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


A brief overview of your bioseparation topic (be sure to put its name in '''bold''' in the first sentence) and the scope of the article goes here.Also see [[CZ:How to start a new article]]
==Types of Centrifuges==


The following list of sections may serve as a loose guideline for developing the body of your article. Before deciding to follow it, take a look at some other articles on subjects like your own. You may like their structure better and if so, adopt it.  
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.


The works cited in references 2-5 are all fake (and are borrowed from another Eduzendium template); their purpose is to serve as a formatting model for your own citations.
===Laboratory Centrifuges===


==The Process==
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.


Here, go into more detail about the process.
For more information:
[[Gas Centrifuge]]
[[Sucrose Gradient Centrifuge]]
[[Micro Centrifuge]]
[[Ultra Centrifuge]]
[[Clinical Centrifuge]]
[[Bench top Centrifuge]]


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


This section should describe the invention and development of the process. If the section runs long, divide it into chronological subsections, for example:
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.  


===Invention and early development===
====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.


This subsection should provide some historical context for the development of your process, describe its invention, and name some early developers and/or applications.<ref>John Q. Sample, ''Chromatography, a new analytical tool''. City: Publisher, 1885.</ref>
====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.  


===Recent developments===
===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.


This section should discuss new developments in the field. Don't hesitate to drop in brief mentions of processes or features you don't intend to discuss in depth.  By so doing you are planting seeds of articles which will eventually be developed by others.<ref>"New Directions for Flocculation," American Flocculation Society. 2006. Retrieved July 21, 2009 from [http://www.amflocsoc.org/future_devs.html http://www.amflocsoc.org/future_devs.html]</ref>
For more information:
[[NASA]]
[[Gravitron|http://www.ride-extravaganza.com/intermediate/gravitron/]]


==Design and Operation==
==Equations Governing Centrifuges==
Use lots of subsections here as you describe various aspects of the process .<ref>First Author and Second Author, "Electro-absorpto-crossflow-sedimento-extractofractionation," ''Journal of Superspecialized Bioseparation Arcana'' 36:2 (2010) pp. 86-52.</ref>


==Applications==
===Sedimentation Velocity (V<sub>g</sub>)===
*The speed at which a particle falls out of solution in Earth’s gravitational field.


This section should discuss how the process is used in practice.<ref>"Major Success for Bioprocess Fractionation," ''Anytown Daily News'', January 1, 2015, p. A6.</ref>
<math>V<sub>g</sub>=(πd<sub>p</sub>∆ρg)/18μ</math>


==Examples==
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)


If you have used a lot of equations in your article, this may be a good place to show an example of how they are used. See the article on the Antoine Equation for an example.
===RCF: “Relative Centrifugal Force” or G’s===
*The strength of the centrifugal acceleration  in multiples of gravitational acceleration
 
<math>RCF= (r*(2πω))<sup>2</sup>/g</math>
 
Where: r – radius of the centrifuge (cm), ω – angular velocity (cm*rad/s), g – gravitational constant (cm/s<sup>2</sup>)
 
===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>)===
*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==
<references/>
<references/>

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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, 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.

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.

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.

Failed to parse (SVG (MathML can be enabled via browser plugin): Invalid response ("Math extension cannot connect to Restbase.") from server "https://wikimedia.org/api/rest_v1/":): {\displaystyle V<sub>g</sub>=(πd<sub>p</sub>∆ρg)/18μ}

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

Failed to parse (syntax error): {\displaystyle RCF= (r*(2πω))<sup>2</sup>/g}

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.

Failed to parse (SVG (MathML can be enabled via browser plugin): Invalid response ("Math extension cannot connect to Restbase.") from server "https://wikimedia.org/api/rest_v1/":): {\displaystyle Q_ret=V<sub>g</sub>*∑}

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:

Failed to parse (SVG (MathML can be enabled via browser plugin): Invalid response ("Math extension cannot connect to Restbase.") from server "https://wikimedia.org/api/rest_v1/":): {\displaystyle ∑=(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>)}

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 ∑=(2πn(r<sub>o</sub><sup>3</sup>-r<sub>i</sub><sup>3</sup> ) ω<sup>2</sup>)/(3gtan(θ))}

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