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Enhancing continuous-flow reactions via compression-molding of solid catalysts and dilutants in packed-bed systems
Kwihwan Kobayashi1, Teruhiko Tanaka1, Yoshihiro Kon1
1Interdisciplinary Research Center for Catalytic Chemistry, National Institute of Advanced Industrial Science and Technology Central 5, Higashi 1-1-1 Tsukuba Ibaraki 305-8565 Japan h-kawanami@aist.go.jp n-koumura@aist.go.jp.
RSC Advances
|February 23, 2024
Summary
This study introduces an improved packed-bed reactor for continuous-flow reactions. By compression-molding platinum (Pt) and silica gel (SiO2), Pt-leaching is suppressed, enabling efficient scaled-up reactions.
Area of Science:
- Chemical Engineering
- Materials Science
Background:
- Continuous-flow reactions are crucial in chemical synthesis.
- Platinum (Pt) catalysts are widely used but prone to leaching.
- Packed-bed reactors offer advantages for heterogeneous catalysis.
Purpose of the Study:
- To develop an improved packed-bed system for continuous-flow reactions.
- To suppress platinum (Pt) leaching from the reaction column.
- To achieve high productivity in scaled-up flow reactions.
Main Methods:
- Utilizing platinum (Pt)-black powder and silica gel (SiO2) in a packed-bed system.
- Employing compression-molding of Pt and SiO2 to enhance stability.
- Analyzing particle-size distribution and using scanning electron microscopy (SEM).
Main Results:
- Compression-molding effectively suppressed Pt-leaching from the packed-bed reactor.
- Crushed and downsized SiO2 particles proved effective in preventing outflow.
- A scaled-up flow reaction in a large column demonstrated excellent productivity.
Conclusions:
- The improved packed-bed system effectively minimizes Pt-leaching.
- Downsized silica gel enhances catalyst retention in continuous-flow systems.
- The developed system is suitable for efficient, large-scale chemical synthesis.

