首页|煅烧温度对ZnGaZrOx/SAPO-34催化性能的影响

煅烧温度对ZnGaZrOx/SAPO-34催化性能的影响

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在CO2加氢制低碳烯烃(C2=-C4=)中,双功能催化剂的煅烧温度对其催化性能具有显著影响.基于此,采用共沉淀法制备了ZnGaZrOx氧化物,水热法制备了SAPO-34分子筛,然后对两者进行研磨制得ZnGaZrOx/SAPO-34双功能催化剂,并考察煅烧温度对ZnGaZrOx和SAPO-34物化性质及催化性能的影响.通过XRD、XPS、H2/CO2/NH3-TPD、SEM、N2吸附-脱附和原位DRIFTS表征发现,在制备ZnGaZrOx过程中,当煅烧温度为650℃时,ZnGaZrOx具有最强的H2和CO2吸附活化能力,能有效提高HCOO*和CH3O*的生成速率和浓度,促进甲醇产物生成;在制备SAPO-34过程中,当煅烧温度为450℃时,分子筛比表面积最大、晶粒尺寸最小、强酸位点的酸性最弱,能有效避免低碳烯烃发生二次加氢,从而获得较高的低碳烯烃选择性.最佳条件下合成的ZnGaZrOx/SAPO-34双功能催化剂在反应温度为390℃、压力为3 MPa、空速为3 600 mL/(g·h)条件下,CO2转化率为28.3%,CO选择性仅为44.6%,C2=-C4=选择性为84.4%,C2=-C4=产率高达13.2%,且在反应100 h内催化性能无明显衰减.该工作为双功能催化剂的改性提供了新的研究思路.
Effect of calcination temperature on catalytic performance of ZnGaZrOx/SAPO-34
In the hydrogenation of CO2 to low-carbon olefins(C2=-C4=),the calcination temperature of the bifunctional cata-lyst has significant effects on its catalytic performance.Based on this,ZnGaZrOx oxides were prepared by co-precipitation method and SAPO-34 molecular sieves were prepared by hydrothermal method,and then both of them were milled to pro-duce ZnGaZrOx/SAPO-34 bifunctional catalysts,and the effects of calcination temperature on the physicochemical proper-ties and catalytic performance of ZnGaZrOx and SAPO-34 were investigated.It was found by XRD,XPS,H2/CO2/NH3-TPD,SEM,N2 adsorption-desorption and in situ DRIFTS characterization that during the preparation of ZnGaZrOx,when the cal-cination temperature was 650℃,ZnGaZrOx had the strongest activation ability of H2 and CO2 adsorption,and it could effec-tively increase the rate and concentration of the generation of HCOO* and CH3O* to promote the methanol product genera-tion.During the preparation of SAPO-34,when the calcination temperature was 450℃,the molecular sieve had the largest specific surface area,the smallest grain size,and the weakest acidity of the strong acid site,which could effectively avoid the secondary hydrogenation of low-carbon olefins,thus obtaining higher selectivity of low-carbon olefins.The ZnGaZrOx/SAPO-34 bifunctional catalysts synthesized under the optimal conditions showed a CO2 conversion of 28.3%,a CO selectiv-ity of only 44.6%,a C2=-C4= selectivity of 84.4%,a C2=-C4= yield of as high as 13.2%at a reaction temperature of 390℃,a pressure of 3 MPa,and an airspeed of 3 600 mL/(g·h).And the catalytic performance did not decay significantly within 100 h of reaction.This work provided a new research idea for the modification of bifunctional catalysts.

CO2 hydrogenationlight olefinscalcination temperatureoxygen vacancyacidity

杨坤、任启霞、董永刚、刘飞、姚梦琴、曹建新

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贵州大学化学与化工学院,贵州贵阳 550025

贵州省绿色化工与清洁能源技术重点实验室,贵州贵阳 550025

贵州省工业废弃物高效利用工程研究中心,贵州贵阳 550025

CO2加氢 低碳烯烃 煅烧温度 氧空位 酸性

贵州省自然科学基金项目贵州省教育厅创新群体项目贵州大学实验室开放项目

黔科合基础-ZK[2023]重点004黔教合KY字[2021]010SYSKF2023008

2024

无机盐工业
中海油天津化工研究设计院 中国化工学会无机酸碱盐专业委员会

无机盐工业

CSTPCD北大核心
影响因子:0.489
ISSN:1006-4990
年,卷(期):2024.56(2)
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