2. Examples of mixing plant calculations
2.1 Vessel with proximity mobile for discontinuous operation
Determine the geometrical and operating characteristics of a stirrer capable of homogenizing a viscoelastic rheofluidifying pasty medium in a 0.8 m 3 reactor in 10 min, and keeping it isothermal. Extrapolation of this operation to a 12 m 3 reactor.
Properties of the pasty medium at process temperature: ρ = 1,000 kg · m -3 ; λ = 0.6 W · m -1 · K -1 ; c p = 4,180 J · kg -1...
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Examples of mixing plant calculations
Mixer environment
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