Microcolumn studies of dye adsorption onto manganese oxides modified diatomite.
The method described here cannot fully replace the analysis of large columns by small test columns (microcolumns). The procedure, however, is suitable for speeding up the determination of adsorption parameters of dye onto the adsorbent and for speeding up the initial screening of a large adsorbent collection that can be tedious if a several adsorbents and adsorption conditions must be tested. The performance of methylene blue (MB), a basic dye, Cibacron reactive black (RB) and Cibacron reactive yellow (RY) was predicted in this way and the influence of initial dye concentration and other adsorption conditions on the adsorption behaviour were demonstrated. On the basis of the experimental results, it can be concluded that the adsorption of RY onto manganese oxides modified diatomite (MOMD) exhibited a characteristic "S" shape and can be simulated effectively by the Thomas model. It is shown that the adsorption capacity increased as the initial dye concentration increased. The increase in the dye uptake capacity with the increase of the adsorbent mass in the column was due to the increase in the surface area of adsorbent, which provided more binding sites for the adsorption. It is shown that the use of high flow rates reduced the time that RY in the solution is in contact with the MOMD, thus allowing less time for adsorption to occur, leading to an early breakthrough of RY. A rapid decrease in the column adsorption capacity with an increase in particle size with an average 56% reduction in capacity resulting from an increase in the particle size from 106-250 microm to 250-500 microm. The experimental data correlated well with calculated data using the Thomas equation and the bed depth-service time (BDST) equation. Therefore, it might be concluded that the Thomas equation and the BDST equations can produce accurate predication for variation of dye concentration, mass of the adsorbent, flow rate and particle size. In general, the values of adsorption isotherm capacity obtained in a batch system show the maximum values and are considerably higher than those obtained in a fixed-bed.
Al-Ghouti
M A
MA
Royal Scientific Society, Industrial Chemistry Centre, P.O. Box 1438, Al-Jubaiha 11941, Jordan. mghouti@rss.gov.jo
Khraisheh
M A M
MA
Ahmad
M N
MN
Allen
S J
SJ
D000327:Adsorption; D002712:Chlorides / Q000737:chemistry; D004396:Coloring Agents / Q000737:chemistry*; D007692:Diatomaceous Earth / Q000737:chemistry*; D017895:Manganese Compounds / Q000737:chemistry; D008751:Methylene Blue / Q000737:chemistry; D010316:Particle Size; D012972:Sodium Hydroxide / Q000737:chemistry; D013997:Time Factors; D014865:Waste Disposal, Fluid / Q000379:methods; D014874:Water Pollutants, Chemical / Q000737:chemistry*; D018508:Water Purification / Q000379:methods
D002712:Chlorides; D004396:Coloring Agents; D017895:Manganese Compounds; D014874:Water Pollutants, Chemical; D012972:Sodium Hydroxide; D007692:Diatomaceous Earth; C033787:diatomite; C025340:manganese chloride; D008751:Methylene Blue