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Introduction to Pharmaceutical Biotechnology, Volume 2 (Second Edition)
that the enzyme is retained, whereas the substrate and product molecules can easily pass through. During this procedure, also known as lattice entrapment, the enzyme (or cell) is not exposed against strong binding forces or structural distortions. During an immobilization process, the level of deactivation might be possible. This happens due to the uctuations in pH or temperature or the addition of solvents. The matrices employed for entrapment of enzymes include polyacrylamide gel, collagen, gelatin, starch, cellulose, silicone and rubber. Enzymes can be entrapped in numerous ways. There are different approaches to entrapping enzymes such as gel [33]orfiber entrapping [34, 35] and microencapsulation [36, 37].
4.6.6.1 Enzyme i nclusion in gels
This is achieved by enzyme entrapment inside gels (gure 4.4). The poly(vinyl alcohol) bearing styrylpyridinium groups (PVA-SbQ), a soluble pre-polymer bearing photo-cross-linkable group, has been used extensively to entrap enzymes, and numerous bioassays based on this immobilization matrix have been demonstrated [38, 39]. The sol–gel process was established on the capability to form solid metal or semi-metal oxides through the aqueous process of hydrolytically labile precursors. Enzymes can also be entrapped in an agarose gel [39]. In contrast to synthetic polymers, e.g. polyacrylamide, this matrix is biocompatible, nontoxic, provides a natural microenvironment to the enzyme and also offers adequate accessibility to electrons to shuttle between the enzyme and the electrode. The entrapment approaches are easy to perform, and allow the deposition of enzymes, mediators, and additives in the same sensing layer. Furthermore, the activity of the enzyme is conserved during the immobilization process, as the biological element is not altered [39]. Biosensors based on physically entrapped enzymes are frequently described by increased operational and storage stability.
Figure 4.4. Immobilization of enzymes by entrapment. (a) Inclusion in gels. (b) Inclusion in bers. (c) Inclusion in microcapsules.
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4.6.6.2 Enzyme i nclusion in fibers
Entrapment involves inclusion of an enzyme in a polymer network (gel lattice) such as an organic polymer, a silica sol–gel or a membrane device such as a hollow ber or a microcapsule. Entrapment requires the synthesis of the polymeric network in the presence of the enzyme. The last step involves cross-linking of enzyme aggregates or crystals, using a bifunctional reagent, to prepare carrier-free macroparticles [40]. The enzymes are trapped in the bers of the matrix.
4.6.6.3 Enzyme i nclusion in microcapsules
During this procedure enzymes are trapped inside a microcapsule matrix (gure 4.4). The hydrophobic forms of the matrix polymerize to yield a microcapsule containing enzyme molecules [41]. The major limitation for entrapment of enzymes is the leakage from the matrix. Most of the researchers suggested utilizing this method of entrapment for immobilization of whole cells. Entrapped cells can be used in large­scale production of amino acids such as l-isoleucine, l-aspartic acid, l-malic acid and hydroquinone [41].
4.6.6.4 Micro-encapsulation
Micro-encapsulation is a kind of entrapment in which spherical particles in a liquid or suspension are enclosed in a semipermeable membrane [42]. The membrane may be polymeric, lipoidal, lipoprotein-based or non-ionic in nature. The three steps of microencapsulation are:
Building superior membrane reactors.
Formation of the emulsion.
Stabilization of the emulsion to yield microcapsules [42].
Currently microencapsulation is employed for immobilization of enzymes and mammalian cells. For example, cultured pancreatic cells can be immobilized by microencapsulation; immobilized hybridoma cells have also been evidenced by this technique [43].
4.6.7 Covalent binding
Enzyme immobilization can be accomplished by formation of covalent bonds between the chemical groups of enzymes and the chemical groups of the support (gure 4.4). This procedure is extensively used. However, covalent binding is frequently linked with loss of some enzyme activity. Pretreatment (to form pre­activated support) of the inert support is typically required before it binds to an enzyme. The following are the common procedures of covalent binding. Immobilizations of proteins by procedures based on the formation of covalent bonds are among the most extensively used. A benet of these procedures is that, because of the stable nature of the bonds developed between enzyme and the matrix, the enzyme is not released into the solution upon use. However, in order to attain high levels of bound activity, the amino acid residues vital for catalytic activity must not be involved in the covalent linkage to the support; this may prove a challenging
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condition to accomplish in some cases. A simple method that occasionally increases the activity yield is to perform the coupling reacti on in the presence of substrate analogs [44]. Covalent methods for immobilization are used when there is a strict obligation for the absence of the enzyme in the product. An extensive range of reactions have been established depending on the functional groups accessible on the matrix [45 ]. Coupling procedures can generally be categorized in two main classes:
Activation of the matrix by addition of a reactive function to a polymer.
