| Wastewater treatment has assumed a different | | | | rectangular and the latter circular. |
| dimension today against the backdrop of the danger | | | | In a rectangular tank, sewage enters continuously at |
| of running out of fresh water. Wastewater is | | | | one end and passes at the other end, generally over |
| sewage, storm-water and water that have been | | | | a weir. Sludge is removed manually into |
| used for various purposes around the community. | | | | sludge-digestion tanks. The scumformed at the |
| Most communities generate wastewater from both | | | | surface is removed by the mechanical scraper with |
| residential and nonresidential sources. | | | | the aid of a second blade called skimmer, through a |
| Unless properly treated, wastewater can harm public | | | | scum trough. |
| health and the environment. | | | | In the case of a circular or upward-flow tank, |
| Here I have discussed about removing the solids | | | | sewage enters at the center, rises vertically to be |
| from wastewater. How can we remove the settling | | | | drawn off by flowing over a peripheral weir arranged |
| solids from the wastewater? | | | | at the surface. Such tanksare particularly designed to |
| Simple. Thru a settling tank. It comprises of the | | | | make use of the principle of flocculation whereby, |
| following units: | | | | small colloidal particles are agglomerated into bulky |
| (a) Sedimentation tanks: either plain or chemical | | | | wooly masses, which are more easilysettled as |
| precipitation | | | | sludge on the bottom of the tank. |
| (b) Septic (Imhoff) tanks | | | | Mechanical scrapers collect the sludge, concentrating |
| (c) Sludge digestion tanks | | | | it towards the center, from where it is removed for |
| **Sedimentation tanks** | | | | further treatment. The effluent flowing over the |
| This is carried out with the objective to remove | | | | outlet weir is collected in an outlet pipe for further |
| suspended mineral and organic matter from sewage | | | | treatment. |
| after the wastewater has been subjected to pass | | | | When only raw sewage is to be treated in these |
| through screens and grit chamber. These are the | | | | tanks, they may be generally termed as primary |
| units in which sedimentation is brought about. The | | | | settling tanks or primary clarifiers. |
| lighter organic sewage solids, which settle in the | | | | While when a sewage that has received secondary |
| sedimentation tanks, are termed as sludge, while the | | | | treatment, as in trickling filters or aeration tanks, is to |
| sewage that has been partially clarified by the settling | | | | be treated in them, then they may be called as |
| out of the solids is known as the effluent. Both | | | | secondary settling tanks or secondary clarifiers. |
| sludge and effluent should be further treated in order | | | | **Design criteria for primary sedimentation tank** |
| to make them stable and unobjectionable. | | | | As with the sedimentation tanks in water supply, the |
| The settlement of the solids may either be caused | | | | capacity is determined by the volume of |
| by gravity or by aggregation or flocculation of | | | | sewage-flow and the required detention period. |
| sewage-particles. If the coagulating chemicals are not | | | | (i) detention period: 1 to 3 hours. Longer periods |
| added in the sewage, the tanks are referred as plain | | | | result in higher efficiency than shorter periods but too |
| sedimentation tanks. whereas, if chemicals are used | | | | long a period induces septic conditions and should be |
| for the purpose of bringing the finer suspended and | | | | avoided. |
| colloidal solids into masses of large bulk, thus | | | | (ii) velocity of flow: about 30 cm square/min. |
| hastening the settlement process, these are then | | | | (iii) surface loading: it may be noted that the overall |
| known as chemical precipitation tanks. The chemicals | | | | range of surface loading between 30,000 to 50,000 l |
| used are alum, lime, ferric chloride, ferric sulfate, | | | | m / day is in conformity with that used in case of |
| chlorinated copper etc. | | | | horizontal flow and vertical flow sedimentation tanks. |
| **Types of sedimentation tanks** | | | | (iv) liquid depth of mechanically cleaned settling tanks |
| Sedimentation is accomplished either in horizontal-flow | | | | should not be less that 2.1 m. And for the final clarifier |
| or vertical-flow tanks. The former are usually | | | | for activated sludge, not less than 2.4 m. |