Development of fermentation process for PLA-degrading enzyme production by a new thermophilic Actinomadura sp. T16-1

The fermentation process for a poly (L-lactide) (PLA)-degrading enzyme production by a newly isolate of thermophilic PLA-degrading Actinomadura sp. T16-1 was investigated. The strain produced 33.9 U/mL of enzyme activity after cultivation at 50°C under shaking of 150 rpm for 96 h in a medium consisting of (w/v) 0.05% PLA film, 0.2% gelatin, 0.4% (NH₄)₂SO₄, 0.4% K₂HPO₄, 0.2 % KH₂PO₄, and 0.02% MgSO₄ · 7H₂O. The optimal concentration of PLA film and gelatin obtained by response surface methodology (RSM) for the highest production of PLA-degrading enzyme was 0.035% (w/v) and 0.238% (w/v), respectively. Under these conditions, the model predicted 40.4 U/mL of PLA-degrading activity and the verification of the optimization showed 44.6 U/mL of PLA-degrading enzymatic activity in the flasks experiment. The maximum PLA-degrading activity reached 150 U/mL within 72 h cultivation in the 3-L airlift fermenter.     

Effective enhancement of polylactic acid-degrading enzyme production by Amycolatopsis sp. strain SCM_MK2-4 using statistical and one-factor-at-a-time approaches

This study aims to find the optimal medium and conditions for polylactic acid (PLA)-degrading enzyme production by Amycolatopsis sp. SCM_MK2-4. Screening of the most effective components in the enzyme production medium by Plackett–Burman design revealed that the silk cocoon and PLA film were the most significant variables enhancing the PLA-degrading enzyme production. After an response surface methodology, a maximum amount of PLA-degrading enzyme activity at 0.74?U?mL^?1 was predicted and successfully validated at 95% after 0.39% (w/v) silk cocoon and 1.62% (w/v) PLA film were applied to the basal medium. The optimal initial pH value, temperature, and inoculum size were evaluated by a method considering one-factor-at-a-time. The values were recorded at an initial pH in the range of 7.5–9.0, a temperature of 30–32°C, and an inoculum size of 4–10%. The highest activity of approximately 0.95?U?mL^?1 was achieved after 4 days of cultivation using the optimized medium and under optimized conditions in a shake flask. Upscaling to the use of a 3-L stirred tank fermenter was found to be successful with a PLA-degrading activity of 5.53?U?mL^?1; which represents a 51-fold increase in the activity compared with that obtained from the nonoptimized medium and conditions in the shake flask.     

Production of poly(l-lactide)-degrading enzyme by Amycolatopsis orientalis for biological recycling of poly(l-lactide)

Efficient production of poly(l-lactide)(PLA)-degrading enzyme was achieved by addition of 0.1% (w/v) silk fibroin powder into a liquid culture medium of an actinomycete, Amycolatopsis orientalis, without other complex nitrogen sources, such as yeast extract and peptone. Scaled-up production of the enzyme in a 5-l jar fermenter showed the possibility of producing this enzyme on an industrial scale at low production cost. The extracellular PLA-degrading enzyme showed potent degrading activity, which is effective for biological recycling of PLA, i.e., 2,000 mg/l of PLA powder was completely degraded within 8 h at 40°C using 20 mg/l purified enzyme. An optically active l-lactic acid with 600 mg/l was obtained as degradation product of PLA without undesirable racemization.     

Purification and characterization of an extracellular poly(L-lactic acid) depolymerase from a soil isolate, Amycolatopsis sp. strain K104-1

Poly(L-lactic acid) (PLA)-degrading Amycolatopsis sp. strains K104-1 and K104-2 were isolated by screening 300 soil samples for the ability to form clear zones on the PLA-emulsified mineral agar plates. Both of the strains assimilated >90% of emulsified 0.1% (wt/vol) PLA within 8 days under aerobic conditions. A novel PLA depolymerase with a molecular weight of 24,000 was purified to homogeneity from the culture supernatant of strain K104-1. The purified enzyme degraded high-molecular-weight PLA in emulsion and in solid film, ultimately forming lactic acid. The optimum pH for the enzyme activity was 9.5, and the optimum temperature was 55 to 60 degrees C. The PLA depolymerase also degraded casein and fibrin but did not hydrolyze collagen type I, triolein, tributyrin, poly(beta-hydroxybutyrate), or poly(epsilon-caprolactone). The PLA-degrading and caseinolytic activities of the enzyme were inhibited by diisopropyl fluorophosphate and phenylmethylsulfonyl fluoride but were not significantly affected by soybean trypsin inhibitor, N-tosyl-L-lysyl chloromethyl ketone, N-tosyl-L-phenylalanyl chloromethyl ketone, and Streptomyces subtilisin inhibitor. Thus, Amycolatopsis sp. strain K104-1 excretes the unique PLA-degrading and fibrinolytic serine enzyme, utilizing extracellular polylactide as a sole carbon source.     

