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1.中国海洋石油集团有限公司 液化天然气及低碳技术重点实验室,北京 100028
2.中海石油气电集团技术研发中心,北京 100028
3.云南大学 化学科学与工程学院,云南 昆明 650091
张瑜(1984—),硕士,高级工程师,研究方向为制氢及氢气利用技术,E-mail:zhangyu52@cnooc.com.cn。
顾榜(1990—),博士,副教授,研究方向为能源催化,E-mail:gubang@ynu.edu.cn。
收稿:2025-06-22,
修回:2025-07-29,
纸质出版:2026-05-25
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张瑜,郑元爽,王秀林等.制备方法对CuZnGa催化剂CO2加氢制甲醇催化性能的影响[J].低碳化学与化工,2026,51(5):29-35.
ZHANG Yu,ZHENG Yuanshuang,WANG Xiulin,et al.Effects of preparation methods on catalytic performances of CuZnGa catalysts for CO2 hydrogenation to methanol[J].Low-Carbon Chemistry and Chemical Engineering,2026,51(5):29-35.
张瑜,郑元爽,王秀林等.制备方法对CuZnGa催化剂CO2加氢制甲醇催化性能的影响[J].低碳化学与化工,2026,51(5):29-35. DOI: 10.12434/j.issn.2097-2547.20250280.
ZHANG Yu,ZHENG Yuanshuang,WANG Xiulin,et al.Effects of preparation methods on catalytic performances of CuZnGa catalysts for CO2 hydrogenation to methanol[J].Low-Carbon Chemistry and Chemical Engineering,2026,51(5):29-35. DOI: 10.12434/j.issn.2097-2547.20250280.
甲醇是一种重要的基础化工原料和能量载体,利用CO
2
催化加氢制甲醇在一定程度上可以缓解能源短缺问题,同时也符合绿色经济发展需求。比较了3种不同制备方法(共沉淀法、水热法和溶胶凝胶法)制备的CuZnGa催化剂在CO
2
加氢制甲醇反应中的性能差异,并结合XRD、TEM、N
2
吸/脱附、XPS、CO
2
-TPD和H
2
-TPR等对催化剂的物化性质进行了系统分析。结果表明,共沉淀法制备的催化剂具有最大的比表面积(49.0 m
2
/g)和最高的氧空位相对含量(19.8%),可提供更多活性位点,显著促进CO
2
的活化与转化。在260 ℃、4 MPa和7500 mL/(g·h)条件下反应10 h,共沉淀法制备催化剂的CO
2
转化率可达15.8%,甲醇选择性可达56.4%,表现出最优的催化性能。
Methanol is an important basic chemical feedstock and energy carrier. Utilizing CO
2
catalytic hydrogenation to methanol can alleviate energy shortages to a certain extent while also aligning with the demands of green economic development. CuZnGa catalysts were synthesized using three different methods (co-precipitation
hydrothermal and sol-gel methods). Their catalytic performances were systematically compared in CO
2
hydrogenation to methanol reaction. Characterization techniques including XRD
TEM
N
2
adsorption/desorption
XPS
CO
2
-TPD
and H
2
-TPR were used to analyze their physicochemical properties. The results show that among three catalysts
the catalyst prepared by co-precipitation exhibits largest specific surface area (49.0 m
2
/g) and highest relative oxygen vacancy (19.8%)
providing abundant active sites for CO
2
activation and conversion. Under reaction conditions of 260 ℃
4 MPa and 7500 mL/(g·h) for 10 h
it achieves CO
2
conversion rate of 15.8% and methanol selectivity of 56.4%
outperforming other catalysts.
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