant temperature difference is used to examine the model validity. Effect of agitation intensity on the gas consumption profile is also investigated. The proposed generalized model has been employed for description of gas consumption time variations during gas hydrate formation and presented in normalized coordinates. It is shown that at high agitation intensities when the reaction kinetic is rate controlling, a unique path exists for pure gas hydrate formation processes. The proposed macroscopic model can be used for studying gas hydrate formation processes in isothermal-isochoric systems.
机译:提出了基于反应化学势的时间变化的广义宏观动力学模型,用于描述等温-等渗体系中天然气水合物的形成过程。使用有关CH_4(甲烷),C_2H_6(乙烷),C_3H_8(丙烷),C0_2(二氧化碳),R-22(氢氯氟烃-22)和Xe(二甲苯)等不同气体水合物形成物的实验气体水合物形成数据进行验证提出的动力学模型。进行了不同的实验,以评估不同驱动力对模型精度的影响。在一组实验中,施加了恒定的压力差,而在另一组实验中,使用了恒定的温度差来检验模型的有效性。还研究了搅拌强度对气体消耗曲线的影响。提出的通用模型已用于描述天然气水合物形成过程中的气体消耗时间变化,并以归一化坐标表示。结果表明,在高搅拌强度下,当控制反应动力学速率时,存在纯气体水合物形成过程的独特路径。所提出的宏观模型可用于研究等温-等渗系统中天然气水合物的形成过程。

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