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A comprehensive study of kinetics mechanism of Fischer-Tropsch synthesis over cobalt-based catalyst

机译:基于钴的钴催化剂的Fischer-Tropsch合成动力学机制综合研究

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A comprehensive kinetics study of Fischer-Tropsch (FT) synthesis mechanism was investigated over an in-house 37% Co-based catalyst on a SiO2 support. A series of combined FT and water gas shift (WGS) reaction mechanisms were developed in order to calibrate the model at twelve different operating conditions. Two different approaches were used to develop a model for the FT synthesis reaction network. The first was based on an empirical approach; whereas the second approach explained the novel mechanistic details of FT kinetics. In the former, the rate equations were derived by power-law rate expressions, while in the latter the rate equations were derived by the Langmuir-Flinshelwood-Houge n-Watson (LHHW) rate theory. The limitations of power-law rate model were highlighted for the applications that wider range of operating conditions has to be selected. In contrast the advantages of LHHW for predicting a wider range of operating conditions were underlined. A comprehensive plausible mechanism-derived FT kinetics models with eight elementary reaction pathways along with seven WGS kinetics models were developed. Such reaction networks were investigated to fit and validate against the newly obtained experimental results which can be used as a key tool to emphasise the most significant facts of FT synthesis catalysis and chemistry. Model validation was carried out subsequent to completion of the model calibration and the estimation of proper kinetic parameters. The overall purpose of the validation study was to ensure that the model provides a robust and realistic assessment of all the parameters. In order to ensure model is precise to an appropriate level, the model was assessed against experimental data at four different operating conditions. The results obtained from kinetic study were compared to the most recent findings that have been reported in literature. It was shown that the novel developed kinetic model based on a combination of allcylialkenyl mechanism for FT reactions (for production of n-paraffins and a-olefins) along with formate mechanism for WGS reaction can provide the most accurate predictions. (C) 2017 Elsevier Ltd. All rights reserved.
机译:在SiO 2载体上在内部37%Co-碱催化剂上研究了对Fischer-Tropsch(FT)合成机制的综合动力学研究。开发了一系列组合的FT和水煤气变换(WGS)反应机制,以便在12个不同的操作条件下校准模型。两种不同的方法用于开发FT合成反应网络的模型。第一个是基于经验方法;而第二种方法解释了FT动力学的新型机制细节。在前者中,速率方程由幂律速率表达得出,而在后者中,速率方程由Langmuir-Flinshelwood-Houge N-Watson(LHHW)速率理论得出。突出了幂律速率模型的局限性,用于更广泛的操作条件的应用程序。相比之下,LHHW用于预测更广泛的操作条件的优点是下划线。开发出具有八个基本反应途径的综合合理的机制衍生的FT动力学模型以及七个WGS动力学模型。研究了这种反应网络以适合并验证新获得的实验结果,可用作强调FT合成催化和化学最重要的事实的关键工具。在完成模型校准和适当的动力学参数估计之后进行模型验证。验证研究的整体目的是确保该模型提供对所有参数的强大和实际评估。为了确保模型精确到适当的水平,在四种不同的操作条件下评估模型的实验数据。将从动力学研究获得的结果与在文献中报告的最新发现进行了比较。结果表明,该新型开发了基于FT反应(用于生产N-链烷烃和α-烯烃)的组合的动力学模型以及用于WGS反应的甲酸机制可以提供最准确的预测。 (c)2017 Elsevier Ltd.保留所有权利。

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