Evaluation of magnetic polymer micro-beads as carriers of immobilised biocatalysts for selective and stereoselective transformations.

The kinetic, selective and stereoselective properties of enzyme immobilised on magnetic polymer beads with diameters in the range 1 microm was studied with penicillin amidase from E. coli. The enzyme was immobilised on epoxy and glutaraldehyde-activated poly(vinyl alcohol), poly(methylmetacrylate) and poly(vinyl acetate-divinylbenzene) magnetic beads. The amount of covalently bound active protein was dependent on the chemical modification of the matrix and increased at higher ionic strength of the immobilisation buffer. The small size of the magnetic beads, that reduces mass transfer limitations, and the decreased charge density in the electric double layer resulted in lower apparent Km values and higher efficiency for benzylpenicillin hydrolysis, higher stereoselectivity in condensation of R-phenylglycine amide with S- and R-Phe and in hydrolysis of racemic phenylacetyl-Phe and higher selectivity in kinetically controlled synthesis of cephalexin compared to the enzyme immobilised on larger and porous carriers.

Improvement of posttranslational bottlenecks in the production of penicillin amidase in recombinant Escherichia coli strains.

Using periplasmic penicillin amidase (PA) from Escherichia coli ATCC 11105 as a model recombinant protein, we reviewed the posttranslational bottlenecks in its overexpression and undertook attempts to enhance its production in different recombinant E. coli expression hosts. Intracellular proteolytic degradation of the newly synthesized PA precursor and translocation through the plasma membrane were determined to be the main posttranslational processes limiting enzyme production. Rate constants for both intracellular proteolytic breakdown (k(d)) and transport (k(t)) were used as quantitative tools for selection of the appropriate host system and cultivation medium. The production of mature active PA was increased up to 10-fold when the protease-deficient strain E. coli BL21(DE3) was cultivated in medium without a proteinaceous substrate, as confirmed by a decrease in the sum of the constants k(d) and k(t). The original signal sequence of pre-pro-PA was exchanged with the OmpT signal peptide sequence in order to increase translocation efficiency; the effects of this change varied in the different E. coli host strains. Furthermore, we established that simultaneous coexpression of the OmpT pac gene with some proteins of the Sec export machinery of the cell resulted in up to threefold-enhanced PA production. In parallel, we made efforts to increase PA flux via coexpression with the kil gene (killing protein). The primary effects of the kil gene were the release of PA into the extracellular medium and an approximately threefold increase in the total amount of PA produced per liter of bacterial culture.

Physico-chemical boundaries in the continuous and one-step discontinuous affinity-chromatographic isolation of proteins.

From a physico-chemical point of view, affinity chromatography has no unambiguous definition. It is generally understood as the one-step chromatographic isolation of a protein from a biological sample. For such processes the protein recovery and the adsorption capacity for a given adsorption time is limited by static and dynamic physico-chemical properties of the system. The protein recovery is limited by the ratio of the static capacity, n(s), and the dissociation constant, K, for the interaction with the immobilized binding site. The limits of these quantities for 90% and 99% protein recovery were estimated. The residence time required to reach 90% of the adsorptive capacity of an adsorbent is a function of the above static properties, the pore-diffusion coefficient, D(p), and the diffusion distance in the adsorbent. It was estimated and was found to correlate well with experimental data. The one-step discontinuous or continuous chromatographic isolation of one protein from a biological sample by means of adsorbents that separate with respect to different properties is reviewed. This is only possible with selective specific adsorbents and, in special cases, also with bifunctional adsorbents that use hydrophobic interactions for the adsorption, and electrostatic repulsion for the desorption.

Direct measurement of pH profiles in immobilized enzyme carriers during kinetically controlled synthesis using CLSM.

Confocal laser scanning microscopy was applied to measure the pH value in the carrier of immobilized enzymes during the enzyme-catalyzed synthesis. pH profiles with a high resolution are shown, with the pH increasing in the core of the particles. Significant differences occur for different carrier material, particle size, porosity and surface modification. The increased pH value is identified as one of the reasons leading to reduced enzyme selectivity in the penicillin amidase catalyzed synthesis of cephalosporins and penicillins.

Stability of immobilized soybean lipoxygenases: influence of coupling conditions on the ionization state of the active site Fe.

