Hollow fibers enzymes immobilization

An immobilized-enzyme continuous-flow reactor incorporating a continuous direct electrochemical regeneration of NAD + has been proposed. To retain the low molecular weight cofactor NADH/NAD+ within the reaction system, special hollow fibers (Dow ultrafilter UFb/HFU-1) with a molecular weight cut-off of 200 has been used [32],... 

O. Miyawaki, K. Nakamura, and T. Yano, Experimental investigation of continuous NAD recycling by conjugated enzymes immobilized in ultrafiltration hollow fiber, J. Chem. Eng. Jpn., 15(3), 224-228 (1982). 

HOLLOW-FIBER MEMBRANES. A hollow-fiher membrane is a capillary having an inside diameter of - inn and an outside diameter < I mm and whose wall functions as a semipermeahlc membrane. The fibers can he employed singly or grouped into a bundle which may contain tens of thousands of fibers and up to several million libers as in reverse osmosis (Fig. 11. In most eases, hollow fibers are used as cylindrical membranes that permit selective exchange of materials across (heir walls. However, they can also he used as containers to effect the controlled release of a specific material, or as reactors to chemically modify a permeate as il diffuses through a chemically activated hollow-liher wall. e g., loaded with immobilized enzyme. 

Lipases (E.C. 3.1.1.3.) catalyze the hydrolysis of lipids at an oil/water interface. In a membrane reactor, the enzymes were immobilized both on the side of the water phase of a hydrophobic membrane as well as on the side of the organic phase of a hydrophilic membrane. In both cases, no other means for stabilization of the emulsion at the membrane were required. The synthesis reaction to n-butyl oleate was achieved with lipase from Mucor miehei, which had been immobilized at the wall of a hollow fiber module. The degree of conversion reached 88%, but the substrate butanol decomposed the membrane before the enzyme was deactivated. 

The lipase enzyme stereospecifically hydrolyzes the (+) isomer of naproxen ester. The enzyme is immobilized in the wall of an inside-skinned hollow fiber membrane. The racemic d and / naproxen ester mixture, dissolved in methyl isobutyl ketone, is introduced on the shell side of the fiber and an aqueous buffer solution is circulated through the fiber lumen. The lipase enzyme hydrolyzes the d form of naproxen ester, forming ethanol and naproxen d. Naproxen d is a carboxylic acid soluble in aqueous buffer but insoluble in methyl isobutyl ketone. Consequently naproxen d is removed from the reactor with the buffer solution. The naproxen / ester remains in the methyl isobutyl ketone solution. This technique achieves an essentially complete separation of the d and Z forms. In a clever final step... 

In a multiphase membrane reactor, the conversion of benzylpenicillin to 6-aminopenidllinic acid is performed. The type of microstructured reactor used is a fermentation reactor which contains the enzyme penicillin acylase immobilized on the wall of a hollow-fiber tube. The hollow-fiber tube extracts 6-aminopenicillinic acid at the same time selectively. Benzylpenicillin is converted at the outer wall of the hollow fiber into the desired product, which passes into the sweep stream inside the fiber where it can be purified, e.g. by ion exchange. The non-converted benzylpenicillin is recycled back through the reactor [84],... 

The basic hydrodynamic equations are the Navier-Stokes equations [51]. These equations are listed in their general form in Appendix C. The combination of these equations, for example, with Darcy s law, the fluid flow in crossflow filtration in tubular or capillary membranes can be described [52]. In most cases of enzyme or microbial membrane reactors where enzymes are immobilized within the membrane matrix or in a thin layer at the matrix/shell interface or the live cells are inoculated into the shell, a cake layer is not formed on the membrane surface. The concentration-polarization layer can exist but this layer does not alter the value of the convective velocity. Several studies have modeled the convective-flow profiles in a hollow-fiber and/or flat-sheet membranes [11, 35, 44, 53-56]. Bruining [44] gives a general description of flows and pressures for enzyme membrane reactor. Three main modes... 

III (10-DAB) was carried out from which baccatin III was produced in an enzyme reactor. The enzyme reactor comprised a hollow-fiber polymeric ultrafiltration membrane, with immobilized acetyl transferase from Taxus species. The process enabled the production of baccatin III without requiring complicated purification steps of the acetyl transferase. The purification of the baccatin III is also made distinctly easier [20]. 

Asymmetric hollow fibers provide an interesting support for enzyme immobilization, in this case the membrane structure allows the retention of the enzyme into the sponge layer of the fibers by crossflow filtration. The amount of biocatalyst loaded, its distribution and activity through the support and its lifetime are very important parameters to properly orientate the development of such systems. The specific effect that the support has upon the enzyme, however, greatly depend upon both the support and the enzyme involved in the immobilization as well as the method of immobilization used. 

