Immobilization of Streptomyces clavuligerus on loofah sponge for the production of clavulanic acid

Clavulanic acid, a naturally occurring powerful inhibitor of bacterial beta-lactamases, is produced by Streptomyces clavuligerus. The high void volume, permeability, and low cost of fibrous matrices prompted the use of Luffa cylindrica as a matrix for the immobilization of S. clavuligerus for the production of clavulanic acid. Immobilization of S. clavuligerus onto loofah sponge discs was studied with respect to the optimization of the inoculum size (number of discs) and its reusability for clavulanic acid production. Best yield of 1125 microg ml(-1) clavulanic acid was reached with two discs of loofah sponge (each approximately 0.136 g dry weight) and 120 h duration in the first cycle. Data obtained during four reusable cycles showed reduction in the initiation time of clavulanic acid production, resulting in higher levels of clavulanic acid in shorter time duration. Immobilization of S. clavuligerus on to loofah sponge discs, therefore, permit repeated reuse under the specified fermentation conditions for clavulanic acid production.     

Production of acid proteinases by Humicola lutea mycelium immobilized in polyurethane sponge.

Humicola lutea 120-5 spores were entrapped in polyurethane sponge cubes and were cultivated inside the carrier to form an immobilized mycelium further used for production of acid proteinases in batch mode. A carrier—spore suspension ratio of 10:0.5 (wt) should be used to obtain optimal results. The polyurethane sponge-immobilized mycelium could be applied repeatedly, the enzyme activity secreted during the first 10 cycles being about the same as that produced by free cells. The advantages of immobilizing fungal cells by germinating conidia entrapped inside the supporting material are discussed.     

Effect of support materials on antibiotic MSW2000 production by immobilized Streptomyces violatus

The production of an antibiotic by free and immobilized cells of Streptomyces violatus through entrapment or adsorption on different materials was investigated. S. violatus entrapped in Ca-alginate beads gave low antibiotic activity compared to the free cell or adsorbed cell, while the adsorption of S. violatus on sponge cubes yielded the highest antibiotic concentration after 4 days of incubation in static cultures. A starch concentration of 10 g/L was optimum for the production of the antibiotic by adsorbed cells. The weight and size of the sponge cubes used for immobilization influenced production of the antibiotic and the optimum weight and size of the sponge were 0.8 g and 1.0 cm(3), respectively, yielding a maximum antibiotic production of 280 mg/ml. Maximum antibiotic production was obtained at an initial pH value of 7.5 and in an inoculum size of 3 ml (spore suspension) per 50 ml. The production of the antibiotic in a fixed-bed bioreactor reached a maximum value after 2 days of incubation at a circulation rate of 30 ml/h. The immobilized cells in the bioreactor were reused seven successive times over a period of 14 days.     

Ethanol production from concentrated food waste hydrolysates with yeast cells immobilized on corn stalk

The aim of the present study was to examine ethanol production from concentrated food waste hydrolysates using whole cells of S. cerevisiae immobilized on corn stalks. In order to improve cell immobilization efficiency, biological modification of the carrier was carried out by cellulase hydrolysis. The results show that proper modification of the carrier with cellulase hydrolysis was suitable for cell immobilization. The mechanism proposed, cellulase hydrolysis, not only increased the immobilized cell concentration, but also disrupted the sleek surface to become rough and porous, which enhanced ethanol production. In batch fermentation with an initial reducing sugar concentration of 202.64 ± 1.86 g/l, an optimal ethanol concentration of 87.91 ± 1.98 g/l was obtained using a modified corn stalk-immobilized cell system. The ethanol concentration produced by the immobilized cells was 6.9% higher than that produced by the free cells. Ethanol production in the 14th cycle repeated batch fermentation demonstrated the enhanced stability of the immobilized yeast cells. Under continuous fermentation in an immobilized cell reactor, the maximum ethanol concentration of 84.85 g/l, and the highest ethanol yield of 0.43 g/g (of reducing sugar) were achieved at hydraulic retention time (HRT) of 3.10 h, whereas the maximum volumetric ethanol productivity of 43.54 g/l/h was observed at a HRT of 1.55 h.     

