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Fischer-Tropsch synthesis in a bench-scale two-stage multitubular fixed-bed reactor: Simulation and enhancement in conversion and diesel selectivity

机译:台式两级多管固定床反应器中的费托合成:转化率和柴油选择性的模拟和增强

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摘要

A process based on a two-stage multitubular fixed-bed reactor is presented to enhance in conversion and diesel selectivity for the Fischer-Tropsch synthesis (FTS) process, which is characterized by the condensation and separation of liquid products and water from the outlet of the first-stage reactor. A two-dimensional pseudohomogeneous reactor model is proposed to simulate the temperature profile and CO conversion of the two-stage fixed-bed process. Model calculations indicate that the condensation and separation of liquid products and water between the two stages of the multitubular fixed-bed reactor plays an important role by changing temperature profile and synthesis gas partial pressure of the second-stage reactor. The model validation has been verified on the basis of the bench-scale test data in a single-stage and two-stage fixed-bed reactor, respectively, which demonstrates the understandable products distribution shift toward diesel-range hydrocarbon. The combined action of higher temperature, syngas/H_2 partial pressure and readsorption of olefins at the two-stage fixed-bed reactor make CO conversion and C_(5+) selectivity increase, while CH_4 and CO_2 selectivity keep decreasing trends. Compared with the single-stage fixed-bed reactor process, the total CO conversion increases from 79% to 89% in the two-stage fixed-bed reactor process. The high valuable diesel range (C_(12)-C_(22)) increases significantly from 67% to 78%, while the gasoline range (C_5-C_(11)) decreases from 27% to 18%. The catalysts exhibit more stability and less deactivation rate over the two-stage fixed-bed process. The results are helpful to obtain more valuable diesel products and effective utilization of the syngas by the multistage fixed-bed process without tail gas recycling, which provides a practical case for multi-stage short reactor rather than one long reactor for FTS to improve products distribution.
机译:提出了一种基于两级多管固定床反应器的工艺,以提高费-托合成(FTS)工艺的转化率和柴油选择性,该工艺的特征是冷凝和分离出液态产物和水。第一阶段反应堆提出了二维伪均相反应器模型,以模拟两阶段固定床过程的温度分布和CO转化。模型计算表明,在多管固定床反应器的两个阶段之间,液体产物和水的冷凝和分离通过改变第二阶段反应器的温度分布和合成气分压起着重要作用。分别在单级和两级固定床反应器中的实验室规模试验数据的基础上,对模型验证进行了验证,这证明了可理解的产品分布向柴油范围碳氢化合物转移。高温,合成气/ H_2分压和烯烃在两级固定床反应器上的再吸收的综合作用使CO转化率和C_(5+)选择性增加,而CH_4和CO_2选择性保持下降趋势。与单级固定床反应器工艺相比,两级固定床反应器工艺的总CO转化率从79%增加到89%。高价值柴油范围(C_(12)-C_(22))从67%显着增加到78%,而汽油范围(C_5-C_(11))从27%减少到18%。在两步固定床工艺中,催化剂表现出更高的稳定性和更低的失活速率。研究结果有助于获得更多有价值的柴油产品,并通过多级固定床工艺有效利用合成气而无尾气再循环,这为多级短反应器而不是一台FTS长反应器提供了实际案例,以改善产品分布。

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