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Steam conversion of carbon monoxide in an annular microchannel

環状マイクロチャネルにおける一酸化炭素の水蒸気改質 (AI 翻訳)

С. В. Димов, О. А. Гасенко

Thermophysics and Aeromechanics📚 査読済 / ジャーナル2026-07-25#水素対象セクター: energy
DOI: 10.1134/s0869864326010130
原典: https://doi.org/10.1134/s0869864326010130

🤖 gxceed AI 要約

日本語

本論文は、水素製造のためのマイクロチャネル反応器における一酸化炭素の水蒸気改質(水性ガスシフト反応)を実験的に検討したものである。白金触媒を用いた環状スロットチャネル内での反応熱特性と転化率を評価し、流量増加に伴う温度上昇と転化率低下を明らかにした。

English

This paper experimentally studies steam conversion of carbon monoxide (water-gas shift reaction) in a microchannel reactor for hydrogen production. Using a platinum catalyst in an annular slotted channel, it evaluates thermal characteristics and conversion rates, showing that increased flow rate raises temperature difference and decreases conversion.

Unofficial AI-generated summary based on the public title and abstract. Not an official translation.

📝 gxceed 編集解説 — Why this matters

日本のGX文脈において

日本では水素社会の実現が掲げられており、効率的な水素製造技術の開発は重要である。ただし、本論文は基礎的な反応工学的研究であり、直接的な政策や開示実務への応用は限定的である。

In the global GX context

This work contributes to hydrogen production technology, which is key for global decarbonization. However, it is a fundamental engineering study with limited direct applicability to climate disclosure or policy frameworks like TCFD/ISSB.

👥 読者別の含意

🔬研究者:Researchers in chemical engineering and hydrogen production may find the experimental data on microchannel reactors useful.

📄 Abstract(原文)

To create an efficient microchannel reactor for hydrogen production, steam reforming of carbon monoxide in a slotted annular channel was experimentally studied. The microchannel reactor is formed by a submillimeter gap between two cylinders, with a catalyst applied to the outer side of the inner cylinder. Platinum applied to cerium oxide was used as a catalyst. The thermal characteristics of the shift reaction with the formation of carbon dioxide and hydrogen were experimentally studied. Experiments were carried out at a steam-to-carbon monoxide ratio of 3:1 at different mixture flow rates. It was shown that a fourfold increase in the mixture flow rate leads to a significant increase in the temperature difference between the reactor inlet and outlet, caused by the heat release of the reaction (from Δ T ≈ 20 °C at a contact time of 189 ms to 80 °C at a contact time of 46 ms). According to analysis of the composition of the outgoing gas, with an increase in the mixture flow rate, the degree of carbon monoxide conversion decreases significantly.

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