Optimization of Cephalosporin C Acylase Expression in Escherichia coli by High-Throughput Screening a Constitutive Promoter Mutant library.

Cephalosporin C acylase (CCA) is capable of catalyzing cephalosporin C (CPC) to produce 7-aminocephalosporanic acid (7-ACA), an intermediate of semi-synthetic cephalosporins. Inducible expression is usually used for CCA. To improve the efficiency of CCA expression without gene induction, three recombinant strains regulated by constitutive promoters BBa_J23105, PLtetO1, and tac were constructed, respectively. Among them, BBa_J23105 was the best promoter and its mutant libraries were established using saturation mutagenesis. In order to obtain the mutants with enhanced activity, a high-throughput screening method based on flow cytometric sorting techniques was developed by using green fluorescent protein (GFP) as the reporter gene. A series of mutants were screened at 28 °C, 200 rpm, and 24-h culture condition. The study of mutants showed that the enzyme activity, fluorescence intensity, and promoter transcriptional strength were positively correlated. The enzyme activity of the optimal mutant obtained by screening reached 12772 U/L, 3.47 times that of the original strain.

Determination of the second autoproteolytic cleavage site of cephalosporin C acylase and the effect of deleting its flanking residues in the α-C-terminal region.

Self-activation through two-step intra-molecular cleavages is of great importance for the synthesis of mature and functional cephalosporin acylase in the N-terminal nucleophile (Ntn) hydrolase superfamily. A synthetic gene for cephalosporin C acylase (sCPCAcy) from Pseudomonas sp. SE83 was overexpressed, and the self-activated sCPCAcy was produced in Escherichia coli JM109(DE3)/pET28-sCPCAcy. The first autoproteolytic cleavage site of Pre-sCPCAcy was determined to be G239-S240 according to the common features of Ntn hydrolases. The second cleavage site was identified as A232-S233 by C-terminus tandem MS/MS analysis of the purified α-subunit, which released a 7-aa spacer peptide with the generation of the α and ß subunits of the mature sCPCAcy. The effect of the cleavage-site-flanking residues in the α-C-terminal region of sCPCAcy on its activation and characteristics was further evaluated. Residue G229 was found to be crucial for the first cleavage of Pre-sCPCAcy. Deletions in the α-C-terminal region were performed, and 14 mutant proteins were constructed. The majority of the fragment-deleted mutant proteins completely lost their activity due to failure of the first autocleavage, but this loss was not observed in mutant proteins D2 (227-AM-228 deletion) and D4 (212-ADLA-215 deletion), which formally activated into mature sCPCAcy with high activity. The Kcat/Km values of mutant proteins D2 and D4 were 46% and 102% higher than that of the original control, respectively.

Biological real-time reaction calorimeter studies for the production of penicillin G acylase from Bacillus badius.

Penicillin G acylase (PGA) is a commercially important enzyme that cleaves penicillin G to 6-amino penicillanic acid (6-APA) and phenyl acetic acid (PAA). The strain Bacillus badius has been identified as potential producer of PGA. A detailed calorimetric investigation on PGA production was carried out to enable generation of thermokinetic data possible for commercial application. Reaction calorimetric studies coupled with respirometric studies suggested that enzyme activity of the species B. badius was calorimetrically traceable. Three phases of growth were distinctly noticeable in the metabolic heat-time curve. Increase in enzymatic activity with restricted growth confirmed intracellular nature of the production process. The estimated heat yields due to biomass growth, 10.026 kJ/g, substrate consumption 22.761 kJ/g, and oxygen uptake 383 ± 10 kJ/mol helped to understand the energetic of the organism under study. Low oxycalorific coefficient confirmed the existence of fermentation-coupled metabolism of B. badius.

High-throughput strategies for penicillin G acylase production in rE. coli fed-batch cultivations.

