Over 70% Conversion in the Direct Splitting of CO2 to CO via a Catalytic Membrane Reactor
Jinkun Tan , Zhengkun Liu , Wanglin Zhou , Guining Chen , Zhenbin Gu , Gongping Liu , Guangru Zhang , Wanqin Jin
Engineering ›› : 202509036
Carbon dioxide direct splitting (CDS;) has potential for converting CO2 into feedstocks and reducing CO2 emissions. Nevertheless, it is severely restricted by its thermodynamic equilibrium, resulting in a minimal 0.00052% CO2 conversion at 900 °C. By selectively removing the oxygen product, a catalytic membrane reactor (CMR) can shift the thermodynamic equilibrium of CDS, achieving CO2 conversions that exceed equilibrium limits. However, issues remain in CMRs, including low catalytic activity, high transport resistance, and inadequate driving force. At the same time, chemical industries burn a substantial quantity of low-grade hydrogen (H2) resources, resulting in low-quality combustion and energy inefficiency. Here, we construct a robust CMR that utilizes low-grade H2 resources for CO2 splitting, enabling an efficiency of over 70% for CO2 conversion at 900 °C. This ultra-high CO2 conversion is achieved by matching the reaction with oxygen separation in the CMR through the use of an active catalyst, a stable membrane, and an adequate driving force supplied by the low-grade H2 resource. This approach is projected to yield a significant reduction in CO2 emissions, holding the potential to mitigate carbon footprints across industrial sectors.
CO2 direct splitting / Membrane reactor / Low-grade H2 resource utilization / Oxygen-permeable membrane
| [1] |
|
| [2] |
|
| [3] |
|
| [4] |
|
| [5] |
|
| [6] |
|
| [7] |
|
| [8] |
|
| [9] |
|
| [10] |
|
| [11] |
|
| [12] |
|
| [13] |
|
| [14] |
|
| [15] |
|
| [16] |
|
| [17] |
|
| [18] |
|
| [19] |
|
| [20] |
|
| [21] |
|
| [22] |
|
| [23] |
|
| [24] |
|
| [25] |
|
| [26] |
|
| [27] |
|
| [28] |
|
| [29] |
|
| [30] |
|
| [31] |
|
| [32] |
|
| [33] |
|
| [34] |
|
| [35] |
|
| [36] |
|
| [37] |
|
| [38] |
|
| [39] |
|
| [40] |
|
| [41] |
|
| [42] |
|
| [43] |
|
| [44] |
|
| [45] |
|
| [46] |
|
| [47] |
|
| [48] |
|
| [49] |
|
| [50] |
|
/
| 〈 |
|
〉 |