近临界和超临界CO/己烷混合物中CO在钴(0001)上吸附的大正则蒙特卡罗模拟:与费托合成的相关性

IF 3.9 3区 工程技术 Q2 ENGINEERING, CHEMICAL
Kenneth M. Benjamin*, Carrie Veer Horwath and Christer Karlsson, 
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引用次数: 0

摘要

在523.15 K(常见的超临界流体费托合成反应温度)条件下,用大正则蒙特卡罗(GCMC)模拟确定了CO/己烷混合物在近临界和超临界条件下对钴(0001)的吸附热力学。GCMC结果表明,由于CO具有较强的化学吸附反应能量,相对于己烷,CO优先吸附在催化剂表面,其表面覆盖度在0.9 ~ 1.5层之间。过量吸附分析表明,在大块CO化学势较大的情况下,催化剂表面(相对于大块流体混合物)的CO会耗损,这与更像液体的流体密度和更大的液相CO摩尔分数有关。在流体相混合物中体积CO化学势较小时,大量观察到过量CO吸附增强。在体积CO和己烷化学势较小的情况下,体积CO/己烷流体混合物更像气体,导致CO的过量吸附值为40-270%。对于这些相同的小体积CO化学势值,当从小体积己烷化学势穿越到大体积己烷化学势时,在体积流体混合物的伪临界点附近存在从类气体吸附到类液体吸附的转变。在己烷含量较高的液状体流体条件下,过量CO吸附量增加到近800%。在结构上,在几乎所有的超临界热力学状态下,钴表面几乎都有接近单层的CO覆盖。总体而言,随着体积己烷化学势的增大,CO吸附能的大小减小。CO吸附能的大小随CO体化学势的增大而减小。这是由于CO在催化剂表面的单层覆盖范围内发生了大量的排斥性、横向相互作用,以及在这些密度更大、富含CO的液体状散装超临界流体环境中CO的相互作用增强。这种增强的CO液相溶剂化与在相同条件下观察到的CO负载耗尽相一致。在体积流体赝临界压力下,吸附能行为的明显的气体和液体区域的转变是显著的。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Grand Canonical Monte Carlo Simulation of CO Adsorption on Cobalt(0001) in Near- and Super-critical CO/Hexane Mixtures: Relevance to Fischer–Tropsch Synthesis

Grand Canonical Monte Carlo Simulation of CO Adsorption on Cobalt(0001) in Near- and Super-critical CO/Hexane Mixtures: Relevance to Fischer–Tropsch Synthesis

Grand canonical Monte Carlo (GCMC) simulations have been used to determine the adsorption thermodynamics of carbon monoxide (CO) and hexane on cobalt(0001) in the presence of near- and super-critical fluid phase CO/hexane mixtures at 523.15 K, a common supercritical fluid Fischer–Tropsch synthesis reaction temperature. GCMC results indicate that CO preferentially adsorbs on the catalyst surface relative to hexane, with surface coverages ranging from 0.9 to 1.5 monolayers, due to the strong chemisorption reaction energetics. Excess adsorption analysis indicates depletion of CO on the catalyst surface (relative to the bulk fluid mixture) at large values of bulk CO chemical potential, which correlates with more liquid-like fluid densities and larger fluid phase CO mole fractions. At smaller bulk CO chemical potentials within the fluid phase mixture, enhanced excess CO adsorption is largely observed. At smaller bulk CO and hexane chemical potentials, the bulk CO/hexane fluid mixture is more gas-like, resulting in excess CO adsorption values of 40–270%. For these same small bulk CO chemical potential values, there is a transition from gas-like to liquid-like adsorption near the pseudocritical point of the bulk fluid mixture, as one traverses from small to large bulk hexane chemical potential. At the more hexane-rich, liquid-like bulk fluid phase conditions, excess CO adsorption increases to almost 800%. Structurally, near monolayer CO coverage and beyond on the cobalt surface is observed at nearly all supercritical thermodynamic states explored. Overall, the magnitude of the energy of adsorption for CO decreased as the bulk hexane chemical potential increased. Moreover, the magnitude of the energy of CO adsorption decreased as the bulk CO chemical potential increased. This was attributed to both to the large number of repulsive, lateral interactions of CO within its monolayer coverage on the catalyst surface and the enhanced CO interactions in these denser, CO-rich, liquid-like bulk supercritical fluid environments. This enhanced CO fluid-phase solvation aligns with the observed depletion in CO loadings under these same conditions. The distinct gas- and liquid-like regions of adsorption energy behavior were marked by a transition at the bulk fluid pseudocritical pressure.

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来源期刊
Industrial & Engineering Chemistry Research
Industrial & Engineering Chemistry Research 工程技术-工程:化工
CiteScore
7.40
自引率
7.10%
发文量
1467
审稿时长
2.8 months
期刊介绍: ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and products.
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