IAST Modelling of Competitive Adsorption, Diffusion and Thermodynamics for CO2-ECBM Process

M. Asif, Lei Wang, R. Hazlett, Galymzhan Serikov
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引用次数: 1

Abstract

The CO2 emission is one of the main causes for the global warming and it may be controlled by sequestrating CO2 into the geological formation. The coalbed formation provides a dual advantage for CO2 sequestration as CO2 may be stored in coal forever with enhancing the coalbed methane recovery. Thus, the cost of CO2 sequestration may be offset completely or partially. The main objective of the paper was to comprehend the CO2-ECBM displacement using the three concepts viz. competitive adsorption, diffusion, and thermodynamic modelling of coal In this paper, the pure gas isotherm on coal for CH4, and CO2 was evaluated using manometric method. The binary gas isotherm or competitive adsorption was studied using IAST modelling. MATLAB code was developed for the solution of IAST model and Newton Raphson approach was followed. The IAST modelling was done by taking 50%/%50 mole fraction of CH4/CO2. By analyzing the binary gas isotherm, the optimum injection pressure was evaluated. On the same injection pressure, co adsorption isotherm was drawn at different mole fraction of CO2 in gas phase. Separation factor was calculated by taking ratio of CO2 and CH4 in the gas and adsorbed phase respectively. Furthermore, adsorption data was used for discussing the sorption kinetics in coal and diffusion coefficient was evaluated. Furthermore, the thermodynamic parameters were also calculated and integrated with above noted parameters for the methane displacement in CO2-ECBM process. The CO2-ECBM displacement is very much dependent on the competitive adsorption and diffusion process in coal. The surface potential and Henry constant are important parameters for defining the CO2-ECBM displacement. The coadsorption isotherm was drawn at the optimum injection pressure and it shows that methane displacement would be the optimum by taking 11 %/89% mole fraction of CO2 and CH4 for two temperatures i.e., 288 K, 308 K. It is identified through diffusion regime that diffusion coefficient for the binary gas isotherm is the average of the diffusion coefficients of pure CO2 and CH4. This is the first kind of study which provides the completely integrated approach for describing the methane displacement in CO2-ECBM process. This novel study promotes our understanding of the complex mechanisms of CO2-ECBM displacement process.
CO2-ECBM过程竞争吸附、扩散和热力学的IAST模型
二氧化碳的排放是全球变暖的主要原因之一,可以通过将二氧化碳封存到地质构造中来控制。煤层气储层具有封存二氧化碳的双重优势,既可以将二氧化碳永久封存在煤中,又可以提高煤层气的采收率。因此,二氧化碳封存的成本可能被完全或部分抵消。本文的主要目的是利用煤的竞争吸附、扩散和热力学建模这三个概念来理解CO2- ecbm的位移。本文使用压力法评估了煤上CH4和CO2的纯气体等温线。采用IAST模型研究了二元气体等温线或竞争吸附。开发了求解IAST模型的MATLAB代码,采用牛顿-拉夫森法求解。采用50%/%50摩尔CH4/CO2分数进行IAST建模。通过分析二元气体等温线,确定了最佳注入压力。在相同注入压力下,绘制了不同气相CO2摩尔分数下的co吸附等温线。分别取气相和吸附相中CO2和CH4的比值计算分离系数。利用吸附数据讨论了吸附动力学,并计算了扩散系数。此外,还计算了CO2-ECBM过程甲烷置换的热力学参数,并与上述参数进行了积分。CO2-ECBM的驱替在很大程度上取决于煤中的竞争吸附和扩散过程。表面电位和亨利常数是确定CO2-ECBM位移的重要参数。绘制了最佳注入压力下的共吸附等温线,结果表明,在288 K、308 K两种温度下,CO2和CH4的摩尔分数分别为11% /89%时,甲烷排量最佳。通过扩散机制可以确定,二元气体等温线的扩散系数是纯CO2和CH4扩散系数的平均值。这是第一次为描述CO2-ECBM过程中甲烷置换提供了完全集成的方法。这项新研究促进了我们对CO2-ECBM置换过程的复杂机制的理解。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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