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A Fugacity Based Kinetic Model for Supercritical Fischer –Tropsch Synthesis Over Cobalt-Based Catalytic Systems

机译:钴基催化体系超临界费托合成的动力学模型

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A kinetic model for Fischer-Tropsch synthesis (FTS) in both conventional reactionmedia (gas-phase) and non-conventional media (near-critical and supercritical solventmedia) was derived from experimental data generated from a commercial aluminasupported cobalt catalyst (15% Co/Al2O3). The model was developed based on partialpressures assuming ideal gas phase as well as based on fugacity coefficients toaccount for the non-ideality in the near critical and supercritical phase. The estimatedkinetics parameters from the fugacity-based model were compared to the kineticsparameters obtained from the ideal gas assumption using the partial pressure basedkinetic model. Similarly, the fugacity-based model successfully predict the methaneformation rates for gas phase as well as near critical and supercritical phase FTS. It wasobserved that the fugacity-based models more accurately predicted the carbonmonoxide consumption rate in gas-phase as well as near critical and supercritical FTSconditions. Our qualitative conclusion is that fugacity-based model will also do a betterjob than the partial pressure based model in predicting the chain growth probability ofthe cobalt catalyst since it can better account for the non-ideality of the reaction in thegas-phase FTS (high pressures operation) and in the near-critical and supercriticalphase.
机译:两种常规反应中费托合成(FTS)的动力学模型 介质(气相)和非常规介质(近临界和超临界溶剂) 介质)是从商业氧化铝产生的实验数据中得出的 负载钴催化剂(15%Co / Al2O3)。该模型是基于部分 假定理想气相的压力以及基于逸度系数的 造成了近临界和超临界阶段的非理想状态。估计 将基于逸度的模型的动力学参数与动力学进行了比较 使用基于分压的理想气体假设获得的参数 动力学模型。同样,基于逸度的模型可以成功预测甲烷 气相以及近临界和超临界相FTS的形成速率。它是 观察到,基于逸度的模型可以更准确地预测碳 气相以及接近临界和超临界FTS的一氧化碳消耗率 情况。我们的定性结论是,基于逸度的模型也可以做得更好 比基于分压力的模型预测链增长概率的工作要好 钴催化剂,因为它可以更好地说明反应中不理想 气相FTS(高压运行)以及近临界和超临界 阶段。

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