Quantities of ammonium sulfate required to reach given degrees of saturation at 20°C .
Purification of protein attracts the scientists’ attention toward science in 1926, as Somnar started purification and crystallization of urease from yeast. As years go forward, protein purification strategies updated from using dextrose passing through DEAE-cellulose and ended by affinity chromatography. In this chapter we will describe some of the concepts and the differences between traditional and novel purification methods, in order to point out how a researcher can start the protein purification techniques. Different fundamental purification steps from plant sample will be discussed in this chapter including isolation, concentration, ion exchanger, and affinity chromatography, as well as the important additives that a researcher should add in order to gain a high purification fold.
- ion exchanger
- gel filtration
- affinity chromatography
Purification is an intrinsic objective for profound and exact portrayal for an objective protein, a target protein. As scientists assume that proteins are responsible for bad and good roles throughout everyday life, in this manner we ought to apply more endeavors to definitely comprehend proteins’ structure and characters. This objective cannot be achieved else we acquired a highly purified protein which is unfortunately usually present in crowed with different protein communities.
Distinctive fundamental purification steps from plant sample will be discussed in this chapter including isolation of chloroplasts and mitochondria from leaves as well as from plant tissues rich in phenolic compounds. Meanwhile, we cannot ignore purification of protein from microorganisms. Diverse types of affinity chromatography will be also talked about in this chapter. Perusing can discover informative topics, which will urge them to experience protein purification methodology.
This chapter portrays contingent techniques which are previously or now utilized in the purification of proteins from planta. In particular biochemists have devoted effort to finding convenient methods for protein purification in case they are aiming to obtain a precise characterization and dive inside the target protein. Much advancement has been made, utilizing a lot of partiality systems. Especially, proteins as biomicromolecules differ in their chemical and physical properties. The physical properties demand special techniques for studying, for example, mass spectroscopy, gel filtration, ion exchanger chromatography, electrophoresis, and chromatofocusing, while the chemical properties include the composition, covalent and non-covalent bonds, and solubility.
2. Extraction of protein from plant and yeast
It is impossible to obtain a pure plant protein by using a single-step protocol of purification, as plant tissues contain a wide range of proteins and have rigid cellulosic cell wall and phenolic compound which may cause protein degradation.
The extraction process starts with utilizing a known and appropriate weight of fresh or frozen plant sample under liquid N2. Homogenize this lot in a prechilled mortar with suitable volume of extraction buffer (3 x of the sample). The extraction buffer type and its pH are distinctive to the sample nature. Some additives should be added to the extraction buffer to improve the obtained extract quality. These additives include:
Phenylmethylsulfonyl fluoride (PMSF, dissolved in very small amount of propanol just before extraction) to inhibit protease
Flavin compounds (FAD)
Dithiothreitol (DTT), to preserve the sulfhydryl group
EDTA, as chemical chelator especially with phosphate buffer
Sodium fluoride to inhibit phosphatase
Polyphenylpyrovate (PVP) 25 gm/k gm fresh weight of sample, which is an insoluble compound and binds to phenolic compound present in the sample, the obtained compound discarded by centrifugation
30% glycerol, which may help to stabilize some highly labile proteins
Antibiotic such as Hibitane, usually used in protein extracted from rhizomes or underground plant parts in general
Filter the homogenate with nylon mush, then centrifuge at 10,000 g for 10 min using cooling centrifuge. Repeat the process of extraction and centrifugation three times to ensure complete extraction of all proteins in the tissue. Nearly a similar technique was followed in extraction of Rubisco from wheat leaves , protein from
In the case of a microorganism, e.g., yeast, a Yeast Protein Extraction Buffer Kit may be used . This buffer is based on organic buffering agents, which utilize mild nonionic detergents, and a proprietary combination of various salts and agents to enhance extraction and stability of proteins. A ready-to-use Zymolyase preparation is also provided.
3. Concentration of crude extract
3.1 Ammonium sulfate precipitation
To concentrate or reduce the total volume of crude extract, solid ammonium sulfate was added to the crude extracts to bring the final concentration to 70% (w/v) or follow up Table 1 to choose alternative concentration. After complete dissolving the added solid ammonium sulfate, the mixture was allowed to stand at 4°C for 24 h, and the precipitate was collected by centrifugation at 10,000 g for 10 min using cooling centrifuge. The precipitated proteins were dissolved in the least amount of extraction buffer. To get rid of excess ammonium ions, dialysis was carried out against the same buffer (see Figure 1).
