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    Liquid-solid mixing often requires the deconstruction of agglomerated solids, by suspending particles in the mixture then destabilizing bulks of solid material. An example of this process occurs in the mixing of concrete, where solutes, cement and sand, are mixed with the solvent and water to create a malleable yet self-hardening product.

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    23/02/2016· Although you can use just about any tank design for blending water-like liquids, the tank geometry determines the placement and number of industrial mixer(s) for effective blending. As an example, for a typical miscible liquid blending application, you can’t place one industrial mixer close to the end of a long, horizontal cylindrical mixing tank (Figure 1) and expect to

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    Severe or catastrophic damage to the mixer occurs when the mixer operates at or near critical speed in air, a condition that exists when the liquid is drained from the tank and the impeller passes through the liquid interface. This condition creates large forces with very little damping and is called the draw-off condition.

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    Impeller-typemixing equipmentrepresentsthelargestcategoryofgeneralpurpose mixing equipment for fluid processing applications. From the process view of impeller-type equipment, an impeller, usually composed of blades mounted to a central hub and rotated by a drive shaft, pushes and moves the material to be mixed.

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    Flocculant mixing tank is a kind of a stirring machine for high efficiency thickener designed for adding flocculant, the impeller is specially designed. The principle of equipment is through the flow driven by the rotation of the impeller in the slurry tank, the liquid can be fully mixed flocculant in the thickener concentration system operation mixing and storage purposes.,It is a high

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    A tank with baffles will be able to rotate to convert the radial-flow impellers rotational motion into vertical motion to displace collected solids. Solid suspension or solid to liquid mixing, often viewed as a high energy cost process, SPX FLOW industrial mixers can be designed to meet specified process needs. Large volumetric flow is recommended for solid suspension, however, high shear, high flow-number

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