首页|期刊导航|低碳化学与化工|造孔剂诱导合成FeCoCuAl催化剂及其与ZSM-5复合催化CO2加氢制高碳烃性能

造孔剂诱导合成FeCoCuAl催化剂及其与ZSM-5复合催化CO2加氢制高碳烃性能OACSTPCD

Pore-forming agent induced synthesis of FeCoCuAl catalysts and their performance in hydrogenation of CO2 to high carbon hydrocarbons with ZSM-5

中文摘要英文摘要

CO2加氢制高碳烃(C5+)是合成高值化学品和燃料的重要途径之一,这既可以实现碳减排,又有助于缓解能源压力.采用沉淀法和等体积浸渍法制备了K、Na修饰的FeCoCuAl催化剂,考察了造孔剂1,3,5-苯三甲酸(BTA)对其在CO2催化加氢制高碳烃反应(温度为300℃、压力为2.0 MPa、原料气n(H2):n(CO2)= 3:1且空速为3600 h-1、时间为6 h)中催化性能的影响.在FeCoCuAl-20.0BTA催化剂(n(BTA):n(Fe)= 20.0%)中引入ZSM-5分子筛,构建了一系列复合催化剂,并研究了其在CO2催化加氢制高碳烃反应中的催化性能.结合N2吸/脱附、X射线衍射(XRD)、H2-程序升温还原(H2-TPR)、CO2程序升温脱附(CO2-TPD)和H2升温脱附(CO2-TPD)等对催化剂的理化性质进行了表征,采用GC-MS对产物油相成分进行了分析.结果表明,与FeCoCuAl催化剂相比,FeCoCuAl-BTA催化剂的比表面积、孔容等均增大,并生成了更多的表面活性物种(Fe或Fe-Co合金),从而使得FeCoCuAl-BTA催化剂在CO2催化加氢反应中表现出更好的催化性能.FeCoCuAl-20.0BTA催化剂的CO2转化率和C5+选择性分别可达70%和42%.FeCoCuAl-20.0BTA催化剂催化CO2加氢生成的产物以C2~C4产物为主,而在FeCoCuAl-20.0BTA催化剂与ZSM-5分子筛以质量比为1.0、颗粒机械混合方式构建的复合催化剂上,FeCoCuAl-20.0BTA上生成的C2~C4产物可在ZSM-5分子筛上发生原位链增长、异构化和芳构化反应,从而提高了CO2转化率和C5+选择性,分别达到79%和66%.

CO2 hydrogenation to high-carbon hydrocarbons(C5+)is one of the important ways to synthesize high-value chemicals and fuels,which can achieve carbon emission reduction as well as help to alleviate energy pressure.K-and Na-modified FeCoCuAl catalysts were prepared by precipitation and iso-volumetric impregnation methods,and the effects of the pore-forming agent 1,3,5-benzenetricarboxylic acid(BTA)on their catalytic performance in CO2-catalyzed hydrogenation to high-carbon hydrocarbons reaction(temperature of 300℃,pressure of 2.0 MPa,n(H2):n(CO2)= 3:1 and space velocity of 3600 h-1 of feed gas,reaction for 6 h)were investigated.ZSM-5 molecular sieve was introduced into FeCoCuAl-20.0BTA catalyst(n(BTA):n(Fe)= 20.0%)to construct a series of composite catalysts and their catalytic performance in the reaction of catalytic hydrogenation of CO2 to high-carbon hydrocarbons was investigated.The physicochemical properties of the catalysts were characterized by combining N2 adsorption/desorption,X ray diffraction(XRD),H2-temperature programmed reduction(H2-TPR),CO2 temperature programmed desorption(CO2-TPD),and H2 temperature programmed desorption(CO2-TPD),and the oil-phase compositions of the products were analyzed by GC-MS.The results show that compared with FeCoCuAl catalysts,the specific surface area and pore volume of FeCoCuAl-BTA catalysts increase,and generate more surface-active species(Fe or Fe-Co alloy),which lead to better catalytic performance of FeCoCuAl-BTA catalysts in CO2 catalytic hydrogenation reaction.The CO2 conversion rate and C5+ selectivity of FeCoCuAl-20.0BTA catalyst are up to 70% and 42%,respectively,and the products generated from CO2 hydrogenation catalyzed by FeCoCuAl-20.0BTA catalyst are mainly C2~C4 products,while on the composite catalyst constructed with FeCoCuAl-20.0BTA catalyst and ZSM-5 molecular sieve in the form of mechanical mixing of particles with the mass ratio of 1.0,the C2~C4 products generated on FeCoCuAl-20.0BTA can undergo in situ chain growth,isomerization and aromatization reactions on ZSM-5 molecular sieves,which lead to the improvement of CO2 conversion rate and C5+ selectivity,reaching 79% and 66%,respectively.

赵治华;徐成华;任红;罗晶;杜磊;刘晨龙;陈雯婧;罗静

成都信息工程大学 资源环境学院 大气环境模拟与污染控制四川省高校重点实验室,四川 成都 610225成都信息工程大学 资源环境学院 大气环境模拟与污染控制四川省高校重点实验室,四川 成都 610225成都信息工程大学 资源环境学院 大气环境模拟与污染控制四川省高校重点实验室,四川 成都 610225成都信息工程大学 资源环境学院 大气环境模拟与污染控制四川省高校重点实验室,四川 成都 610225成都信息工程大学 资源环境学院 大气环境模拟与污染控制四川省高校重点实验室,四川 成都 610225成都信息工程大学 资源环境学院 大气环境模拟与污染控制四川省高校重点实验室,四川 成都 610225成都信息工程大学 资源环境学院 大气环境模拟与污染控制四川省高校重点实验室,四川 成都 610225成都信息工程大学 资源环境学院 大气环境模拟与污染控制四川省高校重点实验室,四川 成都 610225

化学工程

造孔剂FeCoCuAl催化剂ZSM-5CO2加氢高碳烃

pore-forming agentFeCoCuAl catalystsZSM-5CO2 hydrogenationhigh-carbon hydrocarbons

《低碳化学与化工》 2024 (2)

10-16,7

四川省科技厅自然科学基金(2022NSFSC1058)四川省科技厅国际合作项目(2020YFH0133).

10.12434/j.issn.2097-2547.20230234

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