3.2 Fractional precipitation with acetone
The optimum precipitation range for the particular protein fraction is between 37.5 and 50% (v/v). Appropriate and known volume of cruse protein extract is chilled in an ice-salt bath. For each 1 ml of protein solution, add 0.60 ml of acetone (dropwise with constant stirring). After addition of acetone is completed, continue stirring for 10 min with constant control of temperature. The developed precipitate is collected by centrifuging the acetone-protein mixture at 3000
4. Ion-exchange chromatography
4.1 Principles of chromatography
When a sample is applied to any two-phase system (e.g., liquid-liquid, liquid-solid), a molecule may partition between the two phases. With partition coefficient ,
K = Cs/Cm
where C is sample concentration in separation phase (s) and in mobile phase (m). When a mixture of several components is applied to such two-phase system, each component of the mixture will have its own individual partition coefficient.
4.2 Components of liquid chromatography
The chromatography system has two components: one is buffer (represents the mobile phase), and the other is hydrated polymers. Buffers should be degassed and filtered before using, especially in the case of high-resolution chromatography. It pumped from a reservoir onto the column. In FPLC and HPLC, high-precision pumps drive mobile phase through the system. The solid phase should be mechanically stable, chemically inert, and widely ranged in their type, efficiency, and application. Table 2 shows some of the widely used stationary phases; all of them are commercially attainable packed columns.
By the beginning of the chromatographic separation method, the loaded sample is eluted from the column using the mobile phase. This may be achieved in three ways:
Continuous flow elution (mobile phase composition and flow rate remain constant).
Batch flow elution (the adsorbed sample is selectively eluted by using a range of mobile phase) and stepwise introduction of different mobile phases varied in pH, polarity, and salt concentration.
Gradient elution (the adsorbed material separated by two or more mobile phase compositions) is continuously varied.
The chosen way for elution is depending on the behavior of sample components on the stationary phase (Figure 2).
4.3 Types of ion chromatography and elution ways
Amino acid sequence determines the net charge of protein. Ion-exchange chromatography separates proteins either on the basis of their charge type (cationic or anionic) or charge strength (e.g., strongly anionic from weakly anionic). Like most column chromatography techniques, ion-exchange chromatography requires a stationary phase which is usually composed of insoluble, hydrated polymers, such as cellulose, dextran, and Sephadex.Table 2 indicates some of the commonly used ion exchangers . The main concept is that the anion like a negatively charged protein exchanges with chloride ions, while the cation like a positively charged protein exchanges with potassium or sodium ions. This process can later be reversed by washing with chloride ions in the form of NaCl or KCl solution. After loading the crude solution that contained the target protein, some of the proteins are bounded; however, others are not. Elution is carried out by washing with buffer which contained an electrolyte. During elution step, weakly bound proteins are firstly removed, followed by more strongly bound proteins. The opposite is correct for the cation, which like a positive charged protein exchanges with sodium or potassium ion. As an example, in the purification of uricase from soybean, DEAE-cellulose which is an anion exchanger is used. DEAE-cellulose column was prepared and pretreated as recommended by Peterson and Sober . Column was equilibrated with 50 mM phosphate buffer pH 7.5, 1.0 mM EDTA, and 10.0 M mercaptoethanol. The protein was eluted with a stepwise gradient from 0.0 to 0.5 M KCL solutions prepared in the same buffer used in column equilibration. This column was successfully used for purification of uricase extracted from leaves and root nodules of soybean . It is worth to measure uricase activity and protein content in each eluted fraction. Soluble protein was routinely determined spectrophotometrically at 280 nm. Separated peaks may be collected by fraction collector. For more perfection, some researcher may also use 205–220 nm to ensure not missing proteins or peptides which have poor aromatic residues. Elution profile is represented by constructing a plot between detector signal and the retention of sample contents (eluted fractions vs. OD280).
