4.6 Article

Tandem Electrocatalytic-Thermocatalytic Reaction Scheme for CO2 Conversion to C3 Oxygenates

期刊

ACS ENERGY LETTERS
卷 7, 期 9, 页码 2904-2910

出版社

AMER CHEMICAL SOC
DOI: 10.1021/acsenergylett.2c01454

关键词

-

资金

  1. U.S. Department of Energy, Office of Basic Energy Sciences, Catalysis Science Program [DE-FG02-13ER16381]
  2. Synchrotron Catalysis Consortium under the U.S. Department of Energy, Office of Basis Energy Sciences [DE-SC0012704, DE-SC0012653]
  3. U.S. Department of Energy, Office of Science, Office of Workforce Development for Teachers and Scientists, Office of Science Graduate Student Research (SCGSR) program
  4. ORAU [DE-SC0014664]
  5. U.S. Department of Energy (DOE) [DE-SC0012653] Funding Source: U.S. Department of Energy (DOE)

向作者/读者索取更多资源

A two-step tandem electrochemical-thermochemical reaction scheme is demonstrated to convert CO2 into value-added C-3 oxygenate molecules. The CO2 is first electrochemically reduced to ethylene, CO, and H-2, and then undergoes thermochemical hydroformylation reaction to produce 1-propanol and propanal. The tandem configuration achieved a selectivity of 18% for C3 oxygenate products, representing a significant improvement compared to direct electrochemical CO2 conversion methods.
A two-step tandem electrochemical-thermochemical re-action scheme is demonstrated to convert CO2 into value-added C-3 oxygenate molecules: CO2 was electrochemically reduced to ethylene, CO, and H-2, followed by the thermochemical hydroformylation reaction to produce 1-propanol and propanal. The CO2 electrolyzer was evaluated with Cu catalysts containing different oxidation states and with modifications to the gas diffusion layer hydrophobicity, while the hydroformylation reactor was tested over a Rh1Co(3)/MCM-41 catalyst. In situ X-ray absorption spectroscopy showed minimal changes to the Cu and Rh catalysts in the electrochemical and thermochemical reactions, respectively. The tandem configuration achieved a total C3 oxygenate product selectivity (on a basis of reduced CO2) of similar to 18%, representing over a 4-fold improvement compared to direct electrochemical CO2 conversion to 1-propanol in flow cells. Additionally, the CO2 electrolyzer was scaled to a 25 cm(2) device to enhance the C3 oxygenate production rate up to 11.8 mu mol min(-1) and demonstrate potential scalability of the tandem system.

作者

我是这篇论文的作者
点击您的名字以认领此论文并将其添加到您的个人资料中。

评论

主要评分

4.6
评分不足

次要评分

新颖性
-
重要性
-
科学严谨性
-
评价这篇论文

推荐

暂无数据
暂无数据