Optimization of culture variables for improving glucoamylase production by alginate-entrapped Thermomucor indicae-seudaticae using statistical methods

Alginate-entrapped sporangiospores of Thermomucor indicae-seudaticae were used for the production of glucoamylase. The critical variables that affected glucoamylase production were identified by Plackett-Burman design (sucrose, yeast-extract, K(2)HPO(4) and asparagine) and further optimized by using a four factor central composite design (CCD) of response surface methodology (RSM). Immobilized sporangiospores secreted 41% and 60% higher glucoamylase titers in shake flasks and airlift fermenter, respectively, when the variables were used at their optimum levels (sucrose 3.0%, yeast-extract 0.2%, K(2)HPO(4) 0.1% and asparagine 0.35%). Glucoamylase production (26.3 U ml(-1)) in the optimized medium was in good agreement with the values predicted by the quadratic model (26.7 U ml(-1)), thereby confirming its validity. The enzyme production was sustainable in flasks of higher volume and also airlift fermenter, and attained a peak within 32 h in the fermenter as compared to that of 48 h in shake flasks.     

Growth and nicotinate biotransformation in batch cultured and airlift fermenter grown soybean cell suspension cultures

Summary Fermentation of a heterotrophic cell suspension culture of soybean (Glycine max) in a 15 l airlift fermenter for 10 to 12 days yielded appr. 4.67 kg fr. wt. (233.5 g dr. wt.) of biomass starting with an inoculum of 300 g fr. wt. Growth limiting factors were the conditions of preculturing the cells and the available amounts of phosphate and oxygen in the fermenter culture medium. Comparison of the metabolic activity of cells grown in 200 ml Erlenmeyer flasks and in the fermenter was performed by measuring the enzyme activities of nicotinamide-amidohydrolase and SAM: nicotinic acid-N-methyltransferase both in the presence and the absence of exogenous nicotinic acid during the biotransformation of nicotinate to trigonelline. The applied nicotinic acid was quantitatively taken up by the cells and an enhanced production of trigonelline could be observed. The activities of the aforementioned soybean enzymes were the same both in the batch cultured and in the airlift fermenter grown cells indicating good physiological conditions of the cells from the fermenter process.Abbreviations SAM S-adenosyl methionine - SCV sedimented cell volume - fr. wt. fresh weight - dr. wt. dry weight     

Production of carbonyl reductase by Geotrichum candidum in a laboratory scale bioreactor

Fungal fermentation is very complex in nature due to its nonlinear relationship with the time, especially in batch culture. Growth and production of carbonyl reductase by Geotrichum candidum NCIM 980 have been studied in a laboratory scale stirred tank bioreactor at different pH (uncontrolled and controlled), agitation, aeration and dissolved oxygen concentration. The yield of the process has been calculated in terms of glucose consumed. Initial studies showed that fermenter grown cells have more than 15 times higher activity than that of the shake flask grown cells. The medium pH was found to have unspecific but significant influence on the enzyme productivity. However, at controlled pH 5.5 the specific enzyme activity was highest (306U/mg). Higher agitation had detrimental effect on the cell mass production. Dissolved oxygen concentration was maintained by automatic control of the agitation speed at an aeration rate of 0.6 volume per volume per minute (vvm). Optimization of glucose concentration yielded 21g/l cell mass with and 9.77x10(3)U carbonyl reductase activity/g glucose. Adaptation of different strategies for glucose feeding in the fermenter broth was helpful in increasing the process yield. Feeding of glucose at a continuous rate after 3h of cultivation yielded 0.97g cell mass/g glucose corresponding to 29.1g/l cell mass. Volumetric oxygen transfer coefficient (K(L)a) increased with the increasing of agitation rate.     

