Metal-Doped HZSM-5 Zeolite Catalysts for Catalytic Cracking of Raw Bio-Oil: Exploring Activity toward Value-Added Products

被引:3
作者
Chiosso, Maria Eugenia [1 ,2 ]
Crespo, Iratxe [3 ]
Merlo, Andrea Beatriz [4 ]
Valle, Beatriz [3 ]
机构
[1] Univ Nacl Noroeste Prov Buenos Aires UNNOBA, Dept Ciencias Bas & Expt, RA-6000 Junin, Buenos Aires, Argentina
[2] Ctr Invest & Transferencia Noroeste Prov Buenos Ai, CITNOBA UNNOBA UNSAdA CONICET, RA-2700 Pergamino, Buenos Aires, Argentina
[3] Univ Basque Country UPV EHU, Dept Chem Engn, POB 644, Bilbao 48080, Biscay, Spain
[4] Univ Nacl La Plata, Ctr Invest & Desarrollo Ciencias Aplicadas Dr Jorg, CCT CONICET La Plata, Calle 47 257, RA-1900 La Plata, Buenos Aires, Argentina
关键词
raw bio-oil; catalytic cracking; HZSM-5; active metal species; C-2-C-4; olefins; aromatics; FE/ZSM-5; CATALYSTS; ZSM-5; DEACTIVATION; ACIDITY; DEHYDROGENATION; VALORIZATION; REDUCTION; NOX;
D O I
10.3390/catal13081198
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Catalytic cracking of bio-oil, conducted at atmospheric pressure without hydrogen supply, is a cost-effective and versatile approach for the targeted synthesis of biofuels and platform chemicals. The conversion of raw bio-oil follows intricate reaction pathways strongly influenced by the catalyst properties. In this work, we explore the use of various transition metals (Cr, Fe, and Zn) to modify the properties of HZSM-5 zeolite and assess their impact on the catalytic cracking of real raw bio-oil feedstock. The effect of metal loading on physical and chemical characteristics of metal-doped zeolite catalysts was studied through XRD, XRF, N-2 physisorption, NH3-TPD, FTIR, H-2-TPR. The behavior of each catalyst was evaluated in a continuous two-step catalytic cracking system (TS-CC) operating at 450 degrees C and space-time 0.7 g(catalyst)h/g(feed). The results highlight the importance of carefully selecting active metal species to optimize the performance of HZSM-5 in the catalytic cracking of bio-oil. Cr and Fe were found to be effective metals in increasing the selectivity of C-2-C-4 olefins in the gas product and mono-aromatics in the hydrocarbon liquid product, whereas the Zn-doped catalyst exhibits poor activity compared to bulk zeolite. Furthermore, a significant impact of the metal oxidation state on catalytic activity was observed, with reduced metals promoting the formation of H-2, CO, and CO2 at the expense of hydrocarbon production.
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页数:14
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