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CHAPTER 9. AGITATION AND MIXING

CHAPTER 9. AGITATION AND MIXING

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    Diameter : D: mm: 400: 300: Equivalent Diameter : Teq = 4.V/π 1/3: mm: 400: 300: Scaling Exponent : n: 2: Shaft : N: rpm: 400: 300: Reynolds No. Re = D 2.N.ρ/μ: Tip : π.D.N: m/s: Flow Number : Nq: Pumping Rate : Q = Nq.N.D 3: m 3 /s: 400: 300: Power Number : Np: Power Drawn : P = Np.ρ.N 3.D 5: kW: 400: 300: Power/ Volume : P/V: kW / m 3: 400: 300: Froude Number : Fr = N 2.D/g:

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    The should never be run at full with the liquid level at the blade level. When the is run with the fluid in the vessel at approximately the same level as the blades, fluid flow can cause the shaft to “skate”, resulting in excessive stresses and runout in the seal area and upper end of the

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     · Increase in rate from 70 to 100 rpm for the helix type resulted in a more expressive increase for constant k 1S of 52%, increasing from 0.71 to 1.08 h −1, respectively. This makes 100 rpm preferable over 70 rpm

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    Agitation occurs when an impeller Adjusting the shaft height and/or angle allows mixing to occur throughout the profile of the slurry. A shaft can be inserted into a digester through the digester wall below the slurry level with a water-tight seal or through the gas-holder with gas-tight seal

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