Feasibility study for decomposition of gelatin layers on X-ray films by thermostable alkaline protease from alkaliphilic Bacillus sp.

Enzymatic decomposition of gelatin layers on X-ray films and repeated utilization of enzyme for potential industrialization were investigated using thermostable alkaline protease from the alkaliphilic Bacillus sp. B21-2. The decomposition of gelatin layers at 50 °C with the mutant enzyme (Ala187 was replaced by Pro) was higher than those of the wild-type and other mutant enzymes. In the repeated experiment for every 60 min (20 U ml^–1, 50 °C), the mutant enzyme could be satisfactorily used five times while three times for the wild-type enzyme.     

Kinetics of cellobiose hydrolysis using cellobiase composites from Ttrichoderma reesei and Aspergillus niger

The enzymatic hydrolysis of cellulose to glucose involves the formation of cellobiose as an intermediate. It has been found necessary(1) to add cellobiase from Aspergillus niger (NOVO) to the cellobiase component of Trichoderma reesei mutant Rut C-30 (Natick) cellulase enzymes in order to obtain after 48 h complete conversion of the cellobiose formed in the enzymatic hydrolysis of biomass. This study of the cellobiase activity of these two enzyme sources was undertaken as a first step in the formation of a kinetic model for cellulose hydrolysis that can be used in process design. In order to cover the full range of cellobiose concentrations, it was necessary to develop separate kinetic parameters for high- and low-concentration ranges of cellobiose for the enzymes from each organism. Competitive glucose inhibition was observed with the enzymes from both organisms. Substrate inhibition was observed only with the A. niger enzymes.     

Enzymatic hydrolysis of mycelial waste from the production of tetracycline

The process of enzymatic hydrolysis of the mycelial waste from the manufacture of tetracycline with using Streptomyces aureofaciens was studied. For the enzymatic hydrolysis, neutral and alkaline proteinases were used. It was shown that alkaline proteinase (protosubtilin G10X) provided the most efficient hydrolysis. Optimal conditions for the hydrolysis were determined: a temperature of 42 degrees C, hydrolysis time of 4 to 6 hours and enzyme concentrations of 1.25 to 2.20 mg/ml at a mycecial waste concentration of 12.5 mg/ml. The time course of changes in amino acid and amine nitrogen levels during enzymatic hydrolysis was investigated. It was demonstrated that the hydrolysis efficiency depended on the mode of enzyme addition. The highest efficiency was observed with fractional feeding of the enzyme.     

The lysis effect of bull spermatozoa on gelatin substrate film methodical investigations.

Proteolytic activity in the acrosomes of ejaculated bull spermatozoa was demonstrated using an autoradiographic film as a gelatin substrate. Incubation of the spermgelatin adducts at +37 degrees C and 94% humidity, which was kept constant by ventilating an incubator with water-saturated compressed air, yielded reproducible results. Gelatin depolymerisation started adjacent to the posterior segment of the acrosome within 30 to 60 s after application of individual spermatozoa to the substrate membrane and, finally, increased to a white circular digestion area enveloping the entire sperm head. The observed gelatinolysis seems to be mainly caused by acrosin, the trypsin-like acrosomal proteinase. This conclusion is supported by the positive correlation (r = +0.83, P is less than or equal to 0.01) found between the mean values of the lysis areas of individual spermatozoa on gelatin films and the acrosin activity of the sperm population measured with Bz-Arg-OEt as substrate after acidic extraction of the spermatozoa. In addition, prior saturation of the substrate layers with acrosin inhibitor (SSPI-I, II) from boar seminal plasma prevented the lysis reaction. Extraction of acrosin from the spermatozoa before application to the gelatin membranes resulted in a complete loss of any proteolytic activity. If spermatozoa were stored for 4 to 6 days at +4 degrees C or -20 degrees C in Tris buffer and afterwards applied to the substrate layer, lysis areas of individual spermatozoa differed markedly. Spermatozoa from undiluted ejaculated frozen at -20 degrees C showed no proteolytic effect on gelatin films. In general, there was a high correlation (r = +0.83, P is less than or equal 0.01) between the number of "living cells" characterized by live-dead staining and the percentage of spermatozoa active on the substrate membranes.     

