TiCl4
Chemical
- May 1, 2019
- 616
I am assisting a sister plant with debottle-necking production. They produce microsphere particles with a density of ~0.9 s.g. The particles also have a average particle size of 10-50 um. They currently use tall, skinny tanks (aspect ratio is ~1.5-1.8) after the spheres are created to thicken the tank (increasing solids from, say, 20-30% to 40-50%). They let the particles rise to the top over the course of 9-12 hours, then draw the relatively low-solids bottoms water until solids are in spec.
They only have a few of the thickening tanks, but the combination of throughput and different product grades means they have exceeded the capacity of the tanks - they often package these tanks into IBCs to allow for further thickening because they need the tank for an upcoming production run.
Thickeners are typically designed for settling solids, but the same principle for design should apply, correct? In this case, gravity will work against the buoyant force, but the particle should still have a rising rate. If I'm thinking about this properly, a wide and shallow thickener design should produce much higher throughput/lower thickening time than a tall/skinny thickener due to the lower travel distance you need for separation, correct?
Any tips on thickener design? Jar tests can give me rising rates for different products, but what other effects do I need to consider? Brownian motion? Other differences from general thickener design parameters?
They only have a few of the thickening tanks, but the combination of throughput and different product grades means they have exceeded the capacity of the tanks - they often package these tanks into IBCs to allow for further thickening because they need the tank for an upcoming production run.
Thickeners are typically designed for settling solids, but the same principle for design should apply, correct? In this case, gravity will work against the buoyant force, but the particle should still have a rising rate. If I'm thinking about this properly, a wide and shallow thickener design should produce much higher throughput/lower thickening time than a tall/skinny thickener due to the lower travel distance you need for separation, correct?
Any tips on thickener design? Jar tests can give me rising rates for different products, but what other effects do I need to consider? Brownian motion? Other differences from general thickener design parameters?