Alteration of the polymer backbone to synthesize an activated group.
The activation procedures are usually intended to make electrophilic groups on the support which, in the coupling step, react with the strong nucleophiles on the proteins. The basic principles governing the course of covalent coupling to the matrices are similar to those used for the chemical alteration of proteins. The most often used reactions include the following side chains of the amino acids: lysine (ε-amino group), cysteine (thiol group), and aspartic and glutamic acids (carboxylic group).
Cyanogen bromide activation: The inert support materials such as cellulose, sepharose and sephadex enclosing glycol groups are activated by CNBr, which at that time binds to enzymes and immobilizes them (gure 4.5).
Diazotation: A number of the support materials (aminobenzyl cellulose, amino derivatives of polystyrene, aminosilanized porous glass) are exposed to diazotation on treatment with NaNO
and HCI. They, in return, bind
2
covalently to tyrosyl or histidyl groups of enzymes (gure 4.5).
Peptide bond formation: Enzyme immobilization can also be achieved by the development of peptide bonds between the amino (or carboxyl) groups of the support and the carboxyl (or amino) groups of enzymes (gure 4.5). The support material is initially chemically treated to form active functional groups.
Activation by bi- or polyfunctional reagents: A number of reagents, e.g. glutaraldehyde, can be used to build bonds between the amino groups of the enzymes and the amino groups of the support (such as aminoethylcellu­lose, albumin, amino alkylated porous glass). This is represented in gure 4.6.
Figure 4.5. A general representation of the immobilization of enzymes by covalent binding.
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Figure 4.6. Immobilization of enzymes by covalent binding: (a) cyanogen bromide activation, (b) diazotation, (c) peptide bond formation and (d) activation by bifunctional agent.
4.6.8 Cross-linking
A characteristic feature of the immobilization of enzymes by cross-linking is the lack of a solid support. The enzyme molecules are immobilized by building cross-links between them, and by the participation of polyfunctional reagents. In fact, these reagents react with the enzyme and make bridges which further form the support to hold enzyme molecules (gure 4.7). There are a number of reagents used for cross­linking. These include glutaraldehyde, diazobenzidine, hexamethylene diisocyanate
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Figure 4.7. Immobilization of enzyme molecules by cross-linking.
and toluene di-isoth iocyanate. Glutaraldehyde is the most frequently used cross­linking reagent [38]. It successfully reacts with lysyl residues of the enzymes and nally yields a Schiffs base. The cross-links developed between the enzyme and glutaraldehyde are irreversible and can tolerate extreme pH and temperature. Glutaraldehyde cross-linking has been effectively utilized to immobilize a number of industrial enzymes such as glucose isomerase and penicillin amidase [38]. The method of cross-linking is very simple and cost-effective, but the drawback is that it includes the possibility of enzyme denaturation by the polyfunctional reagent.

4.7 Choice of immobilization technique

Selection of a particular procedure for immobilization of enzymes is based on a trial and error approach to select the perfect one. The enzyme catalytic activity, stability, regenerability and cost are the most important factors that decide a technique.
4.7.1 Immobilization of l-amino acid acylase
Japanese researchers [46] discovered the rst enzyme immobilized on a matrix, known as l-amino acid acylase. Later, a number of immobilization procedures were attempted by these researchers, but only three showed promising results. These were:
Covalent binding to iodoacetyl cellulose.
Ionic binding to DEAE-sephadex.
Entrapment with n polyacrylamide.
