Crossflow membrane filtration: Difference between revisions

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imported>Justin D. Finkle
imported>Justin D. Finkle
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==Typical Operation==
==Typical Operation==
===Dissolved Species===
===Dissolved Species===
As the feed flows across the membrane, dissolved molecules will be rejected by the membrane. When this occurs, a concentration gradient develops along the membrane where molecules are in higher concentrations than that of the solution.  Membranes with small enough pore sizes, such as those used in ultrafiltration, can even remove dissolved species and form a gel layer that impedes transmembrane flux (Shuler and Kargi).
===Suspended Species===
===Suspended Species===
===Concentration Polarization===
===Concentration Polarization===

Revision as of 20:43, 12 December 2010

Crossflow filtration is a term used to refer to a membrane filtration technique in which feed flows parallel to the membrane (Harrison, Todd and Rudge). It is typically characterized by having high tangential fluid velocity and a low velocity normal to the membrane. Crossflow filtration is used in many applications of downstream processing including food processing, pharmaceutical production, and cell separation.

Comparison with conventional filtration

In an ideal crossflow filtration system the flux of permeate through the membrane will reach a steady state. This allows for much easier continuous removal of the target material when compared with conventional filtration. In practical applications, though, a cake builds up along the membrane, increasing in thickness further down the filter, as shown on the diagram to the right.

Additionally, because the fluid flow is parallel to the membrane—rather than normal to it as in a conventional filtration system—shear along the membrane prevents continual cake buildup. This contributes to the easy and continuous removal of the target material and reduces the need for cake washing. Fouling of the membrane can still occur along with concentration polarization

Typical Operation

Dissolved Species

As the feed flows across the membrane, dissolved molecules will be rejected by the membrane. When this occurs, a concentration gradient develops along the membrane where molecules are in higher concentrations than that of the solution. Membranes with small enough pore sizes, such as those used in ultrafiltration, can even remove dissolved species and form a gel layer that impedes transmembrane flux (Shuler and Kargi).

Suspended Species

Concentration Polarization

Applications of crossflow filtration

Many different types of filtration exist that are specific to different particle sizes. Choosing the appropriate one depends on the target that is being selected for and the key impurities that will be removed. Different types of filters are shown in Figure 2 and include:microfiltration, ultrafiltration, nanofiltration, and reverse osmosis.

One particular type of crossflow membrane device is the hollow fiber membrane. This is commonly used in dialysis of human blood. In hollow fiber filter systems, the feed flow is run through many tiny hollow tubes and molecules are allowed to diffuse in and out normal to the fluid flow through the tubes.

Membrane fouling

Though fouling is significantly reduced in crossflow membrane systems, as compared with conventional filtration systems, it is still a problem. Depending on the type of filter used and the pore sizes, different problems can arise. Concentration polarization can become exacerbated by gel formation in ultrafiltration systems, and microfiltration of suspended particles can create thick cake layers that reduce transmembrane flux (Harrison, Todd and Rudge). Large, soft particles can adhere to the pores, smaller particles can clog pores, and precipitates can form on the pores all reducing the pore size available and reducing transmembrane flux. Types of pore plugging can be seen in Figure 3 to the left. Gel layer formation can sometimes be reduced by mechanical agitation (Shuler and Kargi).