Characterization of sepiolite as a support of silver catalyst in soot combustion

被引:38
作者
Guengoer, Nurfer
Isci, Sevin
Guenister, Ebru
Mista, Wlodzimierz
Teterycz, Helena
Klimkiewicz, Roman
机构
[1] Polish Acad Sci, Inst Low Temp & Struct Res, PL-50422 Wroclaw, Poland
[2] Wroclaw Univ Technol, Fac Microsyst Elect & Photon, PL-50370 Wroclaw, Poland
[3] Istanbul Tech Univ, Dept Phys, TR-34469 Istanbul, Turkey
关键词
soot combustion; sepiolite; zirconium oxide; silver; support; catalyst;
D O I
10.1016/j.clay.2006.03.005
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
Turkish sepiolite-zirconium oxide mixtures were applied as a support for the silver catalyst in a soot combustion. Sepiolite-Zr-K-Ag-O catalyst was characterized by XRD, N-2 adsorption, SEM, TPR-H-2 and EGA-MS. The combustion of soot was studied with a thermobalance (TG-DTA). The modification resulted in a partial degradation of the sepiolite structure, however, the morphology was preserved. The adsorption of N-2 of the modified sepiolite is a characteristic for mesoporous materials with a wide distribution of pores. The specific surface area S-BET equals 83 m(2)/g and the pores volume is 0.23 cm(3)/g. The basic character of the surface centers of sepiolite is indicated by CO2 desorption (TPD-MS) at 170 degrees C and at about 620 degrees C due to a surface carbonates decomposition. The thermodesorption of oxygen at 650-850 degrees C indicates the decomposition of AgOx phases at the surface. The presence of AgOx phases is also confirmed by TPR-H2 spectrum (low temperature reduction peak at 130 and 180 degrees C). The high-temperature reduction at about 570 degrees C is probably related to Ag-O-M phases on the support. The soot combustion takes place at T-50=575 degrees C. Without silver (sepiolite-Zr-K-O) T-50=560 degrees C but sepiolite modified with silver (sepiolite-Zr-K-Ag-O) undergoes the same process at T-50=490 degrees C. (C) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:291 / 296
页数:6
相关论文
共 38 条
[1]   Dehydration-dehydrogenation of 1-phenylethanol over acid-basic catalysts [J].
Aramendia, MA ;
Borau, V ;
Jimenez, C ;
Marinas, JM ;
Porras, A ;
Urbano, FJ .
REACTION KINETICS AND CATALYSIS LETTERS, 1998, 65 (01) :25-31
[2]   Silica from sepiolite: Preparation, textural properties, and use as support to catalysts [J].
Aznar, AJ ;
Gutierrez, E ;
Diaz, P ;
Alvarez, A ;
Poncelet, G .
MICROPOROUS MATERIALS, 1996, 6 (02) :105-114
[3]   A screening study on the activation energy of vanadate-based catalysts for diesel soot combustion [J].
Badini, C ;
Saracco, G ;
Russo, N ;
Specchia, V .
CATALYSIS LETTERS, 2000, 69 (3-4) :207-215
[4]   An experimental and theoretical investigation of the behavior of a monolithic Ti-V-W-sepiolite catalyst in the reduction of NOx with NH3 [J].
Bahamonde, A ;
Beretta, A ;
Avila, P ;
Tronconi, E .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (08) :2516-2521
[5]   Designing the adequate base solid catalyst with Lewis or Bronsted basic sites or with acid-base pairs [J].
Climent, MJ ;
Corma, A ;
Iborra, S ;
Velty, A .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2002, 182 (01) :327-342
[6]   Alkali-exchanged sepiolites containing palladium as bifunctional (basic sites and noble metal) catalysts for the Heck and Suzuki reactions [J].
Corma, A ;
García, H ;
Leyva, A ;
Primo, A .
APPLIED CATALYSIS A-GENERAL, 2004, 257 (01) :77-83
[7]   INFLUENCE OF THE PROCEDURE OF NICKEL DEPOSITION ON THE TEXTURAL AND CATALYTIC PROPERTIES OF NICKEL SEPIOLITE CATALYSTS [J].
CORMA, A ;
MIFSUD, A ;
PARIENTE, JP .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1988, 27 (11) :2044-2050
[8]   Surface and catalytic properties of lanthanum-promoted Ni/sepiolite catalysts for styrene hydrogenation [J].
Damyanova, S ;
Daza, L ;
Fierro, JLG .
JOURNAL OF CATALYSIS, 1996, 159 (01) :150-161
[9]   A simplified approach to determine the activation energies of uncatalyzed and catalyzed combustion of soot [J].
Dernaika, B ;
Uner, D .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2003, 40 (03) :219-229
[10]  
ECE OI, 1994, CLAYS CLAY MINER, V42, P82