Change of surface structure of poly(3-hydroxybutyrate) film upon enzymatic hydrolysis by PHB depolymerase

The change in the surface structure of poly[(R)-3-hydroxybutyrate] [PHB] films upon the enzymatic hydrolysis was analyzed by attenuated total reflection infrared [ATR/IR] spectrometry. As enzymes, PHB depolymerases isolated from Ralstonia pickettii T1 and Pseudomonas stutzeri were used. By curve decomposition of the carbonyl stretching band of ATR/IR spectra, the change in the surface crystallinity of PHB films by exposure to buffer containing 0, 1, and 4 microg of PHB depolymerases was estimated. It has been widely believed that the enzymatic hydrolysis first occurs in the amorphous phase, followed by the degradation in the crystalline phase, and extracellular PHB depolymerase can degrade only polymer chains in the surface layer of the film. Therefore, the surface crystallinity had been expected to increase upon the enzymatic degradation. However, the results were contrary to this expectation. The surface crystallinity was decreased by the enzymatic attack. Because ATR/IR spectrometry is sensitive to a small change in molecular structure of the sample surface, the decrease in the crystallinity shown by ATR/IR experiments probably does not indicate the complete loss of regularity of the crystalline phase. Because the chains at crystalline surface are more mobile than those inside the crystals, the C=O band for crystalline surface may appear at a position similar to those of the amorphous or interfacial phase in ATR/IR spectra of PHB. Only the chains inside the crystals may contribute to the C=O band of the crystalline phase. Thus, we rather suppose that the decrease in the crystalline peak of the ATR/IR spectra reflects the change in chain mobility or the increase of crystalline surface area by cracking of lamellas at the surface layers of PHB films or both.     

Factors affecting cellulose hydrolysis and the potential of enzyme recycle to enhance the efficiency of an integrated wood to ethanol process

Past technoeconomic modeling work has identified the relatively large contribution that enzymatic hydrolysis adds to the total cost of producing ethanol from lignocellulosic substrates. This cost was primarily due to the high concentration of enzyme and long incubation time that was required to obtain complete hydrolysis. Although enzyme and substrate concentration and end-product inhibition influenced the rate of hydrolysis, the effect was less pronounced during the initial stages of hydrolysis. During this time most of the cellulases were adsorbed onto the unhydrolyzed residue. By recycling the cellulases adsorbed to the residual substrate remaining after an initial 24 h, a high rate of hydrolysis, with low overall residence time and minimal cellulase input, could be achieved for several rounds of enzyme recycle. A comparison of the front end (pretreatment, fractionation, and hydrolysis) of a softwood/hardwood to ethanol process indicated that the lignin associated with the softwood-derived cellulose stream limited the number of times the cellulose containing residue could be recycled. (c) 1996 John Wiley & Sons, Inc.     

Enzymic thin film coatings for bioactive materials

Bioactive materials have been explored for a broad range of applications including biocatalysts, biosensors, antifouling membranes and other functional and smart materials. We report herein a unique method for preparation of bioactive materials through a spin coating process. Specifically, we investigated the preparation of protease Subtilisin Carlsberg-coated plastic films and examined their activities for hydrolysis of chicken egg albumin (CEA). The process generated enzymic coatings with a typical loading of 13 microg/cm2, retaining 46% of the enzyme activity for hydrolysis of CEA in aqueous solutions. Interestingly, the surface-coated protease thin film not only catalyzed the hydrolysis of CEA in aqueous solutions, but also showed good activity for solid-state CEA that was coated on top of the enzyme thin film.     

