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Multiphase Analysis for High-Pressure Adsorption of CO2/Water Mixtures on Wet Coals

机译:湿煤对CO2 /水混合物高压吸附的多相分析

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Traditional modeling of gas adsorption on wet coals does not consider water as a separate adsorbed component and treats the adsorbed water as a "pacifier" of the coal matrix. In a recent work, we presented a new modeling approach for investigating the competitive adsorption of gas/water mixtures in high-pressure systems. We used the simplified local-density (SLD) model to investigate the effect of including the competitive adsorption of water present in coals on gas adsorption under the conditions encountered in coalbed methane (CBM) and CO2 sequestration applications. In continuation of that work, we present here a new multiphase algorithm to investigate the three-phase adsorption equilibrium of CO2/water mixtures on wet coals. When water is treated as one of the adsorbed components in a high-pressure gas adsorption system, as many as three fluid phases may coexist at equilibrium (gas, adsorbed, and liquid phases). A new algorithm is presented in this work to facilitate a Gibbs energy-driven multiphase analysis of the system. The algorithm employs a phase-insertion technique, which involves formally inserting a water-rich, bulk liquid phase and solving a three-phase flash problem, wherein the three phases are the adsorbed, bulk gas, and liquid phases. At equilibrium, the Gibbs energy of the system is calculated based on the phase distribution obtained at each step. This calculation is repeated sequentially with incrementally increased amounts of the inserted third phase. A minimum in the Gibbs energy at the given temperature and pressure, subject to material balance constraints, provides the equilibrium phase distribution in these systems. Multiphase analysis was performed for high-pressure CO2/water mixture adsorption on four wet coals utilizing this algorithm. Analysis indicates that a water-rich liquid phase is present in coals that contain large amounts of inherent moisture. For these coals, the water-rich phase appeared at the higher pressures in the isotherm and the fraction of this phase increased with bulk pressure, reaching a maximum near the CO2 critical pressure. In contrast, the low-moisture coals did not appear to contain a third-phase at equilibrium.
机译:湿煤对气体吸附的传统建模不认为水作为单独的吸附成分,并将吸附的水作为煤基质的“奶嘴”。在最近的工作中,我们提出了一种新的建模方法,用于研究高压系统中气体/水混合物的竞争吸附。我们使用了简化的局部密度(SLD)模型来研究包括在煤层气(CBM)和CO2封存应用中遇到的条件下煤中存在的水在气体吸附中存在的水的竞争吸附的效果。在继续这项工作中,我们在这里展示了一种新的多相算法,以研究湿煤对CO2 /水混合物的三相吸附平衡。当水被视为高压气体吸附系统中的吸附成分之一时,多达三个流体相可以在平衡(气体,吸附和液相)处共存。在这项工作中提出了一种新的算法,以便于系统的GIBBS能量驱动多相分析。该算法采用相位插入技术,其涉及正式插入富含水的散装液相并求解三相闪光问题,其中三相是吸附的,散装气体和液相。在平衡时,基于在每个步骤中获得的相分布来计算系统的GIBBS能量。该计算依次重复,逐渐增加插入的第三阶段的量。在给定的温度和压力下的GIBBS能量中的最小值,受到物质平衡约束,在这些系统中提供平衡相位分布。利用该算法对四个湿煤进行高压CO2 /水混合物吸附的多相分析。分析表明,含有富含水的液相含有大量固有水分的煤中存在。对于这些煤,富含水的相位出现在等温线的较高压力下,并且该相的级分随散装压力而增加,在CO 2临界压力附近达到最大值。相反,低水分煤没有似乎在平衡时含有第三阶段。

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