Micropore size distribution of activated carbons impregnated after carbonization

被引:8
作者
Alvim-Ferraz, MCM [1 ]
Gaspar, CMTB [1 ]
机构
[1] Univ Porto, Dept Engn, Dept Engn Quim, LEPAE, P-4100 Oporto, Portugal
关键词
almond shells; activated carbon; impregnation; micropore volume; Medek; nut shells; CoO; Co3O4; CATALYSTS; SELECTIVITY; TEMPERATURE; MOLYBDENUM; POROSITY; SURFACE;
D O I
10.1023/A:1024034517665
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Impregnated active carbons were prepared to be used as catalysts of complete oxidation, aiming the reduction of atmospheric emission of volatile organic compounds. The onversion efficiency is regulated by the catalyst dispersion in the porous structure where pollutants can access to be converted, which means that a good dispersion is required. Therefore, microporore size distribution has an important role on the catalyst efficiency, either because the access to the catalyst can be made through micropores, or because micropores can offer a significant deposition surface, if they are wide enough. When the impregnation is performed on the raw material or after activation, the micropore size distribution is already well studied. This paper aims to analyse that distribution when impregnation is performed after carbonization, because this knowledge is yet very scarce. Nut and almond shells were used as raw materials to prepare carbons impregnated with CoO and Co3O4. The comparison between the micropore size distributions was performed using Medek model. When impregnation is made after activation, it was concluded that, for both raw materials, the catalysts block part of the initial microporous structure, leading to a decrease in micropore volume and to an increase of the mean equivalent radius. When impregnation step is conducted after carbonization, the total micropore volume can increase or decrease in relation to the non-impregnated carbons, depending on the catalyst distribution and type of carbonized support. Nevertheless, all the carbons analysed showed that impregnation after carbonization increases micropore volume of wider micropores.
引用
收藏
页码:47 / 55
页数:9
相关论文
共 15 条
[1]  
BRADLEY PR, 1994, CARBON, V32, P845
[2]   Comparison of three active carbons using LSER modeling: prediction of their selectivity towards pairs of volatile organic compounds (VOCs) [J].
Burg, P ;
Fydrych, P ;
Bimer, J ;
Salbut, PD ;
Jankowska, A .
CARBON, 2002, 40 (01) :73-80
[3]   The characterization of an active carbon in terms of selectivity towards volatile organic compounds using an LSER approach [J].
Burg, P ;
Fydrych, P ;
Abraham, MH ;
Matt, M ;
Gruber, R .
FUEL, 2000, 79 (09) :1041-1045
[4]   Effects of surface characteristics of activated carbons on VOC adsorption [J].
Chiang, YC ;
Chiang, PC ;
Chang, EE .
JOURNAL OF ENVIRONMENTAL ENGINEERING-ASCE, 2001, 127 (01) :54-62
[5]   Low temperature complete combustion of methane over Ag-doped LaFeO3 and LaFe0.5Co0.5O3 perovskite oxide catalysts [J].
Choudhary, VR ;
Uphade, BS ;
Pataskar, SG .
FUEL, 1999, 78 (08) :919-921
[6]   Interactions between molybdenum and activated carbons on the preparation of activated carbon-supported molybdenum catalysts [J].
de la Puente, G ;
Centeno, A ;
Gil, A ;
Grange, P .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 1998, 202 (01) :155-166
[7]   Influence of the impregnation order of molybdenum and cobalt in carbon-supported catalysts for hydrodeoxygenation reactions [J].
Ferrari, M ;
Delmon, B ;
Grange, P .
CARBON, 2002, 40 (04) :497-511
[8]   PREPARATION OF ACTIVATED CARBON FOR AIR-POLLUTION CONTROL [J].
FERRAZ, MCA .
FUEL, 1988, 67 (09) :1237-1241
[9]  
Ferraz MCMA, 1999, FUEL, V78, P1567
[10]   Palladium catalysts on activated carbon supports - Influence of reduction temperature, origin of the support and pretreatments of the carbon surface [J].
Gurrath, M ;
Kuretzky, T ;
Boehm, HP ;
Okhlopkova, LB ;
Lisitsyn, AS ;
Likholobov, VA .
CARBON, 2000, 38 (08) :1241-1255