5. Gel filtration chromatography
5.1 For protein purification
Shape and mass of proteins are unique. Gel filtration is also known as size exclusion in which the stationary phase is made up of a gel consisting of beads, which have narrow and fixed size pores (Figure 3). So, the proteins below the size pore will diffuse out from the column. Each type of gel filtration has certain cutoff value. By loading the sample, the smaller components pass through the bed and retain faster than the larger ones. The greatest component in the size is eluted freely from the column just after the void volume. Hence, the fraction range will depend uniformly on the population of beds in the column.
Sephacryl S-100 and Sephadex G-100 columns were used extensively for this step. These columns were equilibrated with extraction buffer such as 50 mM phosphate buffer pH 7.5, 1.0 mM EDTA, and 10.0 mM mercaptoethanol. The protein was eluted with the same buffer. Enzyme activity and/or protein content should be assayed for each of the eluted fractions.
5.2 For mass determination
The relative native molecular mass of purified proteins was determined after fractionation on Sephadex G-100 (23 x 1.5 cm) equilibrated with 50 mM phosphate buffer pH 7.5, 1.0 mM EDTA. The marker proteins of known low molecular mass used such as:
aprotinin (6500), cytochrome c (12,400), carbonic anhydrase (30,000), and albumin bovine serum (66,000) Da. The void volume (Vo) was determined with dextran blue (2,000,000) Da. Purified enzyme samples of 2.0 ml volume contained about 2 mg protein/ml was applied to the same column. The protein was eluted from the column with the same buffer used for equilibration. At a flow rate of 1 ml/2.5 min, 2.5 ml fractions were collected. A calibration curve was constructed by plotting log molecular masses versus V/Vo, where (V) was the elution volume and (Vo) was the void volume.
5.3 For removal of low molecular components
Gel filtration may be used in routine way to remove salts. Sephadex G-10 and Sephadex G-25 are commonly used to desalt samples, and hence, it makes the exchange process more rapid and minimizes the dilution of protein sample.
6. Affinity chromatography
The principle of this technique is to fix a small molecule which is called “ligand” on the column stationary phase just before sample loading (Figure 4). Affinity is bispecific recognition and distinguishing of biomolecules. Figure 5 shows a schematic diagram of the steps involved in an affinity-based separation .
There are many types of this technique, the most used of them are:
6.1 Substrate or inhibitor affinity
In this technique an enzyme will be recognized by its substrate or inhibitors or cofactors. As a result of the highly specific nature of this ligand to the target protein, only this protein will be bound to the stationary phase and hence purify with high quality. On the other hand, the other protein molecules will go through the chromatography system. At the end, the target protein will be eluted from the ligand. In the case of closely related proteins or isozymes, a variation of this approach should be applied to create an affinity gradient, where the concentration of ligand is gradually increasing in the mobile phase. Hence, each isozyme is unique in its Km’s for the substrates or Ki’s for the inhibitors.
6.2 Metal affinity
In this technique, metals are binding to a stationary phase, and metal-binding regions of proteins bind to this ligand. The most common metal used in this technique is Cu, Zn, Ca, Ni, and Fe which are covalently bound to iminodiacetic acid (IDA) and then to the stationary phase, i.e., agarose or silica. A critical problem faced by the researchers during using this technique is that some amino acids, i.e., histidine, cysteine, and tryptophan, may be gradually leached from the stationary phase due to the weakness of interaction with IDA. Elution of the target protein is usually displayed by decreasing pH gradient.
Immunoaffinity chromatography (IAC) is a type of liquid chromatography that uses a highly specific binding of antibodies for an antigen which is representing the target protein. The application of IAC includes immune-extraction, immune-depletion, chromatographic immunoassays, and post-column immune-detection . These different applications are coming from the tight and selective interactions between antigens and antibodies. Versatile applications of IAC by using either immobilized antigens or antibodies have been used on purification of wild-type and recombinant mutant amidases from
6.4 Fusion tag protein purification
When proteins are expressed recombinantly, additional amino acids, a functional domain, or a whole protein is often appended to aid in the purification. A standout among the most widely recognized combination labels is His, which is a short chain of six to nine histidine buildups (known as the 6xHis or polyHis tag). Application of 6xHis in purification gives 1000-fold of binding specificity than that of IDA-agarose . The later will bind to metal ions such as nickel or cobalt. Another fusion tag, glutathione S-transferase (GST), which binds tightly to reduced glutathione (GSH), is mostly used. Unlike His and GST tags, most of these other tags are called epitope tags because they require specific antibodies (e.g., immobilized anti-HA antibody) for purification. Epitope labels are irregularly used as it is generally far reaching contrasted with straightforward ligand media, for example, nickel or glutathione agarose. In this way, antibody combination labels are broadly accessible for utilization of single-step liking cleaning.