4.7.2 Stabilization of soluble enzymes
Enzyme stabilization is essential for any biomedical or industrial application of enzymes. In several applications, the objective is to deliver a prolonged active lifetime under normal environmental conditions with traditional substrates at low concentrations in buffered solutions [47]. However, as enzymes are being employed for more and more applications, there is a need to use them under extreme environmental conditions (i.e., high temperatures), in high substrate concentrations and in nontraditional solvent systems [47]. Certain enzymes cannot be immobilized
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as they should be used in soluble form, for example, enzymes used in liquid detergents, some diagnostic reagents and food additives. With the aid of a number of additives or by chemical modications these enzymes can be stabilized. The stabilized enzymes have longer half-lives, although they cannot be recycled. Several signicant procedures for enzyme stabilization are briey described in the following [47]:
Solvent stabilization: Some solvents at low concentrations stabilize the enzymes, whereas at high concentrations the enzymes become denatured, e.g. acetone (5%) ethanol (5%) can stabilize benzyl alcohol dehydrogenase.
Substrate stabilization: By adding substrates the active site of an enzyme can be stabilized, e.g. starch stabilizes α-amylase; glucose stabilizes glucose isomerase.
Stabilization by polymers: This type of stabilization can be achieved by the addition of polymers, such as gelatin, albumin and polyethylene, particularly at increased temperatures.
Stabilization by salts: Metalloenzymes stability of can be attained by supplementing salts, e.g. Ca, Fe, Mn, Cu and Zn. Proteases are commonly stabilized by the addition of calcium.
Stabilization by chemical modications: During this procedure, enzymes can be stabilized by appropriate chemical modications without loss of biological activity. There are different types of chemical modications:– Addition of polyamino side chains, such as polytyrosine.
– Acylation of enzymes by adding groups, e.g. acetyl, propionyl and
succinyl.
Stabilization by rebuilding: Ideally, enzyme stability is dependent on the hydrophobic interactions in the core of the enzyme. It was thus suggested that enzymes can be stabilized by increasing hydrophobic interactions. For this reason, the enzyme is initially unfolded and later rebuilt in one of the following ways (see gure 4.8):– The enzyme can be chemically treated (e.g. using urea and a disulde) and then refolded.
– The refolding can be done in the presence of low molecular weight
ligands.
– For certain enzymes, refolding at higher temperatures (around 50 °C)
stabilizes them.
Stabilization by site-directed mutagenesis: Site-directed mutagenesis has been fruitfully used to synthesize more stable and functionally more efcient enzymes such as subtilisin E.

4.8 Immobilization of cells

A single-step reaction procedure is suitable for the immobilization of an individual cell, but is not appropriate for multienzymes or for reactions demanding co-factors. During this procedure whole cells or cellular organelles can be immobilized, yielding a system which acts as a source for various enzymes, and hence is referred to as a multi-enzyme system. Furthermore, immobilized cells rather than enzymes are often favored even for single reactions, owing to the cost factor in isolating enzymes.
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Figure 4.8. Stabilization of an enzyme by refolding.
For those enzymes which are dependent on the spacial arrangement of the membrane for their activity, cell immobilization is ideal. There are several signicant applications of immobilized enzymes, for example, they are traditionally used for the treatment of sewage. The procedures used for the immobilization of cells are almost the same as those employed for the immobilization of enzymes, with appropriate modications. Techniques such as entrapment and surface attachment are fre­quently used. Gels, and to some extent membranes, are also used.
4.8.1 Immobilization of viable cells
By means of gentle immobilization it is possible to preserve the viability of the cells. These immobilized cells are mainly useful for fermentation. Occasionally, mamma­lian cell cultures are made to function as immobilized viable cells.
4.8.2 Immobilized non-viable cells
In most cases, immobilized non-viable cells are considered over enzymes or even viable cells. This is primarily because of the expensive isolation and purication procedures. An excellent example is the immobilization of cells producing glucose isomerase for the large-scale production of high-fructose syrup.
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4.8.3 Drawbacks of immobilizing eukaryotic cells
Prokaryotic cells (mainly bacterial) are generally used for immobilization. According to various reports it is also possible to immobilize eukaryotic plant and animal cells. Owing to the presence of cellular organelles, the metabolism of eukaryotic cells is slow. Consequently, for the large-scale production of biochem­icals, prokaryotic cells are considered. However, for the synthesis of complex proteins (e.g. immuno-globulins) and for proteins that experienced post-transla­tional modications, eukaryotic cells may be used.
