This impeller can be fabricated to fit almost any shaft diameter and comes standard in 316 Stainless Steel but 304 Stainless Steel versions are also available 304 Stainless Steel Sawblades can be hardened for abrasive mixing applications Various surface finishes are available Power Number Np = Flow Number Nq =
Get Priced —the diameter of the impeller m f —the friction coefficient H —the height of the liquid level in the mixer m NP —power number NP0 —power number without baffle NPmax —power number with baffle r —the rotating rate r s − 1 nb —the number of the baffle nP —the number of the impellers P —required power W Re —Reynolds number
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Get PriceThe power associated with an impeller is related to four primary factors Impeller geometry Impeller diameter Impeller rotational speed Fluid properties of the material being mixed The relationship of these components can be expressed in the following equation Power = Np n3 d5 sg K Np impeller power number geometry factor
Get PriceThe four main dimensionless numbers used to study mixing are based on seven key variables the power delivered P the fluid s density ρ the shaft speed N the impeller diameter D the impeller pumping rate Q the fluid s viscosity µ and the tank diameter T These variables form the dimensionless numbers
Get PriceThe power number P 0 is therefore constant In this region mixing power is proportional to the cube of the rotation speed and to the fifth power of impeller diameter It is proportional to the fluid density but insensitive to viscosity In high power industrial mixers more than one type of impeller may be used in the same unit
Get PricePower Number Np = Flow Number Nq = Our folding impeller is the most robust industrial duty collapsible propeller on the market beware of cheap styles out there For mixing in Totes and Drums this impeller folds to fit in 2″ NPT bungs and opens up when the mixer is turned on
Get PriceHydrofoil PF3 The most common of mixing impellers PF3 Hydrofoil Impeller provides excellent pumping ability with a strong axial flow While useful in most applications this design excels in thinner fluids that are susceptible to settling and provides the MOST pumping per unit of torque input Great for low shear applications
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Get PriceFolding impellers allow a manufacturer to get a large impeller in a closed container due to their unique collapsible blade design Our 4 and 7 folding impellers can fit through a 2 NPT fitting and our 10 12 and 14 folding mixer impellers can fit through a 6 NPT like that on an IBC Tote Some efficiency is sacri
Get PriceThe reactor was designed for L total and L working volume the power rating and power delivery were and hp respectively The operating conditions for the reactor to attain
Get PriceTable 1 Key Dimensions in Mobius Power MIX Mixer Min Sampling Volume liters Max Volume liters Diameter inches Diameter mm H/D at nominal volume Impeller Diameter mm Impeller Wing Height mm Impeller Power Number Motor Size Max RPM 100 25 110 523 120 23 1/3 HP 380 200 40 220 654 120 23 1/3 HP 380
Get PriceMixing power number The power number depends on impeller type and mixing Reynolds number Figure 5 shows this relationship for six commonly used impellers Similar plots for other impellers can be found in the Hterature The functionality between and Re can be described as cc Re in laminar regime and depends on p
Get PriceThe power number for a mixing impeller primarily depends upon the impeller geometry The impeller type number of blades blade angle width and shape etc define the value of the turbulent power number Impeller design also substantially influences power number behavior as a function of Reynolds number in the transition and laminar range
Get PriceGiven the same impeller width and impeller diameter as previous example however the impeller type is pitched blade type with six blades The power number would be N P = [ 12/58 / 1/5 ] x = [2] Determine the power number N P at process and operating conditions Power number is a function of Reynolds number and impeller geometry
Get PricePropeller turbine mixer design calculator solving for impeller diameter given Reynolds number fluid dynamic viscosity Reynolds number < 10 mixing constant laminar flow power requirement turbulent flow Reynolds number >10000 mixing constant turbulent flow fluid mass density rotation speed revolutions per second turbulent flow
Get PriceNumber of impellers = Maximum liquid height x average specific gravity / Diameter of tank The gap between two impellers = Liquid height / Number of impellers Most important parameters are diameter and length of agitator shaft and impeller diameter These are decided by process design calculations
Get PriceThe power number Np also known as Newton number is a commonly used dimensionless number relating the resistance force to the inertia force The power number has different specifications according to the field of application for stirrers the power number is defined as [1] with P power ρ fluid density
Get PriceSTEP 1 Calculate the power number of the agitator 2 STEP 2 Calculate the power number at actual process conditions 3 STEP 3 Calculate the motor power required for the agitator 4 STEP 4 Select the actual size of the motor 5 STEP by STEP example agitator power requirement calculation 6
Get PriceThe power number correlations for two stage referred to Design Handbook for Practical Subject of Chemical Engineering PartII Wang et al 2024 In this investigation the power number for double stage 4 PBT was twice the power number of single impeller Numerical method Computational grids The grids of tank domain and impeller domain were
Get PriceImpeller Technology Mixquip 61 02 4629 3050 sales Quote Request Mixquip Agitators Mixers Impeller Technology Applications About Us Learning Hub Contact Us Shop Online Impeller Technology Home Impeller Technology Power of Mixing The Impeller YOUR PROCESS MATTERS
Get PriceSingle Use Mixer s 500 ml CellMiscelatore 3200 CellMiscelatore Large CellMiscelatore Perfusion Ready CellRider For improved cultivation its better to know your Power Number Marine impeller design with typical Power Number Np ranging in a radial flow distribution setup operating directly in the media without circular
Get PriceReynolds number < 10 mixing constant laminar flow fluid dynamic viscosity rotation speed revolutions per second laminar flow impeller diameter laminar flow power requirement turbulent flow Reynolds number >10000 mixing constant turbulent flow fluid mass density
Get PriceMixing Impeller performance in stirred tanks Authors Richard K Grenville Philadelphia Mixing Solutions LLC An SPX FLOW Brand Jason J Giacomelli Philadelphia Mixing Solutions Ltd
Get PriceMentioning 1 Agitation is of vital importance and is widely used in many chemical processes Much research work has been done on the effect of agitation on suspending solids and dispersing gases in liquids [l 31 The main variable for the mechanical design of agitated vessels is the power requirement of the agitator Extensive work has been performed on impeller power numbers in agitated
Get PriceIn the case of axial flow impellers the power number also relates to the pumping number much like the relationship between lift and drag coefficients on an aircraft wing or propeller blade By focusing this basic discussion of the MI on turbulent mixing the turbulent impeller power numbers effectively are constant values for mixers operating
Get PriceFeatures Varying angle options optimize processes by changing the impeller diameter/tank ratio Maximizes flow with ability to add shear options Standard on the LIGHTNIN LFD Flocculator Improves results up to 40% vs conventional pitched blade turbines
Get PriceWhat is the power number for the impellers How to scale from 10L to 2000L Does the XDR s have the capability for a perfusion process What is the product contact material on the bag What is the maximum shear rate 1/s for a CHO process and how is it calculated What is the impeller material on the XDR s What is the size of the sparge disks
Get PriceNumber of impellers = 1 Mixing speed = 300 rpm Diameter of the Rushton turbine = 1 m Viscosity of the broth = Density of the broth = 1000 3 EduRev gives you an ample number of questions to practice The power required for agitation of non aerated medium in fermentation is conditions are as follows Fermentor
Get PricePropeller Turbine Mixer Design Calculator Wastewater Treatment Mixing Equations Solving for impeller diameter Inputs Reynold s number N R unitless fluid dynamic viscosity μ revolution per second n unitless liquid mass density ρ Conversions Reynold s number N R = 0 = 0 fluid dynamic viscosity μ = 0 = 0 newton second/meter^2
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