催化作用
共沉淀
甲醇
材料科学
产量(工程)
铜
化学工程
接触角
活性炭
碳纳米管负载催化剂
催化剂载体
无机化学
一氧化碳
催化剂中毒
工业催化剂
碳纤维
多相催化
化学
作者
Zhipeng Qiao,Yukai Wang,Fanhui Meng,M. Xing,Jieying Jing,Zhong Li,Wenying Li
标识
DOI:10.1021/acsami.5c26122
摘要
The byproduct water produced in the CO2 hydrogenation to methanol process inevitably oxidizes the active Cu0 of Cu-based catalysts, resulting in catalyst deactivation. Here, the CuZn catalyst is prepared by the coprecipitation method and modified with Zr and chitosan to prepare CuZn@Zr and CuZn@ZrC catalysts. All of the catalysts are investigated for the hydrogenation of CO2 to methanol. For the modified CuZn@ZrC catalyst with the carbon layer, the water contact angle remains stable at 122° even after 10 s, while that of the CuZn catalyst decreases rapidly from 124° to 39° within 2 s. The amount of desorbed CO2 for CuZn@ZrC (320.5 μmol/g) is larger than that for CuZn (192.3 μmol/g). After a 280 h reaction at 240 °C, 3.0 MPa, and 3000 mL·h-1·g-1, the deactivation rate of methanol space-time yield for CuZn@ZrC is only 0.22%/h, whereas for CuZn, it is 0.33%/h. The active Cu0 in the spent CuZn catalyst is oxidized to Cu2+, which results in deactivation. The Cu0 in the spent CuZn@ZrC catalyst remains the dominant copper species due to the presence of a hydrophobic carbon layer that inhibits contact with water. The findings provide a framework for the design and optimization of the required catalyst with the aim of enhancing the catalytic stability in reactions involving water.
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