ISSN: 0304-128X ISSN: 2233-9558
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Publication history
Received December 28, 2024
Revised March 5, 2025
Accepted May 7, 2026
Available online July 29, 2026
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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The Design Of Continuous Fixed Bed Reactor For Biofuel Production Over Fischer-tropsch Synthesis

National Institute of Technology (ITN) Malang 1Malang State University
Korean Chemical Engineering Research, August 2026, 64(3), 105171
https://doi.org/10.9713/kcer.2026.64.3.105171
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Abstract

The development of continuous fixed-bed reactors is essential for studying reaction behavior and catalyst performance under elevated temperature and pressure. However, many Fischer–Tropsch (FT) reactor designs lack detailed specifications, leading to challenges in stability and reproducibility. This study presents a continuous fixed-bed tubular reactor for FT synthesis using synthesis gas (CO and H₂) with controlled temperature, pressure, and flow rate. The reactor employed a ceramic heater with PID controller and a modified double-stage regulator, achieving stable operation at 20 bar (±0.2 bar) and temperature fluctuations within ±3–4°C after reaching steady state over extended continuous operation periods up to 96 hours. The reaction produced two liquid phases: hydrocarbon-rich products in the upper layer and oxygenated compounds in the lower layer. GC-MS peak area analysis showed hydrocarbons were dominated by alkanes (C7–C25), with kerosene as the main fraction. Increasing catalyst weight raised alkane selectivity (up to 99.96%) and straight-chain hydrocarbons (up to 72.03%). This trend was attributed to reduced gas hourly space velocity (GHSV) and increased residence time, which promoted hydrogenation and chain growth. These results demonstrated stable reactor performance, with product distribution reported as relative composition rather than absolute yield.

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