Heating cell immobilization of Streptomyces griseus and its variant for economical fructose production

Aims@#This study determined the optimum temperature for cell immobilization, the optimum time of fructose production by immobilized cell, and immobilized cell stability against repeated use in fructose production. @*Methodology and results@#Research on cell immobilization of Streptomyces griseus and the variant have been done. The S. griseus variant was resulted from UV mutation. The variant was able to produce fructose as hydrolysis product 3 times as much after 30 min. Heating was done at 50, 60, 70, 80 and 90 °C. The fructose production was performed at intervals of 4 h for 32 h. The results showed that the optimum cell immobillization temperature of S. griseus and its variant was 80 °C. The optimum time of fructose production by immobilizing cell of S. griseus was 28 h and its variant cells was 24 h. Immobilized cells of S. griseus can be reused for 6 × 28 h to produce fructose compared to variants cells was 5 × 24 h, respectively. @*Conclusion, significance and impact of study@#This study reported that immobilized cells of S. griseus can be reused and its variant were highly advantageous in the production of fructose. The amount of fructose production was increased as compared to the conventional method and the cost of production could be reduced as well.

Poly(DL-lactide)-degrading enzyme production by immobilized Actinomadura keratinilytica strain T16-1 in a 5-L fermenter under various fermentation processes

Background: Poly(DL-lactic acid), or PDLLA, is a biodegradable polymer that can be hydrolyzed by various types of enzymes. The protease produced by Actinomadura keratinilytica strain T16-1 was previously reported to have PDLLA depolymerase activity. However, few studies have reported on PDLLA-degrading enzyme production by bacteria. Therefore, the aims of this study were to determine a suitable immobilization material for PDLLA-degrading enzyme production and optimize PDLLA-degrading enzyme production by using immobilized A. keratinilytica strain T16-1 under various fermentation process conditions in a stirrer fermenter. Results: Among the tested immobilization materials, a scrub pad was the best immobilizer, giving an enzyme activity of 30.03 U/mL in a shake-flask scale. The maximum enzyme activity was obtained at aeration 0.25 vvm, agitation 170 rpm, 45°C, and 48 h of cultivation time. Under these conditions, a PDLLA-degrading enzyme production of 766.33 U/mL with 15.97 U/mL·h productivity was observed using batch fermentation in a 5-L stirrer fermenter. Increased enzyme activity and productivity were observed in repeated-batch (942.67 U/mL and 19.64 U/mL·h) and continuous fermentation (796.43 U/mL and 16.58 U/mL·h) at a dilution rate of 0.013/h. Scaled-up production of the enzyme in a 10-L stirrer bioreactor using the optimized conditions showed a maximum enzyme activity of 578.67 U/mL and a productivity of 12.06 U/mL·h. Conclusions: This research successfully scaled-up the enzyme production to 5 and 10 L in a stirrer fermenter and is helpful for many applications of poly(lactic acid).

Biovalorization potential of peels of Ananas cosmosus (L.) Merr. for ethanol production by Pichia stipitis NCIM 3498 & Pachysolen tannophilus MTCC 1077.

Bioethanol, is a potential alternate source of energy, renewable and safe. Ethanol production from value added food and feedstock has also not shown growth as estimated. Of late, the second generation processes of production of ethanol, such as from lignocellulosic biomass out of agricultural/domestic waste has been gaining considerable momentum. Here, we explored a new approach for optimizing the conditions of physiochemical pretreatment as well as fermentation process using peels of Ananas cosmosus as substrate and immobilized yeast Pachysolen tannophilus MTCC 1077 and Pichia stipitis NCIM 3498. We have also studied the influence of process variables such as incubation temperature, inoculum concentration and different nutrients on ethanol production. Pulverized peels of A. cosmosus recorded 25 ± 0.31% cellulose, 28 ± 0.18% hemicellulose and 8 ± 0.07% of lignin on dry solid (DS) basis. Peels of A. cosmosus delignified with 1% H2SO4 yielded 18.89% glucose, 38.81% xylose and 29.31% fructose under thermochemical pretreatment using autoclave (121°C, 20 min.), with a hydrolytic efficiency of 75.52 ± 0.45%. FTIR spectroscopy results not only indicated the penetration of H2SO4 in the amorphous region of the biomass and degradation of hemicelluloses but also showed the structural differences before and after pretreatment. The enzymes required for hydrolysis were prepared from culture supernatants of Trichoderma reesei NCIM 1052 using wheat bran as carbon source under submerged fermentation conditions on rotatory shaker incubator (at 28°C for 10 days ). Enzyme activity (U/ml) of crude cellulase produced by T. reesei NCIM 1052 was 311.1 µmole/ml/min. Delignified A. cosmosus peel yielded 51.71 ± 0.44 g/l glucose when enzymatically hydrolysed by crude cellulase at the substrate enzyme ratio of 1:5. Simultaneous saccharification and fermentation (SSF) of peels of A. cosmosus by crude cellulase and separately entrapped Pichia stipitis NCIM 3498 (now known as Scheffersomyces stipitis) and Pachysolen tannophilus MTCC 1077 cells in calcium alginate beads were also investigated in the present study. The fermentation experiments were carried out at flask level. The processing parameters setup for reaching a maximum response for ethanol production was obtained when applying the optimum values for temperature (32°C), inoculum level (6%) and fermentation medium (ammonium sulphate, KH2PO4, peptone and yeast extract) for P. tannophilus MTCC 1077 and temperature (30°C), inoculum level (2%) and fermentation medium (ammonium sulphate, KH2PO4, peptone and yeast extract) for S. stipitis NCIM 3498. Maximum ethanol concentration 10.5 g/l and 10.9 g/l was obtained from P. tannophilus MTCC 1077 and S. stipitis NCIM 3498, respectively at the optimized process conditions in anaerobic batch fermentation.