Improvement of acid phosphatase production by immobilization of Humicola lutea mycelium in polyurethane sponge

Acid phosphatase production by the fungus Humicola lutea 120-5, immobilized in polyurethane sponge, was studied under semicontinuous shake flask fermentation and compared to the enzyme secretion by free cells. The effect of parameters such as the carrier content and the duration of the batch in repeated batch experiments on the phosphatase production half-life was investigated. The best results were obtained with 1.0 g of sponge cubes (about 1.0 cm per side) per culture flask using 72 h runs. In these conditions the half-life of enzyme production by immobilized biocatalyst was 15 sequential cycles (45 days) compared to three cycles (9 days) for the free mycelium. The maximal phosphatase titre registered in free cell fermentation was 2500 U/l (i.e. 100%), while the relative enzyme activity of the optimal immobilized system was over 100% during the whole half-life time of 45 days. Significant improvement (200–215%) in the yield was observed in one-third of this period or 15 days. The supernatant medium obtained at any stage of the repeated batch cultures did not contain free cells and, due to the low pH (3.0–3.5), the whole process was carried out without any bacterial contamination. In comparison with free cell fermentation, the significant improvement of the acid phosphatase production by polyurethane sponge-immobilized H. lutea mycelium as well as its operation stability was confirmed by scanning electron microscopy.     

New method of immobilization of microbial cells by capture on the surface of insoluble pyridinium-type resin

A new method for the immobilization of microbial cells has been developed. Whole cells of Escherichia coli with aspartase activity were immobilized by capture on the surface of cross-linked poly(N-benzyl-4-vinylpyridinium bromide) containing styrene (BVPS resin), an insoluble pyridinium-type resin. When a suspension of the bacterial cells in buffer solution was passed through a glass column containing beads of BVPS resin, the cells were captured on the resin surface and formed an immobilized cell system. A fixed-bed column reactor containing 300 mg of the bacterial cells immobilized by capture on 10 g of BVPS resin beads was used for the preparation of L-aspartic acid from ammonium fumarate. Continuous operation of tne bioreactor produced L-aspartic acid in a quantitative yield when the influent substrate concentration was 0.1M and the flow rate was 0.41-0.83 bed volumes per hour at pH 7.4-7.7 at 30 degrees C.     

Bioreactor for continuous synthesis of compactin by Penicillium cyclopium

Compactin was synthesized by Penicillium cyclopium in submerged as well as in bioreactor systems and assayed spectrophotometrically with a detection limit of 0.5 μg ml⁻¹ solvent. Synthesis in submerged culture was affected by aeration, glucose level, pH, and type and molarity of buffer. Citrate or succinate (pH 4.0, 0.10 M) in malt glucose peptone broth (MGPB) stimulated cell specialization, sporulation, enhanced compactin permeation from mycelia and its production (60.05 μg ml⁻¹ after 12 days). Fungal spores, immobilized onto-into loofah sponge, in a bioreactor, using MGPB-citrate as feed stock, resulted in productivity of 23.04 mg compactin (L⁻¹ h⁻¹) during 50 days operation at 0.45 h⁻¹ dilution rate. Compactin synthesis in the bioreactor was also affected by culture age, substrate, incubation and dilution rates. Scanning electron micrographs of the loofah sponge, prior to, during and post-spores immobilization showed that loofah channels served well for fungal support in the bioreactor. Received 6 October 1997/ Accepted in revised form 2 September 1998     

Fed-batch cultivation for the production of clavulanic acid by an immobilized Streptomyces clavuligerus mutant

In order to obtain high productivity of clavulanic acid, a newly-introduced carrier, polyurethane pellet (PUP) Z97-020 was used for the immobilization process. In a stirred-tank bioreactor, batch cultivation by Streptomyces clavuligerus KK immobilized on PUP Z97-020 gave about 3100 mg of clavulanic acid per litre, representing an increase of 200% in productivity compared with that by fed-batch cultivation of free cells (1500 mg/l). However, the clavulanic acid produced rapidly decomposed due to the pH change during batch cultivation. Fed-batch cultivation by immobilized S. clavuligerus KK gave an excellent level of clavulanic acid up to 3250 mg/l, a productivity increase of 220% compared with that by fed-batch cultivation of free cells. These results suggest that immobilization with PUP Z97-020 is a more effective process for the production of clavulanic acid and that the maintenance of pH by fed-batch cultivation with glycerol as a limiting substrate prevents the clavulanic acid from decomposing during the fermentation.     

Development of a method for immobilization of non-flocculating cells in loofa (Luffa cylindrica) sponge

Both the matrix structure of loofa sponge and the flocculating property of cells were necessary for efficient immobilization. The addition of chitosan to a reactor containing a bed of loofa sponge and a Candida brassicae cell suspension induced cell flocculation and the cells were efficiently immobilized. During ethanol production by the immobilized cells, the free cell concentration in the broth was controlled at the desired level by intermittent addition of chitosan to the reactor. The immobilized cell concentration increased but their specific ethanol productivity decreased with an increase in the chitosan concentration. The maximum ethanol productivity was obtained at a low chitosan concentration of 0·03 g/litre. With this optimal concentration, the cell concentration, ethanol yield and productivity were, respectively, 2, 1·3 and 3 times higher than those of the suspension culture.     

