and are key separation techniques that rely on particle settling. These processes exploit differences in , shape, and density to separate mixtures. Understanding the principles behind these methods is crucial for designing effective separation systems.
Calculations play a vital role in optimizing separation efficiency. From Stokes' Law to sigma theory, various equations help predict settling velocities and compare centrifuge performance. These tools enable engineers to design and select appropriate equipment for specific separation needs.
Principles and Processes
Principles of centrifugation and sedimentation
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Gravitational force drives sedimentation while powers centrifugation
Particle influenced by size, shape, density, fluid and density
Stokes' Law describes settling velocity of particles in laminar flow v=18μd2(ρp−ρf)g
Buoyancy opposes settling dependent on fluid density and particle volume
Drag force resists particle motion through fluid increases with settling velocity
Centrifugation vs sedimentation processes
Sedimentation uses gravity for slower separation suitable for larger particles (settling tanks)
Centrifugation employs centrifugal force for faster separation of smaller particles (disc stack centrifuges)
Centrifugation generally achieves higher separation efficiency
Sedimentation applied in wastewater treatment while centrifugation used in biotechnology
Design of centrifuges and settlers
Gravity settlers use rectangular or circular tanks with inclined plates to improve efficiency
Hydrocyclones have conical shape with tangential inlet for particle separation
Disc stack centrifuges contain series of conical discs for continuous high-throughput operation
Tubular centrifuges feature long narrow bowl for high-speed batch or semi-continuous processing
Decanter centrifuges use horizontal cylindrical bowl with screw conveyor for continuous solids discharge
Calculations for separation efficiency
Terminal settling velocity calculated using Stokes' Law (laminar) or Newton's Law (turbulent)
Centrifugal settling velocity given by vc=18μd2(ρp−ρf)ω2r
Sigma theory compares centrifuge performance to equivalent settling tank area
Separation efficiency determined by E=1−e−QvtA
Cut size represents particle size at which 50% separation occurs
Residence time affects separation efficiency calculated as volume divided by flow rate