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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

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 (002)

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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