Centrifuge: Difference between revisions

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==Types of Centrifuges==
==Types of Centrifuges==


Centrifuges fall into three different categories based on size: laboratory, industrial, and human-sized.  Laboratory centrifuges are the smallest of the three and are primarily used for cell sedimentation and purification.  Industrial sized centrifuges are significantly larger than laboratory centrifuges and are utilized for large separation processes.  Yet the largest centrifuges are human-sized and are scientifically utilized by space agencies and biomedical research to simulate high gravity conditions.
Centrifuges fall into three different categories based on size: laboratory, process-scale, and human-sized.  Laboratory centrifuges are the smallest of the three and are primarily used for cell sedimentation and purification.  Industrial sized centrifuges are significantly larger than laboratory centrifuges and are utilized for large separation processes.  Yet the largest centrifuges are human-sized and are scientifically utilized by space agencies and biomedical research to simulate high gravity conditions.


===Laboratory Centrifuges===
===Laboratory Centrifuges===
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For more information:
For more information:
[[Gas Centrifuge]]
[[Gas Centrifuge]]
[[Sucrose Gradient Centrifuge]]
[[Sucrose Gradient Centrifuge]]
[[Micro Centrifuge]]
[[Micro Centrifuge]]
[[Ultra Centrifuge]]
[[Ultra Centrifuge]]
[[Clinical Centrifuge]]
[[Clinical Centrifuge]]
[[Bench top Centrifuge]]
[[Bench top Centrifuge]]


===Process Scale Centrifuges===
===Process Scale Centrifuges===


Biological and chemical processing plants use large-scale centrifuges for separation and sedimentation.  The two most common separation centrifuges are tubular bowl centrifuges and disk stack centrifuges.  
Biological and chemical processing plants use large-scale centrifuges for separation and sedimentation.  The two most common separation centrifuges are tubular bowl centrifuges and disk stack centrifuges. Large gas chromatography centrifuges are also used in Uranium purification.


====Tubular Bowl Centrifuge====
====Tubular Bowl Centrifuge====
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*The speed at which a particle falls out of solution in Earth’s gravitational field.  
*The speed at which a particle falls out of solution in Earth’s gravitational field.  


<math>V_g=(πd_p∆ρg)/18μ</math>
<math>V_g = \frac{\pi d_p \Delta\rho g}{18\mu}</math>


Where: d<sub>p</sub> - diameter of the particle (cm), ∆ρ – the difference in densities between the particle and the solvent (g/cm<sup>3</sup>), g – gravitational constant (cm/s<sup>2</sup>), μ - viscosity of the solvent (g/cm*s)
Where: d<sub>p</sub> - diameter of the particle (cm), ∆ρ – the difference in densities between the particle and the solvent (g/cm<sup>3</sup>), g – gravitational constant (cm/s<sup>2</sup>), μ - viscosity of the solvent (g/cm*s)
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<math>\ RCF = \frac{(r*(2\pi\omega))^2}{g} \,</math>
<math>\ RCF = \frac{r*(2\pi\omega)^2}{g} \,</math>


Where: r – radius of the centrifuge (cm), ω – angular velocity (cm*rad/s), g – gravitational constant (cm/s<sup>2</sup>)
Where: r – radius of the centrifuge (cm), ω – angular velocity (cm*rad/s), g – gravitational constant (cm/s<sup>2</sup>)
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*The speed at which the particle falls out of solution in the centrifuge
*The speed at which the particle falls out of solution in the centrifuge


<math>V<sub>r</sub>=V<sub>g</sub>*RCF</math>
<math>V_r = V_g*RCF</math>
 
===Retention Flow Rate (Q<sub>ret</sub>)===
*In an process scale centrifuge, the flow rate at which all the particles will sediment out of solution.
<math>Q_ret=V<sub>g</sub>*∑</math>
 
Where: V_g - sedimentation velocity (cm/s), ∑ - sigma factor (cm<sup>2</sup>)
 
===Sigma Factor (∑)===
 
*The operation constant representing the geometry and speed of the centrifuge.
 
