Modeling and optimization of a large-scale slurry bubble column reactor for producing 10,000 bbl/day of Fischer–Tropsch liquid hydrocarbons

Laurent Sehabiague , Romain Lemoine , Arsam Behkish , Yannick J. Heintz , Mariela Sanoja , Rachid Oukaci , Badie I. Morsi
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引用次数: 58

Abstract

A user-friendly simulator based on a comprehensive computer model for slurry bubble column reactors (SBCRs) for Fischer–Tropsch (F–T) synthesis, taking into account the hydrodynamics, kinetics, heat transfer, and mass transfer was developed. The hydrodynamic and mass transfer data obtained in our laboratories under typical F–T conditions along with those available in the literature were correlated using Back Propagation Neural Network and empirical correlations with high confidence levels. The data used covered wide ranges of reactor geometry, gas distributor, and operating conditions. All reactor partial differential equations, equation parameters and boundary conditions were simultaneously solved numerically.

The simulator was systematically used to predict the effects of reactor geometry (inside diameter and height) as well as superficial gas velocity and catalyst concentration on the performance of a large-scale SBCR provided with cooling pipes and operating under F–T conditions with cobalt-supported catalyst and H2/CO = 2. The performance of the SBCR was expressed in terms of CO conversion, liquid hydrocarbon yield, catalyst productivity, and space time yield. The simulator was also used to optimize the reactor geometry and operating conditions in order to produce 10,000 barrels/day (bbl/day) of liquid hydrocarbons.

1万桶/天费托液态烃大型浆态泡塔反应器的建模与优化
基于综合计算机模型,开发了一个考虑流体力学、动力学、传热和传质的费托合成浆体泡塔反应器(SBCRs)用户友好模拟器。我们的实验室在典型的F-T条件下获得的流体力学和传质数据与文献中可用的数据使用反向传播神经网络和高置信度的经验相关性进行关联。使用的数据涵盖了反应器几何形状、气体分布器和操作条件的广泛范围。同时对反应器的偏微分方程、方程参数和边界条件进行了数值求解。该模拟系统地预测了反应器几何形状(内径和高度)、表面气速和催化剂浓度对配备冷却管的大型SBCR性能的影响,并在钴负载催化剂和H2/CO = 2的F-T条件下运行。SBCR的性能以CO转化率、液态烃产率、催化剂生产率和时空产率表示。该模拟器还用于优化反应器的几何形状和操作条件,以生产1万桶/天的液态烃。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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