The P6 PolyMixTM (P6) patented system solves an age-old problem that has been inherent with all dewatering systems. Mixing of suspended solids and polymer has been the weak link in the dewatering process. Thoroughly mixing of the polymer with the suspended solids in the slurry/sludge is required for optimal dewatering. The P6 PolyMix™ system solves the problem of inadequate mixing while saving polymer costs 25% to 50% and increasing cake solids 10% to 50%.
These dramatic improvements/benefits result by reorienting the polymer injection position to the suction side of our Boundary Layer Viscous Drag (BL-VD) sludge/slurry dewatering feed pump and eliminating the high shear mixer valves typically used.
The conventional location for injection of dilute neat polymer is downstream of the dewatering equipment’s feed pump. Belt Filter Presses (BFPs) and Gravity Belt Filters (GBTs) typically have a high shear mixer installed immediately after the polymer injection point or a flocculation tank with shear mixer paddles.
Polymer is a long chain molecule that needs to be “activated” by uncoiling the long chain molecules to allow more electrically charged spaces to attract the opposite charged suspended solids (SS). The solids and polymer chains are trapped on the porous dewatering belts as the water separates from the solids. The concentrated polymer chains are unwound by the dilute neat process and injected into the slurry fluid. However, the normal long polymer chain is mechanically sheared/broken by the turbulent mixer valve or mixer paddles into shorter chain molecules in an attempt to thoroughly mix the suspended solids with the electrically charged polymer chains. If long “unbroken” polymer chains can be maintained with thorough mixing of the suspended particles, less polymer is required to achieve equal dewatering and the longer chain polymers with attached sludge solids are easier to dewater resulting in higher cake solids for a given amount of polymer used.