Structured internals for the intensified Fischer–Tropsch synthesis in fixed-bed reactors†

IF 3.1 3区 化学 Q2 CHEMISTRY, MULTIDISCIPLINARY Reaction Chemistry & Engineering Pub Date : 2024-12-23 DOI:10.1039/D4RE00550C
Evert Boymans, Yadolah Ganjkhanlou, Marco Denneman, Ben Sutens, Jasper Lefevere and Sander Grootjes
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Abstract

To accelerate the energy transition, processes for the production of sustainable fuels are desired such as the conversion of syngas from biogenic residues into liquid fuel by using the Fischer–Tropsch synthesis (FTS). These novel conversion processes are often of smaller scale due to the feedstock for which intensified reactor concepts are required. Structured reactors present viable alternatives to conventional packed bed reactors. Structured reactors can be obtained by e.g. loading a conventional tubular reactor with structured internals. Here, two strategies were followed in an effort to obtain the highest productivity per reactor volume, namely application of 3D-printed catalysts and secondly, thermally conductive aluminium and copper contactors filled with catalyst particles. Superior productivities were obtained by applying Al foam and 3D-printed Cu contactors when packed with FTS catalyst particles, with heat duties of respectively 880 kW m−3 and 1238 kW m−3 compared with only 185 kW m−3 for the 3D-printed catalyst and 218 kW m−3 for a conventional packed bed. For the system using the ordered 3D-printed Cu contactors, it presented a productivity of at least 0.85 gC5+ gcat−1 h−1. The excellent productivities could be correlated to the high thermal conductivity of the metal contactors facilitating the heat transfer from the bed centreline to the reactor wall as revealed by laser flash analysis (LFA) thermal conductivity measurements.

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固定床反应器中强化费托合成的结构内部结构
为加快能源转型,人们希望采用生产可持续燃料的工艺,如利用费托合成(FTS)将生物残留物中的合成气转化为液体燃料。由于原料的原因,这些新型转化工艺通常规模较小,因此需要强化的反应器概念。结构化反应器是传统填料床反应器的可行替代品。结构化反应器可以通过在传统管式反应器上加载结构化内件等方式获得。为了获得最高的单位反应器容积生产率,我们采用了两种策略,一是应用 3D 打印催化剂,二是在导热铝和铜接触器中填充催化剂颗粒。在使用泡沫铝和三维打印铜接触器填充 FTS 催化剂颗粒时,可获得更高的生产率,热负荷分别为 880 kW m-3 和 1238 kW m-3,而三维打印催化剂的热负荷仅为 185 kW m-3,传统填料床的热负荷为 218 kW m-3。对于使用有序三维打印铜接触器的系统,其生产率至少为 0.85 gC5+ gcat-1 h-1。激光闪烁分析(LFA)热导率测量结果表明,出色的生产率与金属接触器的高热导率有关,它促进了从床层中心线到反应器壁的热传导。
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来源期刊
Reaction Chemistry & Engineering
Reaction Chemistry & Engineering Chemistry-Chemistry (miscellaneous)
CiteScore
6.60
自引率
7.70%
发文量
227
期刊介绍: Reaction Chemistry & Engineering is a new journal reporting cutting edge research into all aspects of making molecules for the benefit of fundamental research, applied processes and wider society. From fundamental, molecular-level chemistry to large scale chemical production, Reaction Chemistry & Engineering brings together communities of chemists and chemical engineers working to ensure the crucial role of reaction chemistry in today’s world.
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