Production of tannase by the immobilized cells of Bacillus licheniformis KBR6 in Ca-alginate beads

AIMS: The present study was aimed at finding the optimal conditions for immobilization of Bacillus licheniformis KBR6 cells in calcium-alginate (Ca-alginate) beads and determining the operational stability during the production of tannin-acyl-hydrolase (tannase) under semicontinous cultivation. METHODS AND RESULTS: The active cells of B. licheniformis KBR6 were immobilized in Ca-alginate and used for the production of tannase. The influence of alginate concentration (5, 10, 20 and 30 g l(-1)) and initial cell loading on enzyme production were studied. The production of tannase increased significantly with increasing alginate concentration and reached a maximum enzyme yield of 0.56 +/- 0.03 U ml(-1) at 20 g l(-1). This was about 1.70-fold higher than that obtained by free cells. The immobilized cells produced tannase consistently over 13 repeated cycles and reached a maximum level at the third cycle. Scanning electron microscope study indicated that the cells in Ca-alginate beads remain in normal shape. CONCLUSIONS: The Ca-alginate entrapment is a promising immobilization method of B. licheniformis KBR6 for repeated tannase production. Tannase production by immobilized cells is superior to that of free cells because it leads to higher volumetric activities within the same period of fermentation. SIGNIFICANCE AND IMPACT OF THE STUDY: This is the first report of tannase production from immobilized bacterial cells. The bacterium under study can produce higher amounts of tannase with respect to other fungal strains within a short cultivation period.     

ε-Poly-<Emphasis Type="SmallCaps">l</Emphasis>-lysine: microbial production,biodegradation and application potential

epsilon-Poly-L-lysine (epsilon-PL) is a homo-poly-amino acid characterized by the peptide bond between the carboxyl and epsilon-amino groups of L-lysine. epsilon-PL shows a wide range of antimicrobial activity and is stable at high temperatures and under both acidic and alkaline conditions. The mechanism of the inhibitory effect of epsilon-PL on microbial growth is the electrostatic adsorption to the cell surface of microorganisms on the basis of its poly-cationic property. Due to this antimicrobial activity, epsilon-PL is now industrially produced in Japan as a food additive by a fermentation process using Streptomyces albulus. In spite of the practical application of epsilon-PL, the biosynthetic mechanisms of epsilon-PL have not been clarified at all. epsilon-PL producers commonly possess membrane-bound epsilon-PL-degrading aminopeptidase, which might play a role in self-protection.     

Tagatose production by immobilized recombinant Escherichia coli cells containing Geobacillus stearothermophilus l-arabinose isomerase mutant in a packed-bed bioreactor

Using immobilized recombinant Escherichia coli cells containing Geobacillus stearothermophilus l-arabinose isomerase mutant (Gali 152), we found that the galactose isomerization reaction was maximal at 70 degrees C and pH 7.0. Manganese ion enhanced galactose isomerization to tagatose. The immobilized cells were most stable at 60 degrees C and pH 7.0. The cell and substrate concentrations and dilution rate were optimal at 34 g/L, 300 g/L, and 0.05 h(-1), respectively. Under the optimum conditions, the immobilized cell reactor with Mn2+ produced an average of 59 g/L tagatose with a productivity of 2.9 g/L.h and a conversion yield of 19.5% for the first 20 days. The operational stability of immobilized cells with Mn2+ was demonstrated, and their half-life for tagatose production was 34 days. Tagatose production was compared for free and immobilized enzymes and free and immobilized cells using the same mass of cells. Immobilized cells produced the highest tagatose concentration, indicating that cell immobilization was more efficient for tagatose production than enzyme immobilization.     

Cell immobilization technique for the enhanced production of alpha-galactosidase by Streptomyces griseoloalbus

Streptomyces griseoloalbus was immobilized in calcium alginate gel and the optimal immobilization parameters (concentrations of sodium alginate and calcium chloride, initial biomass and curing time) for the enhanced production of alpha-galactosidase were determined. The immobilization was most effective with 3% sodium alginate and 0.1M calcium chloride. The optimal initial biomass for immobilization was approximately 2.2g (wet wt.). The alginate-entrapped cells were advantageous because there was a twofold increase in the enzyme yield (55 U/ml) compared to the highest yield obtained with free cells (23.6 U/ml). Moreover, with immobilized cells the maximum yield was reached after 72 h of incubation in batch fermentation under optimal conditions, whereas in the case of free cells the maximum enzyme yield was obtained only after 96 h of incubation. The alginate beads had good stability and also retained 75% ability of enzyme production even after eight cycles of repeated batch fermentation. It is significant that this is the first report on whole-cell immobilization for alpha-galactosidase production.     

