Abstract
H2/N2 synthesis gas is of great importance for the ammonia industry, and its production process is both complex and energy consuming. Nitrous oxide (N2O) is a potent greenhouse gas (GHG) that also depletes the stratospheric ozone. Here, we propose a novel concept of a membrane reactor in which ammonia synthesis gas production, N2O decomposition, and water splitting are combined. In this process, oxygen produced from N2O decomposition and water splitting is removed by a dense oxygen permeable membrane, which then reacts with oxygen-consuming gas. This promising membrane reactor process has been successfully demonstrated by experiment. By optimizing the N2O and H2O flow rate, a complete N2O decomposition is achieved, and a synthesis gas with a molar ratio of H2/N2 = 3:1 is produced at the same time. At 850 °C, a H2 production rate of 14.85 mL/min and a N2 production rate of 5.07 mL/min are derived from the membrane reactor with 100% N2O conversion and 29.60% H2O conversion. The reactor also exhibits excellent stability over a 300 h long-term test. This study will give some constructive guides to the subsequent work on process intensification through the membrane reactor and may lead to the development of green chemical production.
| Original language | English |
|---|---|
| Pages (from-to) | 3066-3072 |
| Number of pages | 7 |
| Journal | Industrial and Engineering Chemistry Research |
| Volume | 60 |
| Issue number | 7 |
| DOIs | |
| Publication status | Published - 24 Feb 2021 |
| Externally published | Yes |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
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