Petroleum Refinery Engineering ›› 2024, Vol. 54 ›› Issue (4): 33-38.
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Gan Ze, Li Chuan, Deng Wenan, Du Feng, Luo Hui, Li Shufeng
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甘泽, 李传, 邓文安, 杜峰, 罗辉, 李庶峰
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Abstract:
The effect of metal Ni modification on the activity of Cu/CeO2 catalyst for CO2 hydrogenation to methanol is investigated. The catalyst structure before and after modification is characterized by XRD, BET, XPS, H2-TPR, etc. The results show that the specific surface area of Cu/CeO2 is the largest at a metal loading of 20%. A Cu to Ni mass ratio of 3∶1 results in the largest catalyst alkalinity, the largest oxygen vacancy content, and the strongest Cu-Ni synergism. The catalyst shows a superior reaction effect of CO2 hydrogenation to methanol at a reaction temperature of 240 ℃, a reaction pressure of 3 MPa, a space velocity of 2,400 mL/(g·h), and an H2 to CO2 volume ratio of 3∶1, with a CO2 conversion of 18.5% and a methanol space time yield of 40.43 g/(kg·h).
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Key words: CO2, hydrogenation, methanol, Cu/CeO2 catalyst, reaction condition, conversion rate, selectivity, space time yield
摘要:
考察了第二金属Ni改性对CO2加氢制甲醇Cu/CeO2催化剂活性的影响,并通过XRD、BET、XPS、H2-TPR等手段对改性前后催化剂结构进行了表征。结果表明:金属负载量为20%时,Cu/CeO2的比表面积最大;Cu与Ni质量比为3∶1时,催化剂碱度最大,氧空位含量最高,Cu-Ni协同作用最强;该催化剂在反应温度240℃、反应压力3 MPa、液时空速2 400 mL/(g·h)、H2与CO2体积比为3∶1时催化CO2加氢制甲醇效果较优,CO2转化率为18.5%,甲醇时空产率为40.43 g/(kg·h)。
关键词: CO2, 加氢, 甲醇, Cu/CeO2催化剂, 反应条件, 转化率, 选择性, 时空产率
Gan Ze, Li Chuan, Deng Wenan, Du Feng, Luo Hui, Li Shufeng . Study on Cu/CeO2 catalyst for CO2 hydrogenation to methanol[J]. Petroleum Refinery Engineering, 2024, 54(4): 33-38.
甘泽, 李传, 邓文安, 杜峰, 罗辉, 李庶峰 . CO2加氢制甲醇Cu/CeO2催化剂实验研究[J]. 炼油技术与工程, 2024, 54(4): 33-38.
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