Recycle of enzymes and substrate following enzymatic hydrolysis of steam-pretreated aspenwood

The commercial production of chemicals and fuels from lignocellulosic residues by enzymatic means still requires considerable research on both the technical and economic aspects. Two technical problems that have been identified as requiring further research are the recycle of the enzymes used in hydrolysis and the reuse of the re calcitrant cellulose remaining after incomplete hydrolysis. Enzyme recycle is required to lower the cost of the enzymes, while the reuse of the spent cellulose will lower the feedstock cost. The conversion process studied was a combined enzymatic hydrolysis and fermentation (CHF) procedure that utilized the cellulolytic enzymes derived from the fungus Trichoderma harzianum E58 and the yeast Saccharomyces cerevisiae. The rate and extent of hydrolysis and ethanol production was monitored as was the activity and hydrolytic potential of the enzymes remaining in the filtrate after the hydrolysis period. When a commercial cellulose was used as the substrate for a routine 2-day CHF process, 60% of the original treated, water-extracted aspenwood was used as the substrate, only 13% of the original filter paper activity was detected after a similar procedure. The combination of 60% spent enzymes with 40% fresh enzymes resulted in the production of 30% less reducing sugars than the original enzyme mixture. Since 100% hydrolysis of the cellulose portion is seldom accomplished in an enzymatic hydrolysis pro cess, the residual cellulose was used as a substrate for the growth of T. harzianum E58 and production of celulolytic enzymes. The residue remaining after the CHF process was used as a substrate for the production of the cellulolytic enzymes. The production of enzymes from the residue of the Solka Floc hydrolysis was greater than the production of enzymes from the original Solka Floc.     

Kinetics and mechanism of heterogeneous hydrolysis of poly[(R)-3-hydroxybutyrate] film by PHA depolymerases

The kinetics and mechanism of enzymatic degradation on the surface of poly[(R)-3-hydroxybutyrate] (P[(R)-3HB]) film have been studied using three types of extracellular poly(hydroxyalkanoate) (PHA) depolymerases from Alcaligenes faecalis, Pseudomonas pickettii and Comamonas testosteroni. The monomer and dimer of 3-hydroxybutyric acid were produced during the course of the enzymatic degradation of P[(R)-3HB] film, and the rate of production was determined by monitoring the increase in absorbance at 210 nm on a spectrophotometer. The rate of enzymatic degradation increased to a maximum value with the concentration of PHA depolymerase, followed by a gradual decrease. The kinetic data were accounted for in terms of a heterogeneous enzymatic reaction, involving enzymatic degradation on the surface of P[(R)-3HB] film via two steps of adsorption and hydrolysis by a PHA depolymerase with binding and catalytic domains. The kinetic results suggest that the properties of the catalytic domains are very similar among the three PHA depolymerases, but that those of the binding domains are strongly dependent on the type of depolymerase.     

Enzyme electrode composed of the pyruvate oxidase from pediococcus species coupled to an oxygen electrode for measurements of pyruvate in biological media

Pyruvate oxidase from Pediococcus species was immobilized with gelatin and insolubilized in film form by tanning with glutaraldehyde. The film was fixed onto the tip of an oxygen electrode. The enzyme electrode was specific for pyruvate measurements. This electrode was sensitive to 0.1 mM and could be used up to a final pyruvate concentration of 2 mM.At each step of the enzymatic film preparation and assay 0.7 mM thiamine pyrophosphate, 10 μM flavin adenine dinucleotide, 5mM Mg²⁺ and 10 mM phosphate buffer were necessary.A computerized probe allowed successive measurements every 3 min for more than 20 h with the same enzymatic film. The reproducibillty for the same pyruvate concentration was 2% during 400 assays without special optimization.This enzyme electrode has many applications in basic (metabolism, enzymology) and applied (blood, yoghurt) research. Results obtained from assays carried out in yoghurt are presented.     

