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Poly-dimethylsiloxane (PDMS) based micro-reactors for steam reforming of methanol
Authors:Ji Won Ha  Jae Hyuk Jang
Affiliation:
  • a Department of Chemistry, Rice University, 6100 Main Street, Houston, TX 77005, United States
  • b The University of Texas of The Permian Basin, 4901 E University Road, Odessa, TX 79762, United States
  • c eMD Center, Corporate R&D Institute, Samsung Electro-Mechanics, 314, Maetan3-Dong, Yeongtong-Gu, Suwon, Gyunngi-Do, 443-743, Republic of Korea
  • Abstract:A miniaturized methanol steam reformer with a serpentine type of micro-channels was developed based on poly-dimethylsiloxane (PDMS) material. This way of fabricating micro-hydrogen generator is very simple and inexpensive. The volume of a PDMS micro-reformer is less than 10 cm3. The catalyst used was a commercial Cu/ZnO/Al2O3 reforming catalyst from Johnson Matthey. The Cu/ZnO/Al2O3 reforming catalyst particles of mean diameter 50-70 μm was packed into the micro-channels by injecting water based suspension of catalyst particles at the inlet point. The miniaturized PDMS micro-reformer was operated successfully in the operating temperatures of 180-240 °C and 15%-75% molar methanol conversion was achieved in this temperature range for WHSV of 2.1-4.2 h−1. It was not possible to operate the micro-reformer made by pure PDMS at temperature beyond 240 °C. Hybrid type of micro-reformer was fabricated by mixing PDMS and silica powder which allowed the operating temperature around 300 °C. The complete conversion (99.5%) of methanol was achieved at 280 °C in this case. The maximum reformate gas flow rate was 30 ml/min which can produce 1 W power at 0.6 V assuming hydrogen utilization of 60%.
    Keywords:Micro-reformer   PDMS   Methanol   Steam reforming   Catalyst
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