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An overview of various purification techniques is given <strong>in</strong> the follow<strong>in</strong>g sections. The description of techniques used <strong>in</strong> prote<strong>in</strong><br />

purification <strong>in</strong> the upcom<strong>in</strong>g sections has been kept short and some m<strong>in</strong>ute details have been skipped <strong>in</strong> order to keep the chapter concise.<br />

Fractionation of prote<strong>in</strong>s <strong>in</strong> solution<br />

Almost <strong>in</strong>variably, the target prote<strong>in</strong> is obta<strong>in</strong>ed <strong>in</strong> aqueous solution together with several undesirable prote<strong>in</strong>s impurities. The<br />

fractionation techniques may provide a way to remove at least some of the impurities while reduc<strong>in</strong>g the bulk of the sample. Although<br />

fractionation does only lead to a very partial purification, it generally precedes the high resolution techniques. In this way, a crude sample<br />

is partially purified and its volume is reduced to make it suitable to be processed further by more sophisticated methods. Depend<strong>in</strong>g upon<br />

the properties of the target prote<strong>in</strong>, one of the follow<strong>in</strong>g methods may be used for fractionation.<br />

Fractionation by precipitation: This method utilizes the property of the differential solubility of prote<strong>in</strong>s under different conditions<br />

as well as conditions which allow aggregation of prote<strong>in</strong>s. The precipitation may be enforced by alter<strong>in</strong>g the buffer composition. The<br />

precipitated prote<strong>in</strong> may be separated from other simply by low speed centrifugation. One of the follow<strong>in</strong>g methods may be used to<br />

achieve this objective:<br />

a. Salt fractionation: High ionic strength promotes prote<strong>in</strong> precipitations. With <strong>in</strong>creas<strong>in</strong>g ionic strength, prote<strong>in</strong>s beg<strong>in</strong> to <strong>in</strong>teract<br />

via hydrophobic patches on their surface, as prote<strong>in</strong>s and salt compete for the residual water. This leads to formation of aggregates and<br />

the precipitation of prote<strong>in</strong>s. The phenomenon is termed as “Salt<strong>in</strong>g out” of prote<strong>in</strong>s. Different prote<strong>in</strong>s would precipitate at different salt<br />

concentrations. Ammonium sulfate is used as the salt of choice, s<strong>in</strong>ce it preserves prote<strong>in</strong> activity and promotes precipitation at lower<br />

concentrations than other salts. Other salts may give low ionic strength (e.g. NaCl, KCl), have solubility problems (e.g. Na 2<br />

SO 4<br />

) or may<br />

cause damage to prote<strong>in</strong> structure. Increas<strong>in</strong>g amount of ammonium sulfate is added to the extract, with <strong>in</strong>termittent centrifugation<br />

steps. These stepwise precipitations are referred to as ammonium sulfate “cuts”. The presence of target prote<strong>in</strong> is checked <strong>in</strong> these cuts<br />

and an appropriate cut is determ<strong>in</strong>ed where the major portion of target prote<strong>in</strong> is concentrated. Pre-calculated tables are available to<br />

f<strong>in</strong>d out the amounts of solid ammonium sulfate to be added to a known volume <strong>in</strong> order to obta<strong>in</strong> the desired percentage saturation.<br />

b. Isoelectric precipitation: Apart from ionic strength, the solubility of prote<strong>in</strong>s also depends on pH. As the pH approaches the<br />

pI of a given prote<strong>in</strong> the net charge on that prote<strong>in</strong> gets closer to zero, and weak electrostatic attractive forces lead to aggregation<br />

and precipitation. Lower<strong>in</strong>g ionic strength, or addition of solvent, promotes these <strong>in</strong>teractions. Although, solubility is m<strong>in</strong>imal at the<br />

isoelectric po<strong>in</strong>t, the <strong>in</strong>crease <strong>in</strong> ionic strength <strong>in</strong>creases the solubility even at the isoelectric po<strong>in</strong>t (This effect is called “salt<strong>in</strong>g <strong>in</strong>” of<br />

prote<strong>in</strong>s).<br />

c. Solvent precipitation: The mechanism of solvent fractionation is reduction of availability of water for prote<strong>in</strong> solvation (i.e. a<br />

reduced water activity) which causes the precipitation of the prote<strong>in</strong>. It tends to be more effective at pI which suggests that the mechanism<br />