Effect of Cephtriaxone and Cephtasidim Antibiotics on Enzymatic Hydrolysis of Chitosan-Based Pellicular Materials

Enzymatic hydrolysis of chitosan-based films supplemented with cephtasidim and cephtriaxone antibiotics on a substrate saturated with water, diluted acetic acid, or Ringer-Locke physiological saline was studied. Supplementation with antibiotics having the chemical structure of low molecular weight salts reduced the rate of enzymatic hydrolysis of chitosan regardless of the medium used. The decrease was related to the suppression of polyelectrolyte swelling of the polycation rather than enzyme inhibition. The addition of antibiotics to chitosan films can apparently be considered an approach to directed reduction of the film enzymatic hydrolysis rates, which may contribute to an increase in film lifetime on the wound surface.     

Enzymatic properties of wild-type and active site mutants of chitinase A from Vibrio carchariae, as revealed by HPLC-MS

The enzymatic properties of chitinase A from Vibrio carchariae have been studied in detail by using combined HPLC and electrospray MS. This approach allowed the separation of alpha and beta anomers and the simultaneous monitoring of chitooligosaccharide products down to picomole levels. Chitinase A primarily generated beta-anomeric products, indicating that it catalyzed hydrolysis through a retaining mechanism. The enzyme exhibited endo characteristics, requiring a minimum of two glycosidic bonds for hydrolysis. The kinetics of hydrolysis revealed that chitinase A had greater affinity towards higher Mr chitooligomers, in the order of (GlcNAc)6 > (GlcNAc)4 > (GlcNAc)3, and showed no activity towards (GlcNAc)2 and pNP-GlcNAc. This suggested that the binding site of chitinase A was probably composed of an array of six binding subsites. Point mutations were introduced into two active site residues - Glu315 and Asp392 - by site-directed mutagenesis. The D392N mutant retained significant chitinase activity in the gel activity assay and showed approximately 20% residual activity towards chitooligosaccharides and colloidal chitin in HPLC-MS measurements. The complete loss of substrate utilization with the E315M and E315Q mutants suggested that Glu315 is an essential residue in enzyme catalysis. The recombinant wild-type enzyme acted on chitooligosaccharides, releasing higher quantities of small oligomers, while the D392N mutant favored the formation of transient intermediates. Under standard hydrolytic conditions, all chitinases also exhibited transglycosylation activity towards chitooligosaccharides and pNP-glycosides, yielding picomole quantities of synthesized chitooligomers. The D392N mutant displayed strikingly greater efficiency in oligosaccharide synthesis than the wild-type enzyme.     

Saccharification of biomass using whole solid‐state fermentation medium to avoid additional separation steps

The enzymatic hydrolysis of steam‐exploded sugarcane bagasse (SESB) was investigated using enzymatic extracts (EE) and whole fermentation media (WM), produced in‐house, from Aspergillus niger 3T5B8 and Trichoderma reesei Rut‐C30 cultivated on wheat bran under solid‐state fermentation (SSF). A detailed and quantitative comparison of the different hydrolysis conditions tested was carried out using the Chrastil approach for modeling enzymatic reactions by fitting the experimental data of total reducing sugar (TRS) released according to hydrolysis time. Conversion of SESB using A. niger enzymatic complex were up to 3.2‐fold higher (in terms of TRS) than T. reesei at similar enzyme loadings, which could be correlated to the higher β‐glucosidase levels (up to 35‐fold higher) of A. niger enzymatic complex. Conversion yields after 72 h exceeded 40% in terms of TRS when the WM was supplemented with a low dosage of a commercial enzyme preparation. When the combination of WM (from either T. reesei or A. niger) and commercial cellulase was used, the dosage of the commercial enzyme could be reduced by half, while still providing a hydrolysis that was up to 36% more efficient. Furthermore, SESB hydrolysis using either EE or WM resulted in similar yields, indicating that the enzyme extraction/filtration steps could be eliminated from the overall process. This procedure is highly advantageous in terms of reduced enzyme and process costs, and also avoids the generation of unnecessary effluent streams. Thus, the enzymatic conversion of SESB using the WM from SSF is cost‐effective and compatible with the biorefinery concept. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:1430–1440, 2013     