Selection of strain and optimization of mutanase production in submerged cultures of Trichoderma harzianum

Nineteen fungal strains belonging to different genera were tested for extracellular mutanase production in shaken flasks. The optimal enzymatic activity was achieved by Trichoderma harzianum F-470, a strain for which the mutanase productivity has not yet been published. Some of factors affecting the enzyme production in shaken flasks and aerated fermenter cultures have been standardized. Mandels mineral medium with initial pH 5.3, containing 0.25% mutan and inoculated with 10% of the 48-h mycelium, was the best for enzyme production. A slight mutanolytic activity was also found when sucrose, raffinose, lactose and melibiose were carbon sources. Application of optimized medium and cultural conditions, as well as use of a fermenter with automatic pH control set at pH 6.0 enabled to obtain a high mutanase yield (0.33 U/ml, 2.5 U/mg protein) in a short time (2-3 days). The enzyme in crude state was stable over a pH range of 4.5-6.0, and at temperatures up to 35 degrees C; its maximum activity was at 40 degrees C and at pH 5.5.     

Identification and characterization of novel poly(<Emphasis Type="SmallCaps">dl</Emphasis>-lactic acid) depolymerases from metagenome

Many poly(lactic acid) (PLA)-degrading microorganisms have been isolated from the natural environment by culture-based methods, but there is no study about unculturable PLA-degrading microorganisms. In this study, we constructed a metagenomic library consisting of the DNA extracted from PLA disks buried in compost. We identified three PLA-degrading genes encoding lipase or hydrolase. The purified enzymes degraded not only PLA, but also various aliphatic polyesters, tributyrin, and p-nitrophenyl esters. From their substrate specificities, the PLA depolymerases were classified into an esterase rather than a lipase. Among the PLA depolymerases, PlaM4 exhibited thermophilic properties; that is, it showed the highest activity at 70 degrees C and was stable even after incubation for 1 h at 50 degrees C. PlaM4 had absorption and degradation activities for solid PLA at 60 degrees C, which indicates that the enzyme can effectively degrade PLA in a high-temperature environment. On the other hand, the enzyme classification based on amino acid sequences showed that the other PLA depolymerases, PlaM7 and PlaM9, were not classified into known lipases or esterases. This is the first report on the identification and characterization of PLA depolymerase from a metagenome.     

Optimization of diphtheria toxin production by <Emphasis Type="Italic">Corynebacterium diphtheriae</Emphasis> using a casein-based medium in a fermenter

The Td-based combined vaccine contains only small amounts of the diphtheria toxoid antigen. However, a high level of purity is necessary for this antigen. The diphtheria toxin is produced by growing Corynebacterium diphtheriae in a semisynthetic, casein-based medium in a fermenter. In order to obtain a highly pure diphtheria toxoid, the optimal conditions to express the toxin at 300 Lf/mL in a fermenter culture were determined. When C. diphtheriae was cultivated in a fermenter and a high concentration of toxin was obtained, specific patterns for the pH and dissolved oxygen levels identified. Overall, the fermenter cultivation process was divided into four stages according to variations in the pH. A specific range of K _La in the fermenter (0.0092 ~ 0.0093/sec) was required to produce high level expression of diphtheria toxin. The amount of toxin expression varied significantly according to culture conditions. Agitation and aeration in the fermenter affected toxin expression, even when the optimal K _La value for toxin production was maintained. A previous study has reported that the amounts of agitation and aeration are important factors when cultivating fungus in the fermenter to produce chitinolytic enzyme. A mass production of diphtheria toxoid with a purity level greater than 2,500 Lf/ mgPN was obtained through purification and detoxification from this optimized toxin production.     