The potential application of lipoxygenase as a versatile biocatalyst in enzyme technology is limited by its poor stability. Two types of soybean lipoxygenases, lipoxygenase-1 and -2 (LOX-1 and LOX-2) were purified by a two step anion exchange chromatography. Four different commercially available supports: CNBr Sepharose 4B, Fractogel((R)) EMD Azlactone, Fractogel((R)) EMD Epoxy, and Eupergit((R)) C were tested for immobilization and stabilization of the purified isoenzymes. Both isoenzymes gave good yields in enzyme activity and good stability after immobilization on CNBr Sepharose 4B and Fractogel((R)) EMD Azlactone. Rapid decay in activity associated with change in the ionization state of Fe, as shown by EPR measurements was observed within the first 5 days after immobilization on epoxy activated supports (Eupergit((R)) C and Fractogel((R)) EMD Epoxy) in high ionic strength buffers. Stabilization of the biocatalyst on these supports was achieved by careful adjustment of the immobilization conditions. When immobilized in phosphate buffer of pH 7.5 and low ionic strength (0.05 M), the half-life time of the immobilized enzyme increased 20 fold. The dependence of the stability of LOX immobilized on epoxy activated supports on the coupling conditions was attributed to a modulation of the ligand environment of the iron in the active site and consequently its reactivity.

Structure of a slow processing precursor penicillin acylase from Escherichia coli reveals the linker peptide blocking the active-site cleft.

Penicillin G acylase is a periplasmic protein, cytoplasmically expressed as a precursor polypeptide comprising a signal sequence, the A and B chains of the mature enzyme (209 and 557 residues respectively) joined by a spacer peptide of 54 amino acid residues. The wild-type AB heterodimer is produced by proteolytic removal of this spacer in the periplasm. The first step in processing is believed to be autocatalytic hydrolysis of the peptide bond between the C-terminal residue of the spacer and the active-site serine residue at the N terminus of the B chain. We have determined the crystal structure of a slowly processing precursor mutant (Thr263Gly) of penicillin G acylase from Escherichia coli, which reveals that the spacer peptide blocks the entrance to the active-site cleft consistent with an autocatalytic mechanism of maturation. In this mutant precursor there is, however, an unexpected cleavage at a site four residues from the active-site serine residue. Analyses of the stereochemistry of the 260-261 bond seen to be cleaved in this precursor structure and of the 263-264 peptide bond have suggested factors that may govern the autocatalytic mechanism.

The relative importance of intracellular proteolysis and transport on the yield of the periplasmic enzyme penicillin amidase in Escherichia coli*

Intracellular proteolysis is an important mechanism for regulating the level of the periplasmic enzyme penicillin amidase in Escherichia coli. Evidence is presented that the active enzyme is localized in the periplasmic space and maturation of pro-enzyme occurs during transport through the cytoplasmic membrane or rapidly after its entrance in the periplasm. The rate constants of the transport through cytoplasmic membrane and of the intracellular proteolysis were estimated to be 0.01 h and 0.5 h, respectively. This indicates that more than 90% of the synthesized pre-pro-enzyme is lost by intracellular proteolysis occurring in the cytoplasm.

Intramolecular autoproteolysis initiates the maturation of penicillin amidase from Escherichia coli.

The penicillin amidase (PA) from Escherichia coli belongs to a group of proteolytically processed bacterial enzymes. The mechanism of the maturation of the single polypeptide proenzyme has been studied for the PA from E. coli using a slowly processing mutant proenzyme. The mutant proenzyme was constructed by replacing Thr with Gly in the Thr(263)-Ser(264) bond that must be hydrolysed in active PA. The mutant proenzyme was purified by biospecific affinity chromatography using an immobilized monoclonal antibody against PA. The maturation of the free and covalently immobilized purified proenzyme was studied in vitro. For the free proenzyme the same products with PA activity as observed in homogenates of wild-type PA-producing E. coli cells were found to be formed during this process. A kinetic analysis of the possible inter- and intramolecular processes involved in the maturation demonstrated that unambiguous evidence for the existence of intramolecular processes can only be obtained in systems where intermolecular processes are excluded. The Gly(263)-Ser(264) bond was found to be hydrolysed first in the free and immobilized mutant proenzyme, based on determinations of mass spectra, N-terminal sequences and active site concentrations. In the system with immobilized proenzyme intermolecular processes are excluded, demonstrating that this bond is hydrolysed by intramolecular autoproteolysis. Based on the known three-dimensional structure of the PA from E. coli the same maturation mechanism should apply for the wild-type proenzyme.

pH dependence of penicillin amidase enantioselectivity for charged substrates.