脂肪酶的固定化及其性质研究

采用吸附与交联相结合的方法国定化脂肪酶,研究了脂肪酶固定化的工艺条件,并考察了固定化脂肪酶的催化性能和稳定性。试验结果表明,WA20树脂固定化脂肪酶的最适条件是：酶液pH7．0、给酶量300IU／g树脂、固定时间8h,所得固定化脂肪酶的活力约为165IU／g树脂;固定化酶稳定性较高,在冰箱内贮存6个月活力没有下降,操作半衰期约为750h,而未用戌二醛文联的固定化脂肪酶操作半衰期仅约290h;固定化脂肪酶催化橄榄油水解的最适条件是：PH8．0、温度55℃、底物浓度60％（V／V）、搅拌转速500r／m。     

Loofa (Luffa cylindrica) sponge: Review of development of the biomatrix as a tool for biotechnological applications

The review discusses the development of loofa sponge (Luffa cylindrica) as a biotechnological tool and the diversity of applications in which it has been successfully used since it was first reported as a matrix for the immobilization of microbiological cells in 1993. The fibro‐vascular reticulated structure, made up of an open network of random lattices of small cross‐sections coupled with very high porosity (79–93%), having very low density (0.02–0.04 g/cm³), and high specific pore volume (21–29 cm³/g), has the characteristics of a carrier/scaffold well‐suited for cell immobilization. This has been confirmed through the immobilization of cells of diverse types, including filamentous and microalgae, fungi, bacteria, yeasts, higher plants, and human and rat hepatocytes. The cells immobilized in loofa sponge have performed well and better than free suspended cells and those immobilized in conventionally used natural and synthetic polymeric materials for the production of ethanol, organic acids, enzymes, and secondary metabolites. The loofa‐immobilized cell systems have been efficiently used for the treatment of wastewaters containing toxic metals, dyes, and chlorinated compounds, and the technology has been used to develop biofilms for the remediation of domestic and industrial wastewaters rich in inorganic and organic matter. In addition, three‐dimensional loofa sponge scaffolds for hepatocyte culture have been suggested to have the potential for development into a bioartificial liver device. Loofa sponge is a cost‐effective, eco‐friendly, and easy to handle matrix that has been used successfully as a biotechnological tool in a variety of systems, purposes, and applications. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:573–600, 2013     

Scale up of fuel ethanol production from sugar beet juice using loofa sponge immobilized bioreactor

Production of fuel ethanol from sugar beet juice, using cells immobilized on loofa sponge was investigated. Based on ethanol productivity and ease of cell immobilization, a flocculating yeast strain, Saccharomyces cerevisiae IR2 was selected for ethanol production from sugar beet juice. It was found that raw sugar beet juice was an optimal substrate for ethanol production, requiring neither pH adjustment nor nitrogen source supplement. When compared with a 2 l bubble column bioreactor, mixing was not sufficient in an 8 l bioreactor containing a bed of sliced loofa sponges and consequently, the immobilized cells were not uniformly distributed within the bed. Most of the cells were immobilized in the lower part of the bed and this resulted in decreased ethanol productivity. By using an external loop bioreactor, constructing the fixed bed with cylindrical loofa sponges, dividing the bed into upper, middle and lower sections with approximately 1 cm spaces between them and circulating the broth through the loop during the immobilization, uniform cell distribution within the bed was achieved. Using this method, the system was scaled up to 50 l and when compared with the 2 l bubble column bioreactor, there were no significant differences (P > 0.05) in ethanol productivity and yield. By using external loop bioreactor to immobilize the cells uniformly on the loofa sponge beds, efficient large scale ethanol production systems can be constructed.     