It is significant that the reaction mixture was worked up by removal of the unreacted ester by hexane extraction and concentration of the aqueous layer to obtain the desired (i )-amino acid. The process has a high throughput and was easy to handle on a large scale. However, because of the nature of a batch process, the enzyme catalyst could not be effectively recovered, adding significantly to the cost of the product. In the further scale up to 100-kg quantity productions, the resolution process was performed using Sepracor s membrane bioreactor module. The enzyme was immobilized by entrapment into the interlayer of the hollow-fiber membrane. Water and the substrate amino ester as a neat oil or hexane solution were circulated on each side of the membrane. The ester was hydrolyzed enantioselectively by the enzyme at the membrane interface, and the chiral acid product... 

Another favorable aspect of stirred batch reactors is the fact that they are compatible with most forms of a biocatalyst. The biocatalyst may be soluble, immobilized, or a whole-cell preparation in the latter case a bioconversion might be performed in the same vessel used to culture the organism. Recovery of the biocatalyst is sometimes possible, typically when the enzyme is immobilized or confined within a semi-permeable membrane. The latter configuration is often referred to as a membrane reactor. An example is the hollow fiber reactor where enzymes or whole cells are partitioned within permeable fibers that allow the passage of substrates and products but retain the catalyst. A hollow-fiber reactor can be operated in conjunction with the stirred tank and operated in batch or... 

Immobilization of lipases on hydrophobic supports has the potential to (1) preserve, and in some cases enhance, the activity of lipases over their free counterparts (2) increase their thermal stability (3) avoid contamination of the lipase-modified product with residual activity (4) increase system productivity per unit of lipase employed and (5) permit the development of continuous processes. As the affinity of lipases for hydrophobic interfaces constitutes an essential element of the mechanism by which these enzymes act, a promising reactor configuration for the use of immobilized lipases consists of a bundle of hollow fibers made from a microporous hydrophobic polymer (137). 

Membrane technology is a well-established technology for the immobilization of enzymes [233] since Degussa [234] introduced a continuous acylase process employing an enzyme-membrane reactor for the enantiomeric production of pure L-amino acids in 1981. Polymer membranes configured into hollow-fiber modules are, by far, the most widely used membrane where the enzyme is held back by the low cutoff of the membrane. 

Lipases can hydrolyze triglycerides into fatty acids and glycerol. They have been used extensively to produce optically active alcohols, acids, esters, and lactones by kinetic resolution. Lipases are unique, in that they are usually used in two-phase systems. A classic example is the use of a lipase for the production of (5, / )-2,3-p-methoxyphenylglycyclic acid, an intermediate for diltiazem. In this process, methyl-/7-methoxyphenylglycidate is stereospecifically hydrolyzed by a lipase immobilized in a hollow fiber membrane reactor. The enzyme is located at the interfacial layer between an organic and an aqueous phase. 

Scheme 15. The proposed continuous production of polar head modified phospholipid (1), its purification by PA removal (2) and hydrolysis to the corresponding OP (3). The three enzymes are immobilized in hollow fiber hydrophobic membrane bioreactors [179]...

Hollow-fiber membrane reactors with immobilized lipases have been used for the continuous hydrolysis of triglycerides188 and in the esterification of fatty acids.189 There was no deactivation of the enzyme in the former case in 16 days. In a comparable run in solution, the enzyme lost 80% of its activity in 2 days of operation. The latter case used dodecanol and decanoic acid in hexane to give the ester in 97% yield. The half-life of the immobilized enzyme was 70 days. The integration of reaction and separation can decrease product inhibition, increase selectivity, shift equilibria, and reduce the number of downstream operations.190... 

The term encapsulation has been used to distinguish entrapment preparations in which the biocatalyst environment is comparable to that of the bulk phase and where there is no covalent attachment of the protein to the containment medium (Fig. 6-1 D)[21J. Enzymes or whole cells may be encapsulated within the interior of a microscopic semi-permeable membranes (microencapsulation) or within the interior of macroscopic hollow-fiber membranes. Liposome encapsulation, a common microscopic encapsulation technique, involves the containment of an enzyme within the interior of a spherical surfactant bilayer, usually based on a phospholipid such as lecithin. The dimensions and shape of the liposome are variable and may consist of multiple amphiphile layers. Processes in which microscopic compart-mentalization (cf. living cells) such as multienzyme systems, charge transfer systems, or processes that require a gradient in concentration have employed liposome encapsulation. This method of immobilization is also commonly used for the delivery of therapeutic proteins. 

Besides the immobilization of enzymes on solid particles, enzymes may also be immobilized on the inner or outer surface of tubular supports such as on hollow fibers or flat membranes. Enclosure of enzymes by the use of an ultrafiltration or dialysis membrane is regarded as a form of immobilization. 

C)110 1, BrCN-Sepharose 1011, silica gel11021, or in a hollow fiber ultrafiltration membrane [421. The Eupergit C immobilized pig liver esterase retains 68% of the specific activity of the soluble enzyme. It is easily removed by filtration from the reaction mixture and can be reused several times when stored at 7 °C. In large-scale experiments with pig liver esterase in aqueous solution the enzyme can be stabilized, if necessary, by the addition of inexpensive bovine serum albumin1411. For a determination of the ee value of the monoester, different methods can be used ... 

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