BACKGROUND: Penicillin G acylase (PGA) is used industrially to catalyze the hydrolysis of penicillin G to obtain 6-aminopenicillanic acid. In Escherichia coli, the most-studied microorganism for PGA production, this enzyme accumulates in the periplasmic cell space, and temperature plays an important role in the correct synthesis of its subunits. RESULTS: This work investigates the influence of medium composition, cultivation strategy, and temperature on PGA production by recombinant E. coli cells. Shake flask cultures carried out using induction temperatures ranging from 18 to 28°C revealed that the specific enzyme activity achieved at 20°C (3000 IU gDCW-1) was 6-fold higher than the value obtained at 28°C. Auto-induction and high cell density fed-batch bioreactor cultures were performed using the selected induction temperature, with both defined and complex media, and IPTG and lactose as inducers. Final biomass concentrations of 100 and 120 gDCW L-1, and maximum enzyme productivities of 7800 and 5556 IU L-1 h-1, were achieved for high cell density cultures using complex and defined media, respectively. CONCLUSIONS: To the best of our knowledge, the volumetric enzyme activity and productivity values achieved using the complex medium are the highest ever reported for PGA production using E. coli. Overall PGA recovery yields of 64 and 72% after purification were achieved for crude extracts obtained from cells cultivated in defined and complex media, respectively. The complex medium was the most cost-effective for PGA production, and could be used in both high cell density and straightforward auto-induction protocols.

High-level expression of glutaryl-7-aminocephalosporanic acid acylase from Pseudomonas diminuta NK703 in Escherichia coli by combined optimization strategies.

In this work, a glutaryl-7-aminocephalosporanic acid acylase (GLA) coding gene was cloned from Pseudomonas diminuta NK703 which was screened from oilfield. The concerted effects of the expression system, inducing condition and culture medium on the expression of NK703 GLA in E. coli were firstly investigated. The best combination was the recombinant E. coli strain of pET-28a+GLA/BL21(DE3) with 2.0% (w/v) lactose inducing in YT medium at 25°C. Then, by optimizing the components of culture medium, a synthetic medium with dextrin and a feeding medium with glycerol as the carbon sources were developed to further enhance the GLA yield and improve the GLA solubility. In the end, the NK703 GLA activity increased about 50-fold, reached 14,470 ± 465 U/L, and the GLA productivity and the proportion of soluble GLA to the total soluble protein attained 206.0 ± 9.033 UL(-1)h(-1) and 60.13%, respectively. Scaling up the GLA production in 3.7 L fermenter under the optimized conditions identified in shake flask, the GLA activity also reached 12,406±521U/L, which was the highest report at fermenter level.

Cloning, overexpression, crystallization and preliminary X-ray crystallographic analysis of a slow-processing mutant of penicillin G acylase from Kluyvera citrophila.

Kluyvera citrophila penicillin G acylase (KcPGA) has recently attracted increased attention relative to the well studied and commonly used Escherichia coli PGA (EcPGA) because KcPGA is more resilient to harsh conditions and is easier to immobilize for the industrial hydrolysis of natural penicillins to generate the 6-aminopenicillin (6-APA) nucleus, which is the starting material for semi-synthetic antibiotic production. Like other penicillin acylases, KcPGA is synthesized as a single-chain inactive pro-PGA, which upon autocatalytic processing becomes an active heterodimer of α and ß chains. Here, the cloning of the pac gene encoding KcPGA and the preparation of a slow-processing mutant precursor are reported. The purification, crystallization and preliminary X-ray analysis of crystals of this precursor protein are described. The protein crystallized in two different space groups, P1, with unit-cell parameters a = 54.0, b = 124.6, c = 135.1 Å, α = 104.1, ß = 101.4, γ = 96.5°, and C2, with unit-cell parameters a = 265.1, b = 54.0, c = 249.2 Å, ß = 104.4°, using the sitting-drop vapour-diffusion method. Diffraction data were collected at 100 K and the phases were determined using the molecular-replacement method. The initial maps revealed electron density for the spacer peptide.

Strategies for enhancing the production of penicillin G acylase from Bacillus badius: influence of phenyl acetic acid dosage.

