镍催化剂上甲烷蒸汽重整的一维模型

IF 0.1 Q4 ENVIRONMENTAL SCIENCES
R. Rakhi, Vivien Günther, J. Richter, F. Mauss
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引用次数: 8

摘要

碳氢化合物的蒸汽重整是一种成熟的化学过程,它提供合成气(H2和CO)。因此,这些合成产物可以转化为许多有价值的基础化学品。对于蒸汽重整的工业应用,详细了解该过程是先决条件。捕获详细的均相和非均相反应动力学和综合运输过程及其相互作用的模型有可能优化催化过程,而无需昂贵的实验活动。本文使用LOGEcat一维(1D)模型对镍基催化剂上甲烷蒸汽重整的多步反应机理进行了详细研究[1]。该模型适用于模拟所有标准的燃烧废气后处理催化过程,以及其他涉及多相催化的化学过程,如Sabatier过程[27]。它是一种一维工具,因此在计算上具有成本效益,并且基于一系列完美搅拌反应器(PSR)。利用该模型对不同工况下的温度、压力、流量和S/C比进行了模拟。对不同的化学反应参数,如选择性、产率、转化率和摩尔分数进行了计算,并与二维模拟和实验数据进行了比较。与参考数据相比,我们报告了与1D模型产生的各种剖面的非常好的一致性。请注意,本研究的主要目的是检查一维模型在多大程度上可以捕捉到基于镍基催化剂的甲烷蒸汽重整模型的基本化学性质。有趣的是,成本有效的降阶模型能够捕获与多步反应机制相关的物理和化学,显示了模型的预测能力。该研究为进一步分析该物质的热化学性质以建立动力学一致的反应机制奠定了基础。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Steam reforming of methane over nickel catalyst using a one-dimensional model
Steam reforming of hydrocarbons is a well established chemical process which provides synthesis gas (H2 and CO). These synthesis products can hence be converted to numerous valuable basic chemicals. For the industrial application of steam reforming, a detailed understanding of the process is a prerequisite. Models that capture the detailed homogeneous and heterogeneous reaction kinetics and the comprehensive transport processes as well as their interaction have the potential to optimize the catalytic process without expensive experimental campaigns. In this paper, a detailed investigation has been done using a multi-step reaction mechanism for modeling steam reforming of methane over nickel-based catalyst using a one-dimensional (1D) model, LOGEcat [1]. The model is applicable to the simulation of all standard after-treatment catalytic processes of combustion exhaust gas along with other chemical processes involving heterogeneous catalysis, such as, the Sabatier process [27]. It is a 1D tool, thus is computationally cost effective and is based on a series of perfectly stirred reactors (PSR). The model is used to perform the simulations for various reactor conditions in terms of temperature, pressure, flow rates and steam-to-carbon (S/C) ratio. Several chemical reaction terms, such as, selectivity, yield, conversion, and mole fraction have been shown with respect to the varied parameters and the results are compared with 2D simulations and experimental reference data. We report a very good agreement of the various profiles produced with 1D model as compared to the reference data. Note that the main aim of this study is to check how far the 1D model can capture the basic chemistry for modeling steam reforming of methane over nickel-based catalysts. It is interesting to note that the cost effective reduced order model is capable to capture the physics and chemistry involved with a multi-step reaction mechanism showing the predictive capability of the model. This study forms the basis for further analysis towards the thermochemistry of the species to develop a kinetically consistent reaction mechanism.
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