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作 者:肖艳[1] 马凤云[1] 莫文龙[1] 王晔[1] 钟梅[1] 刘景梅[1] 肖峰[1] 李忠[2] 张静 马空军[1]
机构地区:[1]新疆大学化学化工学院,煤炭洁净转化与化工过程自治区重点实验室,新疆乌鲁木齐830046 [2]太原理工大学煤化工研究所,煤科学与技术教育部和山西省重点实验室,山西太原030024 [3]新疆庆华能源集团有限公司,新疆伊宁835100
出 处:《天然气化工—C1化学与化工》2015年第5期1-4,23,共5页Natural Gas Chemical Industry
基 金:乌鲁木齐市科学技术计划项目(G131010001)
摘 要:采用并流共沉淀法,以Na2CO3为沉淀剂,制备了Cu O/Zn O/Al2O3(CZA)和Zr-Cu O/Zn O/Al2O3(Zr-CZA)催化剂,对其进行了BET、XRD、FT-IR和SEM表征,并考察了其在浆态床中由合成气/CO2合成甲醇的催化性能。结果表明,Zr-CZA催化剂的比表面积达176.19m2·g-1,高于CZA催化剂的89.11m2·g-1;所制备的前驱体均发生了同晶取代反应,生成了活性物相锌孔雀石和绿铜锌矿,且Zr-CZA催化剂还原后的XRD峰更为弥散,说明其活性组分铜的晶粒尺寸更小;Zr-CZA催化剂的CO转化率明显高于CZA催化剂,且在566h的寿命试验中稳定性良好,失活速率仅为0.103%/d。CuO/ZnO/Al2O3 (CZA) and Zr-CuO/ZnO/A1203 (Zr-CZA) catalysts were prepared by parallel current co-precipitation method, and characterized by XRD, FT-IR, SEM and BET. The performances of the catalysts for synthesis of methanol from syngas/ CO., were investigated in a slurry reactor. Results showed that?the specific surface area of catalyst Zr-CZA was up to 176.19m2.g-1, much higher than that of catalyst CZA (89.11m2 .g-1); the isomorphous substitution reactions occurred in the precursors of both catalysts, generating active phase of rosasite and aurichatcite; XRD peaks of reduced Zr-CZA were more diffused, which indicated that its grain size of copper was smaller; and Zr-CZA obviously had higher CO conversion than CZA, and showed good stability in the life test of 566h with a deactivation rate of only 0.103%/d.
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