Comparative study of d-xylose conversion to ethanol by immobilized growing or non-growing cells of the yeast Pachysolen tannophilus

Summary The direct conversion of d-xylose to ethanol was investigated using immobilized growing and non-growing cells of the yeast Pachysolen tannophilus. Both preparations produced ethanol from d-xylose, however the d-xylose conversion to ethanol was much better with immobilized growing cells. Ethanol concentration up to 22.9 g/l and ethanol yield of 0.351 g/g of d-xylose were obtained in batch fermentation by immobilized growing cells whereas only 17.0 g/l and 0.308 g/g of d-xylose were obtained by immobilized non-growing cells. With continuous systems, immobilized growing cells were necessary for the long-term operation, since a steady state ethanol concentration of 17.7 g/l was maintained for only one week by immobilized non-growing cell reactor. With simultaneous control of aeration rate and concentrations of nitrogen sources in feed medium, immobilized growing cells of P. tannophilus showed excellent performance. At a residence time of 25 h, the immobilized cell reactor produced 26.9 g/l of ethanol from 65 g/l of d-xylose in feed medium.     

Production of butanol from glucose and xylose with immobilized cells of Clostridium acetobutylicum

Pretreated cotton towels were used as carriers to immobilize Clostridium acetobutylicum CGMCC 5234 cells for butanol or ABE production from glucose and xylose. Results showed that cell immobilization was a promising method to increase butanol concentration, yield and productivity regardless of the sugar sources compared with cell suspension. In this study, a high butanol concentration of 10.02 g/L with a yield of 0.20 g/g was obtained from 60 g/L xylose with 9.9 g/L residual xylose using immobilized cells compared with 8.48 g/L butanol and a yield of 0.141 g/g with 20.2 g/L residual xylose from 60 g/L xylose using suspended cells. In mixed-sugar fermentation (30 g/L glucose plus 30 g/L xylose), the immobilized cultures produced 11.1 g/L butanol with a yield of 0.190 g/g, which were 28.3% higher than with suspended cells (8.65 g/L) during which 30 g/L glucose was utilized completely using both immobilized and suspended cells while 3.46 and 13.1 g/L xylose maintained untilized for immobilized and suspended cells, respectively. Based on the results, we speculated that immobilized cells showed enhanced tolerance to butanol toxicity and the cultures preferred glucose to xylose during ABE fermentation. Moreover, the cultures showed obvious difference when grown between high initial concentrations of glucose and those of xylose. Repeated-batch fermentations from glucose with immobilized cells showed better long-term stability than from xylose. At last, the morphologies of free and immobilized cells adsorbed on pretreated cotton towels during the growth cycle were examined by SEM.     

Influence of phenol on the biodegradation of pyridine by freely suspended and immobilized Pseudomonas putida MK1

AIMS: To study the effect of co-contaminants (phenol) on the biodegradation of pyridine by freely suspended and calcium alginate immobilized bacteria. METHODS AND RESULTS: Varying concentrations of phenol were added to free and calcium alginate immobilized Pseudomonas putida MK1 (KCTC 12283) to examine the effect of this pollutant on pyridine degradation. When the concentration of phenol reached 0.38 g l(-1), pyridine degradation by freely suspended bacteria was inhibited. The increased inhibition with the higher phenol levels was apparent in increased lag times. Pyridine degradation was essentially completely inhibited at 0.5 g l(-1) phenol. However, immobilized cells showed tolerance against 0.5 g l(-1) phenol and pyridine degradation by immobilized cell could be achieved. CONCLUSIONS: This works shows that calcium alginate immobilization of microbial cells can effectively increase the tolerance of P. putida MK1 to phenol and results in increased degradation of pyridine. SIGNIFICANCE AND IMPACT OF THE STUDY: Treatment of wastewater stream can be negatively affected by the presence of co-pollutants. This work demonstrates the potential of calcium alginate immobilization of microbes to protect cells against compound toxicity resulting in an increase in pollutant degradation.     

Continuous methane fermentation and the production of vitamin B12 in a fixed-bed reactor packed with loofah

A fixed-bed reactor with acclimated methanogens immobilized on a loofah support was studied on a laboratory scale to evaluate the system producing methane from the mixture of CO(2) and H(2) gas, with the production of vitamin B(12) as a by-product. Fermentation using CO(2)/H(2) acclimated methanogens was conducted in a jar fermentor with hydraulic retention times (HRTs) of three and six days. The performance of the reactor was mainly dependent on the HRT. With an HRT of three days, the methane production rate and the vitamin B(12) concentration in the culture broth were 6.18 l/l-reactor/h and 2.88 mg/l-culture liquid; these values were 11.96 l/l-reactor/h and 37.54 mg/l-culture liquid for an HRT of six days. A higher total cell mass of methanogens retained 42.5 g dry cell/l-culture liquid was achieved in the HRT of six days. The loofah carrier immobilized almost 95% of the methanogens, which led to a more effective bio-reaction. It was also observed that the fermentation system had a better ability to buffer pH, especially for an HRT of six days.