Sedimentation ( Settling ) Defination, Types, Design
- 1. Sedimentation Prof. Mrs. D. A. Latthe Assistant Professor Dr. J. J. Magdum College of Engineering , Jaysingpur
- 2. Settling Solid liquid separation process in which a suspension is separated into two phases – • Clarified supernatant leaving the top of the sedimentation tank (overflow). • Concentrated sludge leaving the bottom of the sedimentation tank (underflow).
- 3. Purpose of Settling • To remove coarse dispersed phase. • To remove coagulated and flocculated impurities. • To remove precipitated impurities after chemical treatment. • To settle the sludge (biomass) after activated sludge process / tricking filters.
- 4. Principle of Settling • Suspended solids present in water having specific gravity greater than that of water tend to settle down by gravity as soon as the turbulence is retarded by offering storage. • Basin in which the flow is retarded is called settling tank. • Theoretical average time for which the water is detained in the settling tank is called the detention period.
- 5. Types of Settling Type I: Discrete particle settling - Particles settle individually without interaction with neighboring particles. Type II: Flocculent Particles – Flocculation causes the particles to increase in mass and settle at a faster rate. Type III: Hindered or Zone settling –The mass of particles tends to settle as a unit with individual particles remaining in fixed positions with respect to each other. Type IV: Compression – The concentration of particles is so high that sedimentation can only occur through compaction of the structure.
- 6. Type I Settling Type I Settling • Size, shape and specific gravity of the particles do not change with time. • Settling velocity remains constant. • If a particle is suspended in water, it initially has two forces acting upon it: (1) force of gravity: Fg=rpgVp (2) the buoyant force quantified by Archimedes as: Fb=rgVp If the density of the particle differs from that of the water, a net force is exerted and the particle is accelaratd in the direction of the force: Fnet=(rp-r)gVp This net force becomes the driving force. Once the motion has been initiated, a third force is created due to viscous friction. This force, called the drag force, is
- 7. Stokes Flow • For laminar flow, terminal settling velocity equation becomes: v=( ρp- ρ )*g.d2 18µ • which is known as the stokes equation.
- 8. Factors affecting sedimentation Several factors influence the process of sedimentation in a sedimentation tank, affecting the settling of particles in water. These include: Particle Size and Density • Larger and denser particles tend to settle more rapidly than smaller and less dense particles. The characteristics of suspended particles in the water play a significant role in sedimentation. Flow Velocity • The rate at which water flows through the sedimentation tank affects the settling time of particles. Lower flow velocities allow for better settling, while higher velocities may hinder the process. Temperature • Warmer temperatures generally reduce the viscosity of water, affecting settling rates. Colder water tends to have higher viscosity , potentially slowing down the sedimentation process.
- 9. Depth of Sedimentation Tank • The depth of the tank influences the distance particles must travel before settling. Deeper tanks may provide more time for particles to settle, improving sedimentation efficiency. Design and Shape of Tank • The design and shape of the sedimentation tank, including the presence of baffles, weirs, and other flow control structures, can impact the flow pattern and settling efficiency. Inlet Water Quality • The quality of the incoming water, including its turbidity and the concentration of suspended particles, directly affects the sedimentation process. Higher turbidity levels may require additional settling time. Chemical Coagulants • The addition of coagulants or flocculants to the water can
- 10. pH Level • The pH level of the water can influence the charge on particles, affecting their ability to coagulate and settle. Optimal pH conditions for sedimentation may vary based on the specific treatment requirements. Detention Time • The duration of time water spends in the sedimentation tank, known as the detention time, is critical. Adequate detention time allows particles to settle, and insufficient time may lead to incomplete sedimentation. Tank Loading Rate • The rate at which water is introduced into the sedimentation tank, known as the loading rate, can impact the settling efficiency. Proper loading rates ensure optimal settling conditions. Up flow Velocity • In the case of flow sedimentation tanks, the velocity of water moving upward against settling particles influences their removal. Control of this velocity is crucial for effective sedimentation.
- 11. Types of Settling Tanks • Sedimentation tanks may function either intermittently or continuously. • The intermittent tanks also called quiescent type tanks are those which store water for a certain period and keep it in complete rest. • In a continuous flow type tank, the flow velocity is only reduced and the water is not brought to complete rest as is done in an intermittent type. • Settling basins may be either long rectangular or circular in plan. • Long narrow rectangular tanks with horizontal flow are generally preferred to the circular tanks with radial or spiral flow.