The pH dependence of E (enantiomeric ratio or enantioselectivity, a quantitative measure for enzyme stereospecificity) was studied for penicillin amidase catalysed hydrolysis of charged enantiomeric substrates. Theoretical analysis shows that a pH dependence can only be observed around the pK values of groups in the active site whose ionisation control the enzyme activity. For charged substrates that may perturb these pK values, a pH dependence of E is also expected. This was experimentally verified around these pK values. The S'(1)-stereospecificity of penicillin amidase was studied for the hydrolysis of the enantiomeric phenylacetyl-S/R-Phe and for the racemic phenylacetyl-S,R-PhG. The S(1)-stereospecificity was investigated for the hydrolysis of the enantiomeric S/R-PhG-NH(2). The observed pH modulation of E (more than 3-fold for the studied substrates in the pH range 4.5-9) was found to be a result of compensatory effects for binding and catalysis. The ratios k(cat, S)/k(cat,R) and K(m,S)/K(m,R) for the hydrolysis of the enantiomeric phenylacetyl-Phe were found to decrease from 1000 to 10 and from 0.1 to 0.01, respectively in the pH range 5-8. The dependence was stronger for the S'(1)- than for the S(1)-subsite. This is probably due to the stronger influence of the substrate carboxyl group in the S'(1)-subsite than that of the substrate amino group in the S(1)-subsite on the pK of the N-terminal Ser B1 that is essential for the activity. The observed pH dependence of E was used to discuss the importance of ground-state interactions for discrimination between enantiomers and for enzyme catalysis in general. The experimental results conform to the split site model according to which a better binding must not be fundamentally inhibitory.

Immobilized enzymes: crystals or carriers?

The advantages of immobilized over soluble enzymes arise from their enhanced stability and ease of separation from the reaction media, leading to significant savings in enzyme consumption. Immobilization methods range from binding to prefabricated carrier materials to packaging in enzyme crystals or powders. During their use, mass-transfer effects can produce substrate or pH gradients, which reduce the reaction rates and product yields. The costs of immobilized enzymes must be minimized in order to increase their competitiveness for technical applications.

Crystallization of a precursor penicillin acylase from Escherichia coli.

The crystallization of a mutant precursor penicillin acylase [penicillin amidohydrolase (amidase) E.C. 3.5.1.11] from Escherichia coli W (ATCC 11105) using the hanging-drop method is reported. The crystals are in space group P1 with unit-cell parameters a = 51.04, b = 63.58, c = 71.17 A, alpha = 103.0, beta = 110.6, gamma = 105.3 degrees, with one molecule in the asymmetric unit, and diffract to 1. 8 A using synchrotron radiation.

pH gradients in immobilized amidases and their influence on rates and yields of beta-lactam hydrolysis.

The pH gradients developing within immobilized biocatalysts during hydrolysis of penicillin G and glutaryl-7-aminocephalosporanic acid have been estimated both theoretically and experimentally. For the latter a fluorimetric method for the direct measurement of the average pH value within the carrier during reaction has been developed using the pH-dependent fluorescence intensity of an enzyme-bound fluorophore determined with a fiber bundle. The theoretical calculations were based on a model for the hydrolysis with immobilized enzymes using a kinetic expression with five pH-dependent, measurable kinetic and equilibrium constants. The transport reaction differential equation which considers the laminar boundary layer has been solved numerically for the key component. The calculated values agreed well with the experimental data. Under the typical reaction conditions of penicillin G hydrolysis the average pH value in the carrier was 1 and 2.5 pH units below the bulk pH (=8) with and without buffer, respectively. The corresponding changes for the hydrolysis of glutaryl-7-aminocephalosporanic acid at bulk pH 8 in the presence of buffer was 0.5. This demonstrates the existence of considerable pH gradients in carriers during hydrolytic reactions, even in buffered systems with negligible mass transfer resistance. The low pH value causes suboptimal reaction rates, reduced equilibrium conversion, and reduced enzyme stability. These pH gradients can be minimised by using buffers with pK values approximately equal to the bulk pH used for the hydrolysis. The prediction quality of the model has been tested applying it to fixed bed reactor design. The reduction in rate and yield due to concentration and pH gradients can be overcome with simple measures such as high initial pH value and pH adjustments in segmented or recycling fixed bed reactors. Thus, enzymatic conversions with high yield and high operational effectiveness are achieved.

Purification of monoclonal antibodies by simulated moving-bed chromatography.