Bacillus badius isolated from soil has been identified as potential producer of penicillin G acylase (PGA). In the present study, batch experiments performed at optimized inoculum size, temperature, pH, and agitation yielded a maximum PGA of 9.5 U/ml in shake flask. The experiments conducted in bioreactor with different oxygen flow rates revealed that 0.66 vvm oxygen flow rate could be sufficient for the maximum PGA activity of 12.7 U/ml. From a detailed investigation on the strategies of the addition of phenyl acetic acid (PAA) for increasing the production of PGA, it was found that the controlled addition of 10 ml of 0.1 % (w/v) PAA once in every 2 h from 6th hour of growth showed the maximum PGA activity of 32 U/ml. Thus, our studies for the first time showed that at concentration above 0.1 % (w/v) PAA, the PGA production decreased. This selective condition paves the way for less costly bioprocess for the production of PGA.

A computational model for enhancing recombinant Penicillin G Acylase production from Escherichia coli DH5α.

An attempt was made to develop a computational model based on artificial neural network and ant colony optimization to estimate the composition of medium components for maximizing the productivity of Penicillin G Acylase (PGA) enzyme from Escherichia coli DH5α strain harboring the plasmid pPROPAC. As a first step, an artificial neural network (ANN) model was developed to predict the PGA activity by considering the concentrations of seven important components of the medium. Design of experiments employing central composite design technique was used to obtain the training samples. In the second step, ant colony optimization technique for continuous domain was employed to maximize the PGA activity by finding the optimal inputs for the developed ANN model. Further, the effect of a combination of ant colony optimization for continuous domain with a preferential local search strategy was studied to analyze the performance. For a comparative study, the training samples were fed into the response surface methodology optimization software to maximize the PGA production. The obtained PGA activity (56.94 U/mL) by the proposed approach was found to be higher than that of the obtained value (45.60 U/mL) with the response surface methodology. The optimum solution obtained computationally was experimentally verified. The observed PGA activity (55.60 U/mL) exhibited a close agreement with the model predictions.

Mutations in the translation initiation region of the pac gene resulting in increased levels of activity of penicillin G acylase.

Penicillin G acylase (PA) is an important enzyme used in the industrial production of b-lactam antibiotics. In this study, the effects of mutations in the translation initiation region of the Escherichia coli pac gene, encoding periplasmic PA, were examined. Several mutations led to increased amounts of PA activity, including those that lengthened the spacer region between the ribosome binding site and the ATG start codon, and those with altered codons on positions +2 and +4 relative to the start codon. These results indicated that the wild-type sequence of the pac gene does not provide maximum expression levels and that the strategies applied in this study can be used to improve production of PA in E. coli. Unexpectedly, our study also suggested that translocation of PA was, in contrast to earlier reports, shown not to require the Twin-arginine translocation pathway for transport into the periplasm.

Integrated development of an effective bioprocess for extracellular production of penicillin G acylase in Escherichia coli and its subsequent one-step purification.

An integrated bioprocess for effective production and purification of penicillin G acylase (PAC) was developed. PAC was overexpressed in a genetically engineered Escherichia coli strain, secreted into the cultivation medium, harvested, and purified in a single step by anion-exchange chromatography. The cultivation medium developed in this study had a sufficiently low conductivity to allow direct application of the extracellular fraction to the anion-exchange chromatography column while providing all of the required nutrients for sustaining cell growth and PAC overexpression. It was contrived with the purposes of (i) providing sufficient osmolarity and buffering capacity, (ii) minimizing ionic species to facilitate the binding of extracellular proteins to anion-exchange media, and (iii) enhancing PAC expression level and secretion efficiency. Employing this medium recipe the specific PAC activity reached a high level at 871 U/g DCW, of which more than 90% was localized in the extracellular medium. In addition, the osmotic pressure and induction conditions were found to be critical for optimal culture performance. The formation of inclusion bodies associated with PAC overexpression tended to arrest cell growth, leading to potential cell lysis. Clarified culture medium was applied to a strong anion-exchange (Q) column and PAC was purified by non-retentive separation, where most contaminant proteins bound to the chromatographic media with PAC being collected as the major component in the flow-through fraction. After removing the contaminant oligopeptides using ultrafiltration, purified PAC with a specific activity of 16.3 U/mg was obtained and the overall purification factor for this one-step downstream purification process was up to 3 fold.

Heterologous expression of leader-less pga gene in Pichia pastoris: intracellular production of prokaryotic enzyme.