4.8.4 The effect of immobilization on enzyme properties
Cell immobilization is often linked to modications in enzyme properties, partic­ularly the kinetic properties of enzymes. Some of these are as follows:
A considerable reduction in enzyme specicity. This may be because of conformational changes that take place when the enzyme becomes immobilized.
The kinetic constants (K
m
and V
) of an immobilized enzyme differ from
max
those of the innate enzyme. This is because of the conformational modica­tions of the enzyme which may further affect the afnity between the enzyme and substrate.
4.8.5 Immobilized enzyme reactors
Immobilized enzyme cells are exploited for large-scale production in the form of enzyme reactors [43]. They are generally of two types: batch reactors and continuous reactors. The frequently used enzyme reactors are depicted in gure 4.9.
Batch reactors. In these types of reactors, the immobilized enzymes and substrates are employed, and the reaction is allowed to start under constant stirring. As the reaction is finished, the product is isolated from the enzyme (typically by denatura- tion). Soluble enzymes are frequently used in batch reactors. It is somewhat challenging to isolate the soluble enzymes from the products, therefore, there is the drawback of their reuse. Special procedures have been developed for the recovery of soluble enzymes, which may occasionally result in loss of enzyme activity [48].
Stirred tank reactors. The most modest form of batch reactor is the stirred tank reactor (gure 4.9). It is composed of a reactor xed with a stirrer that permits good mixing, and a suitable temperature and pH control. However, in this system there may be loss of some enzyme activity. The basket reactor is a modication of the stirred tank reactor. In this method, the enzyme is retained over the impeller blades. Both the stirred tank reactor and basket reactor have a well-mixed ow pattern [48].
Plug ow type reactors. These reactors are alternatives to ow pattern type reactors. The ow rate of uids can be regulated by a plug system. Plug ow type reactors are available in the form of packed-bed or uidized-bed reactors (gure 4.9). These reactors are mainly useful when ow type reactors furnish insufcient product formation. Moreover, plug ow reactors are also benecial for obtaining kinetic data on the reaction systems [48].
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Figure 4.9. Immobilized enzyme/cell reactors: (a) batch stirred tank reactor, (b) packed-bed reactor, (c) uidized-bed reactor and (d) continuous stirred tank reactor.
Continuous reactors. During this procedure the substrate is supplemented con­stantly, whereas the product is eliminated. Immobilized enzymes can also be employed for continuous operation. Continuous reactors have certain merits over batch reactors. These entail regulation over the product formation, suitable operation of the system and easy automation of the whole procedure. There are two main types of continuous reactors: the continuous stirred tank reactor (CSTR) and plug reactor (PR) [49]. A schematic depiction of CSTR is shown in gures 4.9 and 4.10. CSTR is suitable for good quality product formation.
Membrane reactors. A number of membranes with an array of chemical compositions can be used. Polysulfone, polyamide and cellulose acetate are the most often used materials for membranes. The biocatalysts (enzymes or cells) are usually retained on the membranes of the reactor. The substrate is added into reactor while the product passes out. Good mixing in the reactor can be attained using a stirrer (gure 4.10). In a continuous membrane reactor, the biocatalysts are held on membrane layers over which substrate molecules are passed (gure 4.10). In a recycle model membrane reactor, the contents, i.e., the solution containing enzymes, co-factors, and substrates, along with freshly released product, are recycled by using a pump (gure 4.10). The product passes out of the system and can be recovered [4345].
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Figure 4.10. Membrane reactors: (a) batch membrane reactor, (b) continuous membrane reactor and (c) recycle membrane reactor (coloured lines indicate membranes).
4.8.6 Applications of immobilized enzymes and cells
Immobilized enzymes and cells are extensively utilized for industrial, analytical and therapeutic applications, including their utilization in food production and research in biochemistry, microbiology and other allied sciences [50]. A summary of industrial applications of immobilized cells is provided in table 4.2.

4.9 Manufacture of commercial products

A list of signicant immobilized enzymes and their industrial applications is mentioned in table 4.2. Further details on the production of L-amino acids and high-fructose syrup are mentioned below.
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