may be similar to that <strong>in</strong> isoelectric precipitation. The precipitation may be achieved by add<strong>in</strong>g water-soluble organic solvents such as<br />

ethanol or acetone. The concentration of solvent required depends on the type of prote<strong>in</strong> and usually ranges between 5 to 60% (v/v). S<strong>in</strong>ce<br />

the denatur<strong>in</strong>g effect of solvents <strong>in</strong>creases with temperature, solvent fractionation is generally carried out around 0°C. The method has<br />

been extensively used <strong>in</strong> the past but nowadays only done <strong>in</strong> few specific cases. The ma<strong>in</strong> disadvantage of the method is the denaturation<br />

of prote<strong>in</strong>s due to non-polar solvents. However, if the prote<strong>in</strong> of <strong>in</strong>terest is known to be stable <strong>in</strong> these conditions, the method may be<br />

worthwhile to use s<strong>in</strong>ce it will remove many of unwanted prote<strong>in</strong>s that are sensitive to solvents.<br />

d. Selective denaturation: Contam<strong>in</strong>ant prote<strong>in</strong>s <strong>in</strong> isolated cases can be selectively denatured by heat, extremes of pH, and organic<br />

solvents. These treatments may be carried out if the prote<strong>in</strong> of <strong>in</strong>terest is stable towards one or more of these conditions. However, the<br />

treatment may result <strong>in</strong> chemical modification of the desired prote<strong>in</strong>.<br />

It is important to note that whole of the prote<strong>in</strong> of <strong>in</strong>terest may not come <strong>in</strong> a s<strong>in</strong>gle fraction. Many times, some of the prote<strong>in</strong> has to<br />

be sacrificed <strong>in</strong> order to get a better elim<strong>in</strong>ation of impurities.<br />

Ultra filtration: Dialysis, that employs a semi permeable membrane made from cellulose, is frequently used for desalt<strong>in</strong>g purposes.<br />

The prote<strong>in</strong> is reta<strong>in</strong>ed <strong>in</strong> the dialysis bag while the salt moves out. If the membrane has larger pores that also allow small prote<strong>in</strong>s to move<br />

out while reta<strong>in</strong><strong>in</strong>g the larger ones, such membranes can be used for prote<strong>in</strong> fractionation. S<strong>in</strong>ce dialysis speed is a function of molecular<br />

mass, the movement of prote<strong>in</strong>s through dialysis tub<strong>in</strong>g would be <strong>in</strong>significant. Ultrafiltration, on the other hand, uses such membranes<br />

and employs pressure to force the sample through. Membranes rang<strong>in</strong>g from 10kD to 100kD molecular weight cutoffs are commercially<br />

available. The method is not very efficient due to significant loss of sample, but may be useful <strong>in</strong> certa<strong>in</strong> specific cases.<br />

In order to <strong>in</strong>crease the process<strong>in</strong>g potential and the specificity of membrane filtration, aff<strong>in</strong>ity ultrafiltration concept was <strong>in</strong>troduced.<br />

Aff<strong>in</strong>ity ultrafiltration follows the pr<strong>in</strong>ciple that<br />

a. When the target prote<strong>in</strong> and impurities are free <strong>in</strong> a solution pass via the ultrafiltration membrane.<br />

b. Whereas, when a macro-ligand is bound to the target prote<strong>in</strong>, the resultant is a membrane-reta<strong>in</strong>ed complex.<br />

After the target prote<strong>in</strong> b<strong>in</strong>ds to the macroligand, the impurities are washed away. Dissociation of the target prote<strong>in</strong> from macroligand<br />

can be performed by provid<strong>in</strong>g suitable conditions.<br />

Solid Phase Extraction (SPE)<br />

Solid Phase Extraction (SPE) is method that uses a solid phase and a liquid phase to isolate one type of analyte from others based<br />

on physic-chemical properties. It is generally used to concentrate and/or clean up a sample before us<strong>in</strong>g a chromatographic or other<br />

analytical method. Solid-phase extractions use the same type of stationary phases as are used <strong>in</strong> liquid chromatography (discussed <strong>in</strong><br />

later sections).<br />

SPE uses the aff<strong>in</strong>ity of solutes dissolved or suspended <strong>in</strong> a liquid phase (the mobile phase) for a solid phase (the stationary phase)<br />

OMICS Group eBooks<br />

007

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