====For Tubular Bowl Centrifuge:====
 
<math>∑=(πL(r<sub>o</sub><sup>2</sup>-r<sub>i</sub><sup>2</sup>) ω<sup>2</sup>)/gln(r<sub>o</sub>/r<sub>i</sub>)</math>
Where: L – length of the column (m), r<sub>o</sub> - outer radius of centrifuge (cm), r<sub>i</sub> - inner radius of centrifuge (cm), ω – angular velocity (cm*rad/s), g – gravitational constant (m/s<sup>2</sup>)
====For a Disk Stack Centrifuge:====
<math>∑=(2πn(r<sub>o</sub><sup>3</sup>-r<sub>i</sub><sup>3</sup> ) ω<sup>2</sup>)/(3gtan(θ))</math>
 
Where: ω – angular velocity (cm*rad/s), n – number of discs, r<sub>o</sub> - outer radius of disks (cm), r<sub>i</sub> - inner radius of disks (cm), θ - angle between disc and vertical (rad), g – gravitational constant (cm/s<sup>2</sup>)
 
==References==
<references/>
 
===Particle Velocity (V<sub>r</sub>)===
*The speed at which the particle falls out of solution in the centrifuge
 
<math>V<sub>r</sub>=V<sub>g</sub>*RCF</math>


===Retention Flow Rate (Q<sub>ret</sub>)===
===Retention Flow Rate (Q<sub>ret</sub>)===
*In an process scale centrifuge, the flow rate at which all the particles will sediment out of solution.
*In an process scale centrifuge, the flow rate at which all the particles will sediment out of solution.
<math>Q_ret=V<sub>g</sub>*</math>
<math> Q_ret = V_g*\Sigma</math>


Where: V_g - sedimentation velocity (cm/s), ∑ - sigma factor (cm<sup>2</sup>)
Where: V_g - sedimentation velocity (cm/s), ∑ - sigma factor (cm<sup>2</sup>)
Line 100: Line 77:
====For Tubular Bowl Centrifuge:====
====For Tubular Bowl Centrifuge:====


<math>=(πL(r<sub>o</sub><sup>2</sup>-r<sub>i</sub><sup>2</sup>) ω<sup>2</sup>)/gln(r<sub>o</sub>/r<sub>i</sub>)</math>
<math>\Sigma = \frac{(\pi L(r_o^2-r_i^2 ) \omega^2)}{g ln(r_o/r_i )} </math>
   
   
Where: L – length of the column (m), r<sub>o</sub> - outer radius of centrifuge (cm), r<sub>i</sub> - inner radius of centrifuge (cm), ω – angular velocity (cm*rad/s), g – gravitational constant (m/s<sup>2</sup>)
Where: L – length of the column (m), r<sub>o</sub> - outer radius of centrifuge (cm), r<sub>i</sub> - inner radius of centrifuge (cm), ω – angular velocity (cm*rad/s), g – gravitational constant (m/s<sup>2</sup>)
====For a Disk Stack Centrifuge:====
====For a Disk Stack Centrifuge:====
<math>=(2πn(r<sub>o</sub><sup>3</sup>-r<sub>i</sub><sup>3</sup> ) ω<sup>2</sup>)/(3gtan(θ))</math>
<math>\Sigma = \frac{2\pi n(r_o^3-r_i^3) ω^2}{(3g \tan(\theta)}</math>


Where: ω – angular velocity (cm*rad/s), n – number of discs, r<sub>o</sub> - outer radius of disks (cm), r<sub>i</sub> - inner radius of disks (cm), θ - angle between disc and vertical (rad), g – gravitational constant (cm/s<sup>2</sup>)
Where: ω – angular velocity (cm*rad/s), n – number of discs, r<sub>o</sub> - outer radius of disks (cm), r<sub>i</sub> - inner radius of disks (cm), θ - angle between disc and vertical (rad), g – gravitational constant (cm/s<sup>2</sup>)

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Centrifuge - a mechanical device that decreases sedimentation time through the use of centripetal acceleration.