6.5 Heme-tagged protein
The addition of affinity tags to the amino- (N) or carboxyl- (C) terminus of a target protein for purification purposes can dramatically reduce the amount of preparation time, reduce the number of purification steps needed, and increase the yield of pure protein [19, 20, 21, 22]. Recently, the combination of heme tag-HIS has been found more convenient as the target protein was visible and easy to be detected. For this purpose, as the heme chromophore grants the fusion protein with an intense red or red brown color, visible detection significantly reduces the time and effort associated with protein expression and handling during all purification and chromatographic steps. Heme tags are composed of a heme-binding peptide (HBP) that is linked to the heme chromophore by two stable thioether bonds . HBPs are used for HIS affinity purification. HBPs are typically small, consisting of 14–20 amino acid residues. The critical element of a HBP is a Cys-X-X-Cys-His (CXXCH) heme-binding motif within the sequence, with X representing any amino acid residue . The basis of the heme-tag-HIS affinity purification method is the reversible coordination between the heme-iron open coordination site and the side chain of histidine immobilized on Sepharose beads. Later on, the target protein can be eluted from the column using an imidazole-containing buffer, a low pH (≤5) buffer, or a high pH (≥8) buffer.
6.6 Avidin-biotin systems
Biotin or vitamin H is a small molecule (MW 244.3) that is present in humble amounts in all living cells. The acidic side of this vitamin can be incorporated with various reactive groups. Once biotin is attached to a molecule, the molecule can be captured for detection, immobilization, or affinity purification using conjugates or supports based on avidin or streptavidin proteins, which bind strongly and explicitly to the biotin group. Native and recombinant derivatives of avidin and streptavidin proteins are promptly accessible in a wide assortment of altered, labeled, and immobilized forms. The “avidin-biotin system” has been adapted for use in many kinds of research applications for detection or purification. As the avidin-biotin affinity interaction is so strong, therefore it is usually impractical to elute biotinylated targets that have been captured to immobilize avidin or streptavidin support. However, modified versions of biotin labeling reagents have been developed, such as cleavable biotin, iminobiotin, and desthiobiotin; these provide readily reversible interactions with streptavidin, making them useful tools for soft-release applications.
6.7 Cellulose binding model
Cellulose binding module (CBM) has been distinguished as a potential tool for the fast and easy assembling of recombinant proteins [21, 25]. CBM is an attractive affinity tag for protein purification because of its high capacity and specific adsorption to cellulose. In addition, it can be efficiently adsorbed to cellulose in most buffers and eluted under non-denaturing conditions. There are many advantages of this technique such as low cost, appropriate physical properties, applicable for most proteins, and high stability in the presence of buffers. All of these make it an ideal matrix for large-scale affinity. Moreover, cellulose is easily procured and safe for many pharmaceutical and human purposes. The method of purification of the recombinant protein with a CBM3 tag was developed in both
6.8 Affinity precipitation
A novel affinity precipitation developed by Arnold and Chen  was very promising. One-step binding and precipitation resulted in >95% recovery yield directly from crude extract and a 22.7-fold purification, giving a specific activity of 420 U/mg. The soybean peroxidase isolated using this affinity precipitation meets or exceeds the quality specifications of reagent grade products. The molar ratio of ligand to target fucosylated protein is key for the recovery yield.
Affinity precipitation is an alternative approach with the potential to overcome the challenges associated with affinity chromatography, as it retains the specific interaction of affinity ligand with the protein of interest while avoiding column operation .
As there is no restricted catalog for purification steps of proteins to follow it up, the researcher should design its own protocol according to the aimed target and the final quality that is being looked for. Gel filtration and ion exchangers are suitable for broad mass and low-cost aim. However, affinity chromatography with its versatile types is the only technique for highly purified and selective protein yield. All purification techniques have the same major steps that include equilibration of a column, adsorption of a sample, washing to remove unbound materials, and elution of bound protein target protein and ended with regeneration of the media.