Measurement of the effective diffusivity for a vanadia-tungsta-titania/sepiolite catalyst for SCR of NOx

被引:17
作者
Santos, A
Bahamonde, A
Avila, P
GarciaOchoa, F
机构
[1] CSIC,INST CATALISIS & PETR QUIM,E-28049 MADRID,SPAIN
[2] UNIV COMPLUTENSE MADRID,FAC CIENCIAS QUIM,DEPT INGN QUIM,E-28040 MADRID,SPAIN
关键词
diffusion coefficient (effective); selective catalytic reduction; monolithic catalyst; V-W-Ti/sepiolite; pore model; percolation model;
D O I
10.1016/0926-3373(95)00056-9
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
Experimental measurement of the effective diffusion coefficient for a vanadia-tungsta-titania/sepiolite catalyst, as employed for SCR of NOx, was carried out using a chromatographic technique in a packed column (under inert conditions) employing helium as carrier and nitrogen, argon and oxygen as tracers. Measurements were carried out at temperatures 298 and 473 K with particle sizes 0.4 and 0.5 mm. The values obtained for D-e are from 0.6 10(-6) to 0.94 . 10(-6) for the gas tracers and temperature range employed. Adsorption constant for the gas tracers above quoted have been also determined giving values of K-a around 1.3, thus, a light adsorption strength existed. Because D-e depends on the gas temperature and composition, different structure models for the solid have been applied to calculate from D-e the corresponding structural parameters: tau (in pore models) or Z (in percolation model), which only depends on the solid structure and can be employed for other gases and temperatures. The tau values obtained from the bundle pore model (around 3) are smaller than calculated applying the cross linked pore model (tau between 5 and 6). The coordination number, Z, has a meaningless value when catalyst is analyzed as unimodal (Z < 3). On the other hand, if the experimental pore size distribution was taken into account Z yields appropriate values were between 5 and 6.
引用
收藏
页码:299 / 314
页数:16
相关论文
共 42 条
[1]   RATE PARAMETERS FOR ADSORPTION OF CO2 IN BEDS OF CARBON PARTICLES [J].
ANDRIEU, J ;
SMITH, JM .
AICHE JOURNAL, 1980, 26 (06) :944-948
[2]   INFLUENCE OF THE BINDER ON THE PROPERTIES OF CATALYSTS BASED ON TITANIUM VANADIUM-OXIDES [J].
AVILA, P ;
BLANCO, J ;
BAHAMONDE, A ;
PALACIOS, JM ;
BARTHELEMY, C .
JOURNAL OF MATERIALS SCIENCE, 1993, 28 (15) :4113-4118
[3]  
BAHAMONDE A, 1992, THESIS U COMPLUTENSE
[4]   DETERMINATION OF INTRAPARTICLE DIFFUSION-COEFFICIENTS IN CATALYST PELLETS - A COMPARATIVE-STUDY OF MEASURING METHODS [J].
BAIKER, A ;
NEW, M ;
RICHARZ, W .
CHEMICAL ENGINEERING SCIENCE, 1982, 37 (04) :643-656
[5]   DESIGN OF MONOLITH CATALYSTS FOR POWER-PLANT NOX EMISSION CONTROL [J].
BEECKMAN, JW ;
HEGEDUS, LL .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (05) :969-978
[6]   MEASUREMENT OF THE EFFECTIVE DIFFUSION-COEFFICIENT OF NITROGEN MONOXIDE THROUGH POROUS MONOLITH-TYPE CERAMIC CATALYSTS [J].
BEECKMAN, JW .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (02) :428-430
[7]   INFLUENCE OF PHOSPHORUS IN VANADIUM-CONTAINING CATALYSTS FOR NOX REMOVAL [J].
BLANCO, J ;
AVILA, P ;
BARTHELEMY, C ;
BAHAMONDE, A ;
ODRIOZOLA, JA ;
DELABANDA, JFG ;
HEINEMANN, H .
APPLIED CATALYSIS, 1989, 55 (01) :151-164
[8]  
Bosch H., 1986, CATAL TODAY, V2, P369, DOI DOI 10.1016/0920-5861(88)80002-6
[9]  
Broadbent S. R., 1957, P CAMBRIDGE PHIL SOC, V53, P629, DOI DOI 10.1017/S0305004100032680
[10]  
*EPA EPRI, 1991, JOINT S STAT COMB NO