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Table 1 BET and NH3-TPD results of Fe and Cr modified ZSM-5 catalysts Sample Rel.
Table 1 BET specific surface area, mesopore volume, percentage of oxygen, and capacitance of the analyzed nanotubes.
Those characteristics (MB adsorption: 608.9 mg g− 1, iodine adsorption: 1026.4 mg g− 1, phenol adsorption: 633.3 mg g− 1, BET surface area: 1292 m2 g− 1) were shown greater than those of a commercial activated carbon used in water treatment and those reported by other researchers studying activated carbon preparation from various solid wastes by steam activation method.
Table 1 BET surfaces areas, average pore diameters and pore volumes for the supports and prepared catalysts Sample Surface area (m2 g−1) Average pore diameter Pore volume (cm3 g−1) Silica support 148 203 0.75 Co/silica 59 182 – Alumina support 205 155 0.79 Co/alumina 132 132 0.42.
The physiochemical properties of calcined support, unpromoted and promoted catalysts are presented in Table 1; BET surface area, pore volume and pore size of calcined catalysts had smaller values than the support as a result of pore blockage by Ni metal particles.
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Table 1 BET-SA and pore volumes of gold catalysts on various oxide supports Entry Catalyst BET-SA (m2/g) Pore vol. of cat.
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