A simulated moving bed (SMB) system has been developed for the biospecific purification of monoclonal antibodies. Adsorption and desorption of the desired product is performed under different conditions. To increase the purity and yield of the antibodies, two purge steps have to be introduced. The steady-state performance of the SMB system was modelled by solving the governing differential equations using a linear driving force approximation. The model parameters were determined independently in batch experiments. They were used to determine the operating conditions of the SMB system for the purification of monoclonal antibodies from cell culture supernatant. The antibodies could be isolated with a yield of > or = 90. SDS gel electrophoresis of the feed and product stream showed that more than 99% of the contaminating proteins were removed in a single step by SMB chromatography.

Temperature effects on S1- and S'1-enantioselectivity of alpha-chymotrypsin.

The temperature dependence of E (enantiomeric ratio or enantioselectivity, a quantitative measure for enzyme stereospecificity) has been studied for the alpha-chymotrypsin catalysed hydrolysis of the enantiomeric N-Boc-L/D-TyrOMe, L/D-TyrOMe, Ac-L/D-PhgOMe, L/D-PhgOMe and for the kinetically controlled synthesis of the diastereomeric dipeptides N-Ac-L-Tyr-L/D-ArgNH2 and N-Ac-L-Tyr-L/D-ValNH2. The results show that the S1- and S'1-enantioselectivity can be modulated by the temperature (3-15 fold for the studied substrates in the range 5-45 degrees C). For L/D-PhgOMe a reversal in stereospecificity was found in this temperature interval. For the studied substrates both an increase or decrease of the enantiomeric ratio with increasing temperature was observed. For these processes the following relation for the temperature dependence of E has been derived ln E = ln(kL/kD) = -(delta deltaH# - delta deltaHb)/RT + (delta deltaS# - delta deltaSb)/R where kL and kD are apparent second order rate constants for the reactions with the L- and D-enantiomers, respectively. Delta delta denotes the differences between the thermodynamic parameters for transformation of the enantiomeric substrates. The subscript b applies for the binding of the substrate or the nucleophile and the superscript # for the formation of the transition state of the enzyme acylation or deacylation. For the studied processes either the enthalpy (delta deltaH# - delta deltaHb) or the entropy (delta deltaS# - delta deltaSb) term was found to control the discrimination. Thus, the enantioselectivity decreases or increases with temperature, respectively. The influence of ground-state interactions and transition-state stabilisation on enzyme enantioselectivity has been discussed.

Purification and Properties of a Highly Thermostable, Sodium Dodecyl Sulfate-Resistant and Stereospecific Proteinase from the Extremely Thermophilic Archaeon Thermococcus stetteri.

The cultivation of the extremely thermophilic archaeon Thermococcus stetteri in a dialysis membrane reactor was paralleled by the production of an extremely heat-stable proteinase(s). By applying preparative sodium dodecyl sulfate (SDS)-polyacrylamide gel electrophoresis, an SDS-resistant proteinase was purified 67-fold in one step with a yield of 34%. The purified enzyme, which was composed of a single polypeptide chain with a molecular mass of 68 kDa, showed a broad temperature and pH profile (50 to 100(deg)C; pH 5 to 11). The optimal activity with substantial thermal stability was measured with casein at 85(deg)C and pH 8.5 to 9. Inhibition by phenylmethylsulfonyl fluoride and diisopropylfluorophosphate demonstrated that the enzyme was a serine proteinase. The enzyme displayed a relatively narrow substrate specificity, catalyzing the hydrolysis only of N-protected p-nitroanilides or p-nitrophenyl esters of basic (Arg or Lys) or hydrophobic (Phe or Tyr) l-amino acids. l-Phenylglycine amide was also attacked by the proteinase, but with a lower specificity constant. Within the detection limit, no hydrolysis of d-amino acid derivatives was observed. The catalytic efficiency of the enzyme at 80(deg)C (k(infcat)/K(infm) for benzoyl-Arg-p-nitroanilide, 10(sup4)) is the same order of magnitude when compared with that of functionally similar mesophilic enzymes. The proteinase also acts as a transferase, catalyzing the acyl transfer from protected amino acid ester or amide to amino acid amide. The observed thermostability, SDS resistance, relatively narrow substrate specificity, high stereospecificity, and limited catalytic efficiency probably reflect the tighter packing of the thermostable protein molecule and its limited flexibility. This was supported by fluorescence spectra of the enzyme, mainly due to tryptophan residues, in the temperature range of 30 to 90(deg)C. Structural reorganization was observed at temperatures over 100(deg)C. The results obtained could be of relevance for the better understanding of the structure-function relationship of enzymes from extreme thermophiles and suggest possible biotechnological application of the proteinase for resolution of racemic mixtures.

Enzyme catalyzed biotransformations in aqueous two-phase systems with precipitated substrate and/or product.