Optimization of exopolysaccharide production from Armillaria mellea in submerged cultures

Aims: To study the optimization of submerged culture conditions for exopolysaccharide (EPS) production by Armillaria mellea in shake‐flask cultures and also to evaluate the performance of an optimized culture medium in a 5‐l stirred tank fermenter. Methods and Results: Shake flask cultures for EPS optimal nutritional production contained having the following composition (in g l^?1): glucose 40, yeast extract 3, KH₂PO₄ 4 and MgSO₄ 2 at an optimal temperature of 22°C and an initial of pH 4·0. The optimal culture medium was then cultivated in a 5‐l stirred tank fermenter at 1 vvm (volume of aeration per volume of bioreactor per min) aeration rate, 150 rev min^?1 agitation speed, controlled pH 4·0 and 22°C. In the optimal culture medium, the maximum EPS production in a 5‐l stirred tank fermenter was 588 mg l^?1, c. twice as great as that in the basal medium. The maximum productivity for EPS (Q_p) and product yield (Y_P/S) were 42·02 mg l^?1 d^?1 and 26·89 mg g^?1, respectively. Conclusions: The optimal culture conditions we proposed in this study enhanced the EPS production of A. mellea from submerged cultures. Significance and Impact of the Study: The optimal culturing conditions we have found will be a suitable starting point for a scale‐up of the fermentation process, helping to develop the production of related medicines and health foods from A. mellea.     

Purification and characterization of poly(L-lactic acid)-degrading enzymes from Amycolatopsis orientalis ssp. orientalis

Polylactide or poly(l-lactic acid) (PLA) is a commercially promising material for use as a renewable and biodegradable plastic. Three novel PLA-degrading enzymes, named PLAase I, II and III, were purified to homogeneity from the culture supernatant of an effective PLA-degrading bacterium, Amycolatopsis orientalis ssp. orientalis. The molecular masses of these three PLAases as determined by sodium dodecyl sulfate-polyacrylamide gel electrophoresis were 24.0, 19.5 and 18.0 kDa, with the pH optima being 9.5, 10.5 and 9.5, respectively. The optimal temperature for the enzyme activities was 50-60 degrees C. All the purified enzymes could degrade high-molecular-weight PLA film as well as casein, and the PLA-degrading activities were strongly inhibited by serine protease inhibitors such as phenylmethylsulfonyl fluoride and aprotinin, but were not susceptive to chymostatin and pepstatin. Taken together, these data demonstrated that A. orientalis ssp. orientalis produces multiple serine-like proteases to utilize extracellular polylactide as a sole carbon source.     

Biodegradation of poly(l-lactide)

The biodegradation of poly(L-lactide) (PLA) is reviewed. The important role of actinomycetes in PLA degradation is emphasized. These PLA-degrading actinomycetes belong phylogenetically to the Pseudonocardiaceae family and related genera, including Amycolatopsis, Lentzea, Streptoalloteichus, Kibdelosporangium and Saccharothrix. A PLA-degrading enzyme purified from an isolated Amycolatopsis strain-41 has substrate specificity on PLA higher than proteinase K. The application of these strains and their enzymes can be effectively used for biological treatment of plastic wastes containing PLA.     

Effects of initial maltose concentration, agitation and aeration rates on the production of glucosyltransferase byAspergillus niger CCRC 31494

Summary The microorganism Aspergillus niger CCRC 31494 can produce an extracellular glucosyltransferase (GTase, EC 2.4.1.24) with a high transglucosylating activity. The maximal enzyme production occurred at initial maltose concentration of 40 gl^-1. The microorganism was also grown in a 5-liter jar fermenter for GTase production. It was found that the optimal agitation and aeration rates were 750 rev min^-1 and 1.0 l min^-1, respectively, and the enzyme production was about 0.25–0.26 units ml^-1.     

Mannitol production by Leuconostoc citreum KACC 91348P isolated from Kimchi

Leuconostoc genus, which comprise heterofermentative lactic acid bacteria, reduces fructose to mannitol by recycling intracellular NADH. To evaluate the mannitol productivities of different Leuconostoc species, 5 stock cultures and 4 newly isolated strains were cultivated in MRS and simplified media containing glucose and fructose (1:2 ratio). Among them, L. citreum KACC 91348P, which was isolated from kimchi, showed superior result in cell growth rate, mannitol production rate, and yield in both media. The optimal condition for mannitol production of this strain was pH 6.5 and 30°C. When L. citreum KACC was cultured in simplified medium in a 2 l batch fermenter under optimal conditions, the maximum volumetric productivity was 14.83 g·l(-1)h(-1) and overall yield was 86.6%. This strain is a novel and efficient mannitol producer originated from foods to be used for fermentation of fructose-containing foods.     