Enhanced resistance of polyelectrolyte multilayer microcapsules to pepsin erosion and release properties of encapsulated indomethacin

Polyelectrolyte multilayer films were prepared through layer-by-layer (LbL) self-assembly using polysaccharide sodium alginate (ALG) and chitosan (CHI). After incubation in an enzyme pepsin solution, the multilayer film was partially destroyed as detected by the decrease in fluorescent intensity because of the enzymatic degradation of CHI. The enzymatic desorption was also observed from the microcapsule wall made of the ALG/CHI multilayer film directly deposited on indomethacin (IDM) microcrystals through LbL self-assembly. After pepsin erosion, the IDM release from the microcapsules monitored by UV absorbance was obviously accelerated because of desorption. To enhance the stability of the ALG/CHI multilayer film to the enzymatic erosion, some physical and chemical methods were established to increase film thickness or to cross-link the polysaccharides within the film. Increasing the layer number and raising the deposition temperature effectively slowed down the enzymatic desorption and release rate. Especially, increasing deposition temperature was more effective because of producing a more perfect structure in the ALG/CHI multilayer film. Cross-linking the neighboring layers of ALG and CHI with 1-ethyl-3-(3-dimethylamino-propyl)carbodiimide in the ALG/CHI multilayer film significantly reduced the enzymatic desorption and release rate. Therefore, increasing deposition temperature and cross-linking neighboring layers are effective methods to protect the multilayer film fabricated using LbL assembly from the enzymatic erosion and to prolong the release of the encapsulated drug.     

Enzymatic synthesis of polyaniline film using a copper-containing oxidoreductase: bilirubin oxidase.

Electroactive polyaniline films have been synthesized by using a copper-containing oxidoreductase, bilirubin oxidase (BOD). Enzymatic polymerization took place on the surface of BOD-adsorbed solid matrix which was in contact with a buffer solution containing aniline. Optimum conditions for enzymatic polymerization of aniline were investigated. Elemental analysis and IR spectroscopy indicated that the enzymatically synthesized film was polyaniline. The cyclic voltammetric studies demonstrated that the polyaniline film was electrochemically reversible in the redox properties in acidic aqueous solutions. Since the film retained enzymatic activity of BOD which was employed as a catalyst for polymerization, enzymatic polymerization seems promising in preparation of immobilized enzyme membranes.     

Influence of mechanical agitation on cutinases and protease activity towards polyamide substrates

Two polyamide 6,6 substrates with different constructions, namely a model substrate and a fabric, were hydrolyzed using native cutinase and L182A cutinase mutant (from Fusarium solani pisi) and a protease (subtilisin from Bacillus sp.). The catalytic efficiency of these enzymes, measured in terms of hydrolysis products release, was measured for both substrates and the protease released five times more amines to the bath treatment. The L182A cutinase mutant showed higher activity when compared with the native enzyme.

All enzymes have shown activity additive effects with higher levels of mechanical agitation for polyamide fabrics. The results achieved are of paramount importance on the design of a process of enzymatic functionalization of polyamide.     

Effect of compounds released during pretreatment of wheat straw on microbial growth and enzymatic hydrolysis rates

In the process of producing ethanol from lignocellulosic materials such as wheat straw, compounds that can act inhibitory to enzymatic hydrolysis and to cellular growth may be generated during the pretreatment. Ethanol production was evaluated on pretreated wheat straw hydrolysate using four different recombinant Saccharomyces cerevisiae strains, CPB.CR4, CPB.CB4, F12, and FLX. The fermentation performance of the four S. cerevisiae strains was tested in hydrolysate of wheat straw that has been pretreated at high dry matter content (220 g/L dry matter). The results clearly showed that F12 was the most robust strain, whereas the other three strains were strongly inhibited when the fraction of hydrolysate in the fermentation medium was higher than 60% (v/v). Furthermore, the impact of different lignin derivatives commonly found in the hydrolysate of pretreated wheat straw, was tested on two different enzyme mixtures, a mixture of Celluclast 1.5 L FG and Novozym 188 (3:1) and one crude enzyme preparation produced from Penicillium brasilianum IBT 20888. From all the potential inhibiting compounds that were tested, formic acid had the most severe influence on the hydrolysis rate resulting in a complete inactivation of the two enzyme mixtures.     