BACKGROUND: Penicillin G acylase of Escherichia coli (PGAEc) is a commercially valuable enzyme for which efficient bacterial expression systems have been developed. The enzyme is used as a catalyst for the hydrolytic production of beta-lactam nuclei or for the synthesis of semi-synthetic penicillins such as ampicillin, amoxicillin and cephalexin. To become a mature, periplasmic enzyme, the inactive prepropeptide of PGA has to undergo complex processing that begins in the cytoplasm (autocatalytic cleavage), continues at crossing the cytoplasmic membrane (signal sequence removing), and it is completed in the periplasm. Since there are reports on impressive cytosolic expression of bacterial proteins in Pichia, we have cloned the leader-less gene encoding PGAEc in this host and studied yeast production capacity and enzyme authenticity. RESULTS: Leader-less pga gene encoding PGAEcunder the control of AOX1 promoter was cloned in Pichia pastoris X-33. The intracellular overproduction of heterologous PGAEc(hPGAEc) was evaluated in a stirred 10 litre bioreactor in high-cell density, fed batch cultures using different profiles of transient phases. Under optimal conditions, the average volumetric activity of 25900 U l-1 was reached. The hPGAEc was purified, characterized and compared with the wild-type PGAEc. The alpha-subunit of the hPGAEc formed in the cytosol was processed aberrantly resulting in two forms with C- terminuses extended to the spacer peptide. The enzyme exhibited modified traits: the activity of the purified enzyme was reduced to 49%, the ratios of hydrolytic activities with cephalexin, phenylacetamide or 6-nitro-3-phenylacetylamidobenzoic acid (NIPAB) to penicillin G increased and the enzyme showed a better synthesis/hydrolysis ratio for the synthesis of cephalexin. CONCLUSIONS: Presented results provide useful data regarding fermentation strategy, intracellular biosynthetic potential, and consequences of the heterologous expression of PGAEc in P. pastoris X-33. Aberrant processing of the precursor of PGAEc in the cytosol yielded the mature enzyme with modified traits.

Monitoring bioreactors using principal component analysis: production of penicillin G acylase as a case study.

The complexity of biological processes often makes impractical the development of detailed, structured phenomenological models of the cultivation of microorganisms in bioreactors. In this context, data pre-treatment techniques are useful for bioprocess control and fault detection. Among them, principal component analysis (PCA) plays an important role. This work presents a case study of the application of this technique during real experiments, where the enzyme penicillin G acylase (PGA) was produced by Bacillus megaterium ATCC 14945. PGA hydrolyzes penicillin G to yield 6-aminopenicilanic acid (6-APA) and phenyl acetic acid. 6-APA is used to produce semi-synthetic beta-lactam antibiotics. A static PCA algorithm was implemented for on-line detection of deviations from the desired process behavior. The experiments were carried out in a 2-L bioreactor. Hotteling's T(2) was the discrimination criterion employed in this multivariable problem and the method showed a high sensibility for fault detection in all real cases that were studied.

A process to produce penicillin G acylase by surface-adhesion fermentation using Mucor griseocyanus to obtain 6-aminopenicillanic acid by penicillin G hydrolysis.

The production of extracellular and mycelia-associated penicillin G acylase (maPGA) with Mucor griseocyanus H/55.1.1 by surface-adhesion fermentation using Opuntia imbricata, a cactus, as a natural immobilization support was studied. Enzyme activity to form 6-aminopencillanic acid (6-APA) from penicillin G was assayed spectrophotometrically. The penicillin G hydrolysis to 6-APA was evaluated at six different times using PGA samples recovered from the skim milk medium at five different incubation times. Additionally, the effect of varying the penicillin G substrate concentration level on the PGA enzyme activity was also studied. The maximum reaction rate, V (max), and the Michaelis constant, K (M), were determined using the Michaelis-Menten model. The maximum levels for maPGA and extracellular activity were found to be 2,126.50 international unit per liter (IU/l; equal to 997.83 IU/g of support) at 48 h and 755.33 IU/l at 60 h, respectively. Kinetics of biomass production for total biomass showed a maximum growth at 60 h of 3.36 and 2.55 g/l (equal to 0.012 g of biomass per gram of support) for the immobilized M. griseocyanus biomass. The maPGA was employed for the hydrolysis of penicillin G to obtain 6-APA in a batch reactor. The highest quantity of 6-APA obtained was 226.16 mg/l after 40-min reaction. The effect of substrate concentration on maPGA activity was evaluated at different concentrations of penicillin G (0-10 mM). K(M) and V(max) were determined to be 3.0 x 10(-3) M and 4.4 x 10(-3) mM/min, respectively.