Investigation of acid proteinase biosynthesis by the fungus Humicola lutea 120-5 in an airlift bioreactor

Acid proteinase production using filamentous fungus Humicola lutea 120-5 was studied under batch and continuous fermentation conditions in an airlift bioreactor. A comparison with proteinase production by fungal cells, cultivated in stirred tank bioreactor was made. The process performance in both fermentation devices was similar with respect to substrate utilization, biomass, and enzyme concentration. Continuous acid proteinase production was achieved for 14 days at an optimal dilution rate of 0.05/h with maximum specific activity of 90 U/mg DW of mycelia and yield of 38 U/mg glucose. The volumetric productivity (50 U/ml. h) was approximately 3 times higher than this of the batch system. All continuous experiments were carried out without any bacterial contamination, due to the low pH (3.0-3.5) during the process. The "pellet" type growth of the fungus in the airlift reactor prevented the system from plugging with filaments.     

Enhancement of α-amylase production by immobilized Bacillus subtilis in an airlift fermenter

Bacillus subtillis ATCC 21770 was entrapped in a carrageenan gel, especially formulated for immobilization. Bacterial growth and α-amylase (1,4-α-d-glucan glucanohydrolase EC 3.2.1.1) production were tested. The bead suspensions were submitted to two aeration modes, one consisting of bubbling air into a round flask, the other involving sparging of air into an airlift fermenter. The latter system, which produces microbubbles, gave 40–70% increase in enzyme production over the former and a doubling of bacterial density within the beads was measured. The use of CaCl₂instead of KCl as polymerization agent led to a better yield of α-amylase.     

Improved poly-ε-lysine biosynthesis using Streptomyces noursei NRRL 5126 by controlling dissolved oxygen during fermentation

The growth kinetics of Streptomyces noursei NRRL 5126 was investigated under different aeration and agitation combinations in a 5.0 l stirred tank fermenter. Poly-epsilon-lysine biosynthesis, cell mass formation, and glycerol utilization rates were affected markedly by both aeration and agitation. An agitation speed of 300 rpm and aeration rate at 2.0 vvm supported better yields of 1,622.81 mg/l with highest specific productivity of 15 mg/l.h. Fermentation kinetics performed under different aeration and agitation conditions showed poly- epsilon-lysine fermentation to be a growth-associated production. A constant DO at 40% in the growth phase and 20% in the production phase increased the poly-epsilon-lysine yield as well as cell mass to their maximum values of 1,992.35 mg/l and 20.73 g/l, respectively. The oxygen transfer rate (OTR), oxygen utilization rate (OUR), and specific oxygen uptake rates (qO2) in the fermentation broth increased in the growth phase and remained unchanged in the stationary phase.     

Production of leucine amino peptidase in lab scale bioreactors using Streptomyces gedanensis

Studies were conducted on the production of leucine amino peptidase (LAP) by Streptomyces gedanensis to ascertain the performance of the process in shake flask, parallel fermenter and 5-L fermenter utilizing soy bean meal as the carbon source. Experiments were conducted to analyze the effects of aeration and agitation rate on cell growth and LAP production. The results unveiled that an agitation rate of 300 rpm, 50% dissolved oxygen (DO) upholding and 0.15 vvm strategies were the optimal for the enzyme production, yielding 22.72 ± 0.11 IU/mL LAP in parallel fermenter which was comparable to flask level (24.65 ± 0.12 IU/mL LAP) fermentation. Further scale-up, in 5-L fermenter showed 50% DO and 1 vvm aeration rate was the best, producing optimum and the production was 20.09 ± 0.06 IU/mL LAP. The information obtained could be useful to design a strategy to improve a large-scale bioreactor cultivation of cells and production of LAP.     

克鲁维酵母Y-85合成菊粉酶最适条件的研究

采用响应面方法对克鲁维酵母Ｙ－８５产菊粉酶培养基成份进行了优选,和正交试验相比,该法选出的最适培养基的酶发酵水平提高２８％。用１５Ｌ自控发酵罐进行产酶条件控制试验,并在１０００Ｌ罐上进行了５批次酶发酵中试,平均菊粉酶活性达６８．９ｕ／ｍｌ。