Biotransformations catalyzed by free and immobilized enzymes have been carried out in aqueous suspensions with up to 25% (w/w) precipitated substrate or product. For the kinetically controlled synthesis of N-Acetyl-Tyr-Arg-NH(2) with up to 0.8 M insoluble activated substrate N-Acetyl-TyrOEt catalyzed by alpha-chymotrypsin (EC3.4.21.1) the dipeptide yield was found to be >90%. This and the space-time yields were higher than those observed for one-phase aqueous systems and much higher than in systems where the insoluble substrate had been solubilized by addition of organic solvents. In the equilibrium controlled hydrolysis of 0.4 M D-phenylglycine-amide catalyzed by immobilized penicillin amidase (EC 3.5.1.11) the product precipitates. The enzyme immobilized in the support with the smallest pores could be reused without reduction in the rate due to precipitation in the pores. This decreases the number of immobilized enzyme molecules that can be used as biocatalysts. The latter was observed for supports with larger pores as the solubility decreases with increasing particle size. These results demonstrate that biotransformations with insoluble substrates or products using free or immobilized enzymes can be easily carried out in aqueous two-phase systems, without organic solvents, provided that the pore sizes of the supports are sufficiently small and that the rate of mass transfer from the precipitated substrate is large. The latter increases with decreasing particle size. (c) 1995 John Wiley & Sons, Inc.

Perfusible and non-perfusible supports with monoclonal antibodies for bioaffinity chromatography of Escherichia coli penicillin amidase within its pH stability range.

Several monoclonal antibodies (mABs) have been prepared and immobilized for the biospecific isolation of penicillin amidase (PA) from Escherichia coli (EC 3.5.1.11), an enzyme without S-S bridges and a pH stability range of 4-9. During the immobilization the fluorescence emission maxima of the mABs were found to change from 336 nm to ca. 350 nm. Only one of these mABs was found to be suitable for preparative bioaffinity chromatography of PA within the pH stability range. This mAB was immobilized on different spherical supports (Eupergit C 250 L and Sepharose) and one perfusible support (Knauer Quick Disc) and used for analytical and preparative bioaffinity chromatography. Under isocratic conditions the plate height for the perfusible biospecific adsorbent was found to be an order of magnitude lower than for the other supports. The different forms of this proteolytically processed bacterial enzyme could not be separated, however, by the biospecific adsorbents. At the mAB density used in the adsorbents (10-30 microM), less than 30% of the theoretical binding capacity of the immobilized mABs could be used to adsorb the enzyme.

Contributions to the S'-subsite specificity of papain.

The product ratio was analyzed for the papain-catalyzed acyl transfer from the specific acyl donor Mal-Phe-Ala-OEtCl to various nucleophilic amino components, ranging from amino acid amides to tripeptide amides. The data obtained are discussed in terms of binding specificity. From the structure-activity relationships for the S'1-P'1 interaction it follows that only three methyl(ene) groups can be accommodated in the S'1 subsite. Hydrophilic side chains are bound better to S'1 than indicated by their hydrophobicities. Negatively charged amino components are inefficient deacylating agents. However, there was no evidence for electrostatic contributions to the nucleophile binding. Amino components with bulky hydrophobic amino acid residues in the P'2 and in the P'3 position, respectively, are preferentially bound to Mal-Phe-Ala-papain. The results of this study can be applied to the planning of papain-catalyzed peptide synthesis reactions.

The membrane dialysis bioreactor with integrated radial-flow fixed bed--a new approach for continuous cultivation of animal cells.

A hybridoma cell was cultivated continuously in a membrane dialysis bioreactor with an integrated radial-flow fixed bed consisting of porous Siran carriers over a period of 6 weeks. Antibodies accumulated to an average of 100 mg l-1, approx. 10 times more than in fixed bed cultures without dialysis membrane. Serum costs could be reduced about 85% due to an appropriate feeding strategy. Siran carriers with 3-5 mm diameter showed an advantage compared to those with 1-2 mm diameter. For the 3-5 mm carrier the specific glucose uptake rate and the MAb production rate were constant, if the velocity was between 0.09 mm s-1 and 0.75 mm s-1. At higher velocities cells are washed out of the bed. Furthermore antibody consistency and cell stability were verified in long-term cultivations over a period of 96 days. From an estimation of the antibody concentration reachable with the reactor concept under optimal conditions a concentration 45 times higher compared to axial-flow fixed bed reactors and 11 times higher compared to stirred tank reactors can be expected.