Adsorption of cellulase from Trichoderma reesei on cellulose and lignacious residue in wood pretreated by dilute sulfuric acid with explosive decompression

The adsorption of cellulase on cellulose and a lignacious residue was examined by using cellulase from Trichoderma reesei, hardwood pretreated by dilute sulfuric acid under high pressure, and a lignacious residue prepared by a complete enzymatic hydrolysis of the pretreated wood. A significant amount of cellulase was found to adsorb on the lignacious residue during the hydrolysis of the pretreated wood. Hence, the adsorption of enzyme on the lignacious residue as well as cellulose must be taken into account in the development of the hydrolysis kinetics. It was found that the adsorption of enzyme on cellulose and on the lignacious residue could be represented by Langmuir type isotherms. The data show that the pretreatment at a higher temperature results in more enzyme adsorption on the cellulose fraction and less on the lignacious residue fraction. The relationship between the hydrolysis rate and the amount of enzyme adsorbed is discussed.     

Immobilization of acetylcholinesterase on gold nanoparticles embedded in sol-gel film for amperometric detection of organophosphorous insecticide

A simple method to immobilize acetylcholinesterase (AChE) on silica sol-gel (SiSG) film assembling gold nanoparticles (AuNPs) was proposed, thus a sensitive, fast and stable amperometric sensor for quantitative determination of organophosphorous insecticide was developed. The large quantities of hydroxyl groups in the sol-gel composite provided a biocompatible microenvironment around enzyme molecule and stabilized its biological activity to a large extent. The immobilized AChE could catalyze the hydrolysis of acetylthiocholine chloride (ATCl) with a Kmapp value of 450 microM to form thiocholine, which was then oxidized to produce detectable single with a linear range of 10-1000 microM. AuNPs catalyzed the electro-oxidation of thiocholine, thus increasing detection sensitivity. Based on the inhibition of organophosphorous insecticide on the enzymatic activity of AChE, using monocrotophos as a model compound, the conditions for detection of the insecticide were optimized. The inhibition of monocrotophos was proportional to its concentration ranging from 0.001 to 1 microg/ml and 2 to 15 microg/ml, with the correlation coefficients of 0.9930 and 0.9985, respectively. The detection limit was 0.6 ng/ml at a 10% inhibition. The developed biosensor exhibited good reproducibility and acceptable stability, thus providing a new promising tool for analysis of enzyme inhibitors.     

Replacement of arginine 246 by histidine in the beta subunit of Escherichia coli H+-ATPase resulted in loss of multi-site ATPase activity

A mutant strain KF43 of Escherichia coli defective in the beta subunit of H+-translocating ATPase (F0F1) was examined. In this mutant, replacement of Arg246 by His was identified by DNA sequencing of the mutant gene and confirmed by tryptic peptide mapping. The mutant F1-ATPase was defective in multi-site hydrolysis of ATP but was active in uni-site hydrolysis. Studies on the kinetics of uni-site hydrolysis indicated that the k1 (rate of ATP binding) was similar to that of the wild-type, but the k-1 (rate of release of ATP) could not be measured. The mutant enzyme had a k3 (rate of release of inorganic phosphate) about 15-fold higher than that of the wild-type and showed 3 orders of magnitude lower promotion from uni- to multi-site catalysis. These results suggest that Arg246 or the region in its vicinity is important in multi-site hydrolysis of ATP and is also related to the binding of inorganic phosphate. Reconstitution experiments using isolated subunits suggested that hybrid enzymes (alpha beta gamma complexes) carrying both the mutant and wild-type beta subunits were inactive in multi-site hydrolysis of ATP, supporting the notion that three intact beta subunits are required for activity of the F1 molecule.