Details
| Original language | English |
|---|---|
| Pages (from-to) | 18289-18294 |
| Number of pages | 6 |
| Journal | Angewandte Chemie - International Edition |
| Volume | 60 |
| Issue number | 33 |
| Early online date | 10 Jun 2021 |
| Publication status | Published - 3 Jul 2021 |
Abstract
The hydrogenation of sequestrated CO2 to methanol can reduce CO2 emission and establish a sustainable carbon circuit. However, the transformation of CO2 into methanol is challenging because of the thermodynamic equilibrium limitation and the deactivation of catalysts by water. In the present work, different reactor types have been evaluated for CO2 catalytic hydrogenation to methanol. Best results have been obtained in a bifunctional catalytic membrane reactor (CMR) based on a zeolite LTA membrane and a catalytic Cu-ZnO-Al2O3-ZrO2 layer on top. Due to the in situ and rapid removal of the produced water from the catalytic layer through the hydrophilic zeolite LTA membrane, it is effective to break the thermodynamic equilibrium limitation, thus significantly increasing the CO2 conversion (36.1 %) and methanol selectivity (100 %). Further, the catalyst deactivation by the produced water can be effectively inhibited, thus maintaining a high long-term activity of the CMR.
Keywords
- catalytic membrane reactor, CO-to-methanol, reaction–separation integration, zeolites
ASJC Scopus subject areas
- Chemical Engineering(all)
- Catalysis
- Chemistry(all)
- General Chemistry
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In: Angewandte Chemie - International Edition, Vol. 60, No. 33, 03.07.2021, p. 18289-18294.
Research output: Contribution to journal › Article › Research › peer review
}
TY - JOUR
T1 - Highly Selective CO2 Conversion to Methanol in a Bifunctional Zeolite Catalytic Membrane Reactor
AU - Yue, Wenzhe
AU - Li, Yanhong
AU - Wei, Wan
AU - Jiang, Jianwen
AU - Caro, Jürgen
AU - Huang, Aisheng
N1 - Funding Information: Financial supports by the National Natural Science Foundation of China (21761132003, 21878100), the Fundamental Research Funds for the Central Universities (40500–20101222093), DFG (Ca147/21) and the National University of Singapore and the Ministry of Education of Singapore (R‐279‐000‐598‐114, R‐279‐000‐574‐114, C‐261‐000‐207‐532/C‐261‐000‐777‐532) are acknowledged.
PY - 2021/7/3
Y1 - 2021/7/3
N2 - The hydrogenation of sequestrated CO2 to methanol can reduce CO2 emission and establish a sustainable carbon circuit. However, the transformation of CO2 into methanol is challenging because of the thermodynamic equilibrium limitation and the deactivation of catalysts by water. In the present work, different reactor types have been evaluated for CO2 catalytic hydrogenation to methanol. Best results have been obtained in a bifunctional catalytic membrane reactor (CMR) based on a zeolite LTA membrane and a catalytic Cu-ZnO-Al2O3-ZrO2 layer on top. Due to the in situ and rapid removal of the produced water from the catalytic layer through the hydrophilic zeolite LTA membrane, it is effective to break the thermodynamic equilibrium limitation, thus significantly increasing the CO2 conversion (36.1 %) and methanol selectivity (100 %). Further, the catalyst deactivation by the produced water can be effectively inhibited, thus maintaining a high long-term activity of the CMR.
AB - The hydrogenation of sequestrated CO2 to methanol can reduce CO2 emission and establish a sustainable carbon circuit. However, the transformation of CO2 into methanol is challenging because of the thermodynamic equilibrium limitation and the deactivation of catalysts by water. In the present work, different reactor types have been evaluated for CO2 catalytic hydrogenation to methanol. Best results have been obtained in a bifunctional catalytic membrane reactor (CMR) based on a zeolite LTA membrane and a catalytic Cu-ZnO-Al2O3-ZrO2 layer on top. Due to the in situ and rapid removal of the produced water from the catalytic layer through the hydrophilic zeolite LTA membrane, it is effective to break the thermodynamic equilibrium limitation, thus significantly increasing the CO2 conversion (36.1 %) and methanol selectivity (100 %). Further, the catalyst deactivation by the produced water can be effectively inhibited, thus maintaining a high long-term activity of the CMR.
KW - catalytic membrane reactor
KW - CO-to-methanol
KW - reaction–separation integration
KW - zeolites
UR - http://www.scopus.com/inward/record.url?scp=85109354921&partnerID=8YFLogxK
U2 - 10.1002/anie.202106277
DO - 10.1002/anie.202106277
M3 - Article
AN - SCOPUS:85109354921
VL - 60
SP - 18289
EP - 18294
JO - Angewandte Chemie - International Edition
JF - Angewandte Chemie - International Edition
SN - 1433-7851
IS - 33
ER -