source : http://civil.eng.usm.my/awam07/sample%20paper.doc
Three types of coagulants were examined using standard jar test apparatus, i.e., aluminum sulphate (alum), ferric chloride (FeCl3) and ferrous sulphate (FeSO4). The effects of agitation speed, settling time, pH, coagulant dosages and temperature were exermined. At 300 rpm of rapid mixing and 50 rpm of slow mixing and 60 minutes settling time, higher removals of suspended solids (over 95%), colour (90%) and COD (43%) were achieved at pH 4 and 12. FeCl3 was found to be superior compared with other coagulants. At pH 4 and 12, fair removal of suspended solids was observed at reasonably lower amount of coagulant, i.e., 600 mg/L. However, about 2500 mg/L of coagulant was required to achieve good removals at pH 6. Better removals were achieved at higher temperature.
The coagulation-flocculation process was employed for the treatment of reactive dye wastewaters, with ferric chloride hexahydrate employed as the coagulant. The process was found to be very effective with a more than 99.5% colour removal. Typical representatives of monochlorotriazine reactive dyes, with azo and anthraquinone chromophores, were CI Reactive Red 45 and CI Reactive Green 8, which were chosen as the model dyes. In order to determine the optimum pH range and coagulant concentration, a series of jar tests was done. Further experiments were conducted using a square flocculation tank with turbine impeller applying rapid and slow mix operations. The optimisation of initial rapid mixing, which has an important role in the overall coagulation process efficiency, was carried out. The optimum combination of velocity gradient and time of rapid mix was suggested for reactive dye wastewater treatment. Sedimentation curves for both model dyes were also obtained.
FeCl3 was found to be generally superior to the other two coagulants in removing all the parameters.
FeCl3 at pH 4 (at a coagulant dosage of 600 mg/L) and pH 6 (at a coagulant dosage of 2500 mg/L).
exhibited better performance with 90% and 97% removals, respectively.
Table 2:Removal of suspended solids, colour and COD at different pH values and dosages of coagulants.
pH | Results | Suspended Solids | Colour | COD | ||||||
Alum | FeCl3 | FeSO4 | Alum | FeCl3 | FeSO4 | Alum | FeCl3 | FeSO4 | ||
4 | Optimum/ economical dosage (mg/L) | 600 | 600 | 600 | 600 | 600 | 600 | 600 | 600 | 600 |
Initial* concentration | 1106 | 1106 | 1068 | 6450 | 6460 | 7275 | 2660 | 2565 | 3320 | |
Final** concentration | 282 | 59 | 582 | 2554 | 626 | 5485 | 1862 | 1472 | 1291 | |
% Removal | 74.5 | 94.7 | 45.5 | 60.4 | 90.3 | 24.6 | 30 | 42.6 | 61.1 | |
6 | Optimum/ economical dosage (mg/L) | 2500 | 2500 | 2500 | 2500 | 2500 | 2500 | 2500 | 2500 | 2500 |
Initial* concentration | 983 | 786 | 878 | 7005 | 7100 | 7003 | 3015 | 2980 | 3066 | |
Final** concentration | 291 | 8 | 506 | 3159 | 249 | 5953 | 2204 | 1648 | 2422 | |
% Removal | 70.4 | 99 | 42.4 | 54.9 | 96.5 | 15 | 26.9 | 44.7 | 21 | |
12 | Optimum/ economical dosage (mg/L) | 600 | 600 | 600 | 600 | 600 | 600 | 600 | 600 | 600 |
Initial* concentration | 1106 | 932 | 1068 | 6460 | 6658 | 7270 | 3210 | 3565 | 3320 | |
Final** concentration | 90 | 52 | 197 | 2558 | 1738 | 2690 | 2793 | 2777 | 2825 | |
% Removal | 91.9 | 94.4 | 81.6 | 60.4 | 73.9 | 63 | 13 | 22.1 | 14.9 |