Types of Centrifuges

Centrifuges fall into three different categories based on size: laboratory, process-scale, and human-sized. Laboratory centrifuges are the smallest of the three and are primarily used for cell sedimentation and purification. Industrial sized centrifuges are significantly larger than laboratory centrifuges and are utilized for large separation processes. Yet the largest centrifuges are human-sized and are scientifically utilized by space agencies and biomedical research to simulate high gravity conditions.

Laboratory Centrifuges

Laboratory Centrifuges are frequently used in various scientific protocols such as DNA and protein purification. The most common laboratory centrifuge is the bench top centrifuge because they are multipurpose and have removable rotors. Laboratory centrifuges can spin up to about 20,000 rpm.

For more information:

Gas Centrifuge

Sucrose Gradient Centrifuge

Micro Centrifuge

Ultra Centrifuge

Clinical Centrifuge

Bench top Centrifuge

Process Scale Centrifuges

Biological and chemical processing plants use large-scale centrifuges for separation and sedimentation. The two most common separation centrifuges are tubular bowl centrifuges and disk stack centrifuges. Large gas chromatography centrifuges are also used in Uranium purification.

Tubular Bowl Centrifuge

The tubular bowl centrifuge operates by allowing fluid to enter the bottom of the centrifuge and exit out the top. Particles separated from the centrifuge are collected on the side of the bowl and need to be cleaned after processing. Fortunately, the bowl is usually easy to remove and wash. Another application for the tubular bowl centrifuge is the separation of a light liquid from a heavy liquid because of the density difference.

Disk Stack Centrifuge

The disk stack centrifuge is fed from the top into a basin and the clarified liquid is removed from the top after passing through a series of disks. Similar to the tubular bowl centrifuge, the dense particles are captured on the side of the centrifuge. Some disk stack centrifuges have solid discharge valves that can clean the sides and prevent buildup.

Human-sized Centrifuge

Moving to a larger scale, human-sized centrifuges are used for high gravity training by NASA and entertainment value in carnival rides such as the Gravitron. Human sized centrifuges spin much slower than their smaller counter parts as sedimentation is undesired.

For more information: NASA http://www.ride-extravaganza.com/intermediate/gravitron/

Equations Governing Centrifuges

Sedimentation Velocity (Vg)

  • The speed at which a particle falls out of solution in Earth’s gravitational field.

Where: dp - diameter of the particle (cm), ∆ρ – the difference in densities between the particle and the solvent (g/cm3), g – gravitational constant (cm/s2), μ - viscosity of the solvent (g/cm*s)

RCF: “Relative Centrifugal Force” or G’s

  • The strength of the centrifugal acceleration in multiples of gravitational acceleration


Where: r – radius of the centrifuge (cm), ω – angular velocity (cm*rad/s), g – gravitational constant (cm/s2)

Particle Velocity (Vr)

  • The speed at which the particle falls out of solution in the centrifuge

Retention Flow Rate (Qret)

  • In an process scale centrifuge, the flow rate at which all the particles will sediment out of solution.

Where: V_g - sedimentation velocity (cm/s), ∑ - sigma factor (cm2)

Sigma Factor (∑)

  • The operation constant representing the geometry and speed of the centrifuge.

For Tubular Bowl Centrifuge:

Where: L – length of the column (m), ro - outer radius of centrifuge (cm), ri - inner radius of centrifuge (cm), ω – angular velocity (cm*rad/s), g – gravitational constant (m/s2)

For a Disk Stack Centrifuge:

Failed to parse (syntax error): {\displaystyle \Sigma = \frac{2\pi n(r_o^3-r_i^3) ω^2}{(3g \tan(\theta)}}

Where: ω – angular velocity (cm*rad/s), n – number of discs, ro - outer radius of disks (cm), ri - inner radius of disks (cm), θ - angle between disc and vertical (rad), g – gravitational constant (cm/s2)

References