Heterologous production of Escherichia coli penicillin G acylase in Pseudomonas aeruginosa.

Penicillin G acylase (PGA) is a widely studied bacterial enzyme of great industrial importance. Since its overproduction in the original organisms is mostly limited to the intracellular bacterial spaces which may lead to aggregation and cell toxicity, we have set out to explore the host organism Pseudomonas aeruginosa that possesses the Xcp machinery for secretion of folded proteins to the extracellular medium. We have made fusion proteins, consisting of Pseudomonas Sec- or Tat-specific signal peptides, the elastase propeptide and the mature penicillin G acylase. With all constructs we obtained production of PGA in P. aeruginosa, but we observed that processing of the PGA was temperature dependent and that the active enzyme could only be found after growth at 25 degrees C or lower temperatures. Remarkably, the mature protein, expressed from a TatProPGA hybrid, was not only found in the extracellular medium and the periplasm, but also in the cytoplasm as assessed by comparison to the reporter beta-lactamase protein. The unusual cytoplasmic localization of the mature protein strongly suggests that processing of PGA can also occur in the cytoplasm of P. aeruginosa. The extracellular localization of the TatProPGA hybrid was found not to be dependent on the tatABC-genes. The elastase signal sequence/propeptide combination appeared to be an inadequate carrier for transporting penicillin G acylase across the outer membrane of P. aeruginosa.

Optimization of glutaryl-7-aminocephalosporanic acid acylase expression in E. coli.

A recombinant glutaryl-7-aminocephalosporanic acid acylase (GLA) from Pseudomonas N176 has been over-expressed in BL21(DE3)pLysS Escherichia coli cells. By alternating screenings of medium components and simplified factorial experimental designs, an improved microbial process was set up at shake-flask level (and then scaled up to 2L-fermentors) giving a approximately 80- and 120-fold increase in specific and volumetric enzyme productivity, respectively. Under the best expression conditions, approximately 1380 U/g cell and 16,100 U/L of GLA were produced versus the approximately 18 U/g cell and the approximately 140 U/L obtained in the initial standard conditions. Osmotic stress caused by the addition of NaCl, low cell growth rate linked to high biomass yield in the properly-designed rich medium, optimization of the time and the amount of inducer's addition and decrease of temperature during recombinant protein production, represent the factors concurring to achieve the reported expression level. Notably, this expression level is significantly higher than any previously described production of GLAs. High volumetric production, cost reduction and the simple one-step chromatographic purification of the His-tagged recombinant enzyme, makes this GLA an economic tool to be used in the 7-ACA industrial production.

[Cloning and expression of variants of the glutaryl-7-aminocephalosporic acid acylase of the bacterium Brevundimonas diminuta in Escherichia coli cells].

The gene coding for glutaryl-7-aminocephalosporic acid acylase (Gl7ACA acylase) of the bacterium Brevundimonas diminuta (BrdGl7ACA), a commercial enzyme widely used in modem biocatalytic technologies for manufacture of b-lactam antibiotics, was cloned. Efficient expression systems for producing a "native" recombinant BrdGl7ACA and its analogs modified by attaching affinity groups--the chitin-binding domain of chitinases A1 and hexahistidine sequence--were designed. It was demonstrated that both the recombinant hybrid proteins and the native Gl7ACA acylase produced in E. coli cells underwent a correct autoproteolytic processing with generation of functionally active enzymes and could be isolated with a high yield using one-step affinity chromatography.

Effects of induction starting time and Ca2+ on expression of active penicillin G acylase in Escherichia coli.

