Accessibility in alumina matrices of FCC catalysts

The accessibility in aluminas considered to be representative of matrices used in FCC resid catalysts, with mean pore sizes between 64 and 201 Å, was characterized through a kinetic approach by means of the conversion of 1,3,5-tri-isopropylbenzene (TIPB) at 500 °C in a CREC Riser Simulator fluidized...

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Autor principal: Falco, M.
Otros Autores: Morgado, E., Amadeo, Nora Elvira, Sedran, U.
Formato: Capítulo de libro
Lenguaje:Inglés
Publicado: Elsevier 2006
Acceso en línea:Registro en Scopus
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100 1 |a Falco, M. 
245 1 0 |a Accessibility in alumina matrices of FCC catalysts 
260 |b Elsevier  |c 2006 
270 1 0 |m Sedran, U.; Instituto de Investigaciones en Catálisis y Petroquímica (INCAPE), FIQ, UNL-CONICET, Santiago del Estero 2654, 3000 Santa Fe, Argentina; email: usedran@fiqus.unl.edu.ar 
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506 |2 openaire  |e Política editorial 
520 3 |a The accessibility in aluminas considered to be representative of matrices used in FCC resid catalysts, with mean pore sizes between 64 and 201 Å, was characterized through a kinetic approach by means of the conversion of 1,3,5-tri-isopropylbenzene (TIPB) at 500 °C in a CREC Riser Simulator fluidized bed laboratory reactor. The product distribution was essentially the same as that observed on an equilibrium commercial FCC catalyst, but the activity of the aluminas was much lower. The main products (propylene, benzene, isopropylbenzene, di-isopropylbenzenes) showed that a series cracking mechanism prevailed in the conversion of TIPB. The apparent first order kinetic constants assessed and the conversion profiles allowed establishing a ranking of activities that could be associated directly to accessibilities and not to the number of acid sites (Lewis nature), which was proportional to the specific surface area of the alumina. The sequence of accessibilities followed the same trend as the mean pore size of the aluminas. © 2006 Elsevier B.V. All rights reserved.  |l eng 
536 |a Detalles de la financiación: Agencia Nacional de Promoción Científica y Tecnológica, PICT2000-2001 14-08990 
536 |a Detalles de la financiación: 20-144 
536 |a Detalles de la financiación: Consejo Nacional de Investigaciones Científicas y Técnicas, PIP 0630/98 
536 |a Detalles de la financiación: This work was performed with the financial assistance of University of Litoral (Santa Fe, Argentina), Secretary of Science and Technology, Project CAID 2002 #20-144, CONICET, PIP 0630/98 and ANPCYT, PICT2000-2001 14-08990. The authors gratefully acknowledge the useful discussions with and contributions from Petrobras specialists Dr. Rosana L.P. Cardoso (GC–MS), and Denise Costa and Denise D. Filgueiras (FT-IR). 
593 |a Instituto de Investigaciones en Catálisis y Petroquímica (INCAPE), FIQ, UNL-CONICET, Santiago del Estero 2654, 3000 Santa Fe, Argentina 
593 |a Centro de Pesquisas e Desenvolvimento Leopoldo A.M. Mello, PETROBRAS (CENPES/TFCC), Cidade Universitária, Q.7, Rio de Janeiro 21949-900, Brazil 
593 |a Departamento de Ingeniería Química (FI, UBA), Ciudad Universitaria, 1428 Buenos Aires, Argentina 
690 1 0 |a ACCESSIBILITY 
690 1 0 |a ALUMINA 
690 1 0 |a CATALYTIC CRACKING 
690 1 0 |a MATRIX 
690 1 0 |a RESID 
690 1 0 |a ALUMINA 
690 1 0 |a CATALYTIC CRACKING 
690 1 0 |a FLUIDIZED BEDS 
690 1 0 |a MATRIX ALGEBRA 
690 1 0 |a PORE SIZE 
690 1 0 |a REACTION KINETICS 
690 1 0 |a ACCESSIBILITY 
690 1 0 |a ALUMINA MATRICES 
690 1 0 |a CRACKING MECHANISMS 
690 1 0 |a KINETIC CONSTANTS 
690 1 0 |a CATALYSTS 
700 1 |a Morgado, E. 
700 1 |a Amadeo, Nora Elvira 
700 1 |a Sedran, U. 
773 0 |d Elsevier, 2006  |g v. 315  |h pp. 29-34  |p Appl Catal A Gen  |x 0926860X  |w (AR-BaUEN)CENRE-3756  |t Applied Catalysis A: General 
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