- 12. Long Rectangular Settling Basin • Long rectangular basins are hydraulically more stable, and flow control for large volumes is easier with this configuration. • A typical long rectangular tank have length ranging from 2 to 4 times their width. The bottom is slightly sloped to facilitate sludge scraping. • A slow moving mechanical sludge scraper continuously pulls the settled material into a sludge hopper from where it is pumped out periodically.
- 13. A long rectangular settling tank can be divided into four different functional zones: Inlet zone: Region in which the flow is uniformly distributed over the cross section such that the flow through settling zone follows horizontal path. Settling zone: Settling occurs under quiescent conditions. Outlet zone: Clarified effluent is collected and discharge through outlet weir. Sludge zone: For collection of sludge below settling zone.
- 14. Inlet and Outlet Arrangement • Inlet devices: Inlets shall be designed to distribute the water equally and at uniform velocities. A baffle should be constructed across the basin close to the inlet and should project several feet below the water surface to dissipate inlet velocities and provide uniform flow; • Outlet Devices: Outlet weirs or submerged orifices shall be designed to maintain velocities suitable for settling in the basin and to minimize short-circuiting. Weirs shall be adjustable, and at least equivalent in length to the perimeter of the tank. However, peripheral weirs are not acceptable as they tend to cause excessive short-circuiting.
- 15. Weir Overflow Rates • Large weir overflow rates result in excessive velocities at the outlet. • These velocities extend backward into the settling zone, causing particles and flocs to be drawn into the outlet. • Weir loadings are generally used upto 300 m3 /d/m. It may be necessary to provide special inboard weir designs as shown to lower the weir overflow rates.
- 16. Circular Basins • Circular settling basins have the same functional zones as the long rectangular basin, but the flow regime is different. • When the flow enters at the center and is baffled to flow radially towards the perimeter, the horizontal velocity of the water is continuously decreasing as the distance from the center increases. • Thus, the particle path in a circular basin is a parabola as opposed to the straight line path in the long rectangular tank. • Sludge removal mechanisms in circular tanks are simpler and require less maintenance.
- 17. Parameters of Sedimentation Tank Design • To design a Sedimentation tank following elements require consideration: • Overflow velocity • Detention period • Flow through velocity • Dimensions of the tank • Sludge zone depth • Efficiency
- 18. Design Details • Detention period: for plain sedimentation: 3 to 4 h, and for coagulated sedimentation: 2 to 2.5 h. • Velocity of flow: Not greater than 30 cm/min (horizontal flow). • Tank dimensions: L:B = 3 to 5:1. Generally L= 30 m (common) maximum 100 m. Breadth= 6 m to 10 m. Circular: Diameter not greater than 60 m. generally 20 to 40 m. • Depth 2.5 to 5.0 m (3 m). • Surface Overflow Rate: For plain sedimentation 12000 to 18000 L/d/m2 tank area; for thoroughly flocculated water 24000 to 30000 L/d/m2 tank area. • Slopes: Rectangular 1% towards inlet and circular 8%.
- 19. Overflow velocity, also known as surface loading rate, is the volume of water applied per unit time per unit horizontal surface area. It must be less than the settling velocity of particles to ensure proper settling within the sedimentation tank.
- 20. Flow Through Velocity • Flow through velocity (V) is the speed of water as it travels from the inlet to the outlet of the sedimentation tank. • The allowable flow-through velocity in the tank is 0.005m/s. The formula for flow- through velocity is • V = Discharge/area = Q / (BxH).
- 21. Detention Period • The detention period, or detention time, is the time taken by water to travel from the inlet to the outlet of the sedimentation tank. • The allowable detention period in the tank is 4 to 8 hours. • The formula for detention time is Detention Time = Volume of tank/discharge = V/Q.
- 22. Dimensions of Sedimentation Tank • The basin dimensions, including length, breadth, and depth, are derived from the volume of the tank and overflow velocity. The area of the tank is calculated as A = Volume of water/overflow velocity. The breadth of the sedimentation tank should be 10 to 12 meters, the length should be at least 4 times the breadth, and the depth should range from 3 to 4.5 meters.
- 23. Sludge Zone Depth • The sludge zone depth is used to collect settled particles and is provided when sludge removal is manual. • Generally, it is limited to 0.8 to 1.2 meters.
- 25. Thank You