Formation of inclusion bodies is an important obstacle to the production of active recombinant protein in Escherichia coli. Thus, soluble expression of penicillin G acylase from Kluyvera citrophila was investigated in BL21(DE3). In this study, the yield of active enzyme was significantly enhanced by the composition of the medium and induction opportunity. When 0.5 mmol/L IPTG was added to complex medium at 15 h after incubation, the volumetric and specific activities of penicillin G acylase both achieved the highest values, respectively. However, aggravation of intracellular proteolysis and decline of enzyme expression were also observed if induction occurred too much later. Ca2+ ion was another critical factor in cell growth and protein expression. When 24 mmol/L Ca2+ ion was adding to the medium at the beginning of fermentation, a greater than 2-fold increase in cell density and a 7-fold increase in volumetric activity of penicillin G acylase were reached. Nevertheless, no significant benefit for recombination protein expression was found when excess Ca2+ was added after induction time. This study demonstrates that the induction starting time and Ca2+ ion are two critical factors for the expression of active penicillin G acylase.

Comparing the performance of multilayer perceptrons networks and neuro-fuzzy systems for on-line inference of Bacillus megaterium cellular concentrations.

Penicillin G acylase (PGA) is one of the most important enzymes for the pharmaceutical industry. Bacillus megaterium has the advantage of producing extra-cellular PGA. This work compares two neural networks (NNs) architectures for on-line inference of B. megaterium cell mass in an aerated stirred tank bioreactor, during the production of PGA. Nowadays, intelligent computing tools such as artificial NNs and fuzzy logic are commonly applied for state inference and modeling of bioreactors. Combining these two approaches in hybrid, neuro-fuzzy systems, may be advantageous. Our results indicate that a neuro-fuzzy inference system showed a better performance to infer cell concentrations, when compared to multilayer perceptrons networks.

Effect of heat-shock proteins for relieving physiological stress and enhancing the production of penicillin acylase in Escherichia coli.

High-level expression of recombinant penicillin acylase (PAC) using the strong trc promoter system in Escherichia coli is frequently limited by the processing and folding of PAC precursors (proPAC) in the periplasm, resulting in physiological stress and inclusion body formation in this compartment. Periplasmic heat-shock proteins with protease or chaperone activity potentially offer a promise for overcoming this technical hurdle. In this study, the effect of the two genes encoding periplasmic heat-shock proteins, that is degP and fkpA, on pac overexpression was investigated and manipulation of the two genes to enhance the production of recombinant PAC was demonstrated. Both DeltadegP and DeltafkpA mutants showed defective culture performance primarily due to growth arrest. However, pac expression level was not seriously affected by the mutations, indicating that the two proteins were not directly involved in the pathway for periplasmic processing of proPAC. The growth defect caused by the two mutations (i.e., DeltadegP and DeltafkpA) was complemented by either one of the wild-type proteins, implying that the function of the two proteins could partially overlap in cells overexpressing pac. The possible role that the two heat-shock proteins played for suppression of physiological stress caused by pac overexpression is discussed.

The penicillin G acylase production by B. megaterium is amino acid consumption dependent.

Aiming at to enhance the production of penicillin G acylase (PGA) by Bacillus megaterium, we have performed flasks experiments using different medium composition. Using 51 g/L of casein hydrolyzed with Alcalase and 2.7 g/L of phenylacetic acid (PhAc), the following carbon substrates were tested, individually and combined: glucose, glycerol, and lactose (present in cheese whey). Glycerol and glucose showed to be effective nutrients for the microorganism growth but delayed the PGA production. Cheese whey always increased enzyme production and cell mass. However, lactose (present in cheese whey) was not a significant carbon source for B. megaterium. PhAc, amino acids, and small peptides present in the hydrolyzed casein were the actual carbon sources for enzyme production. Replacement of hydrolyzed casein by free amino acids, 10.0 g/L, led to a significant increase in enzyme production (app. 150%), with a preferential consumption of alanine, aspartic acid, glycine, serine, arginine, threonine, lysine, and glutamic acid. A decrease of the enzyme production was observed when 20.0 g/L of amino acids were used. Using the single omission technique, it was shown that none of the 18 tested amino acids was essential for enzyme production. The use of a medium containing eight of the preferentially consumed amino acids lead to similar enzyme production level obtained when using 18 amino acids. PhAc, up to 2.7 g/L, did not inhibit enzyme production, even if added at the beginning of the cultivation.