Enhancement of chitosanase production by cell immobilization of Gongronella sp. JG

Chitosanase production of Gongronella sp. JG cells immobilized in calcium alginate gel and polyurethane foam was compared with that of the free cells, there was a 60% increase in the enzyme yield (2429 U/L) compared to the highest yield obtained from free cells (1513 U/L). The optimal immobilization parameters (concentrations of sodium alginate, calcium chloride, bead inoculums, bead diameter, etc) for the enhanced production of chitosanase were determined as: sodium alginate 2% (w/v), 0.1 M calcium chloride, inoculum 10 mL beads to 100 mL production media and 2.7 mm bead diameter. Maximum chitosanase production was achieved with initial pH of 5.5 and temperature of 30 ºC. The alginate beads had well stability, retained 85% ability of enzyme production even after 7 cycles of repeated batch fermentation. These results showed the immobilization technique was a feasible and economical method for chitosansase production by Gongronella sp. JG.

Ethanol fermentation of sugarcane molasses by Zymomonas mobilis MTCC 92 immobilized in Luffa cylindrica L. sponge discs and Ca-alginate matrices

Bio-ethanol production from cane molasses (diluted to 15 % sugar w/v) was studied using the bacterium, Zymomonas mobilis MTCC 92 entrapped in luffa (Luffa cylindrica L.) sponge discs and Ca-alginate gel beads as the immobilizing matrices. At the end of 96 h fermentation, the final ethanol concentrations were 58.7 ± 0.09 and 59.1 ± 0.08 g/l molasses with luffa and Ca-alginate entrapped Z. mobilis cells, respectively exhibiting 83.25 ± 0.03 and 84.6 ± 0.02 % sugar conversion. There was no statistical significant difference (Fischer's LSD) in sugar utilization (t = 0.254, p <0.801) and ethanol production (t =-0.663, p <0.513) between the two immobilization matrices used. Further, the immobilized cells in both the matrices were physiologically active for three more cycles of operation with less than 15 % decrease in ethanol yield in the 4th cycle, which was due to some leakage of cells. In conclusion, luffa sponge was found to be equally good as Ca-alginate as a carrier material for bacterial (Z. mobilis. cell immobilization for ethanol production. Further, it has added advantages such as it is cheap, non-corrosive and has no environmental hazard.

Production of Halophilic α-Amylase by Immobilized Cells of Moderately Halophilic Bacillus sp. Strain TSCVKK.

Aims: To investigate the effect of cell immobilization on amylase production by the moderately halophilic bacterium, Bacillus sp. strain TSCVKK and to compare the properties of the amylase produced under immobilized conditions with the enzyme produced by the free cells. Study Design: Cell immobilization. Place and Duration of Study: Department of Chemistry, Biochemistry Lab, Indian Institute of Technology (IIT Madras), Chennai, Tamil Nadu, between Jan 2009 and March 2009. Methodology: Bacillus sp. strain TSCVKK was immobilized in alginate, agar, polyacrylamide and gelatin. Production of amylase was determined using 3, 5- dinitrosalicylic acid (DNS). Effect of NaCl, pH, temperature on the activity of amylase was determined and compared with the amylase produced by the free cells. Results: Maximum production of 832 mU/ml was achieved with an initial cell load of 1.2% (w/v; wet weight) of 24 h grown cells immobilized in 2% agar of 4 mm3 block size using GSL-2 medium containing 10% NaCl and 1.5% dextrin at pH 8.0 at 30ºC after 36 h of growth. Amylase production was lower when the cells were immobilized in alginate (211 mU/ml) or with the free cells of same biomass concentration as used for immobilization (333 mU/ml). Amylase was not produced when gelatin or polyacrylamide was used as the immobilization matrix. The immobilized cells in 2% agar could be used up to 5 cycles without much reduction in amylase production. Amylase produced through cell immobilization retained all the properties that were shown by amylase produced under submerged fermentation. Conclusion: Agar was the suitable matrix to immobilize Bacillus sp. strain TSCVKK for amylase production. Amylase produced under immobilization conditions retained its temperature, salt and pH requirements. Immobilized cells were used for 5 cycles without much decrease in production.

Biodegradation kinetics of o-cresol by Pseudomonas putida DSM 548 (pJP4) and o-cresol removal in a batch-recirculation bioreactor system

The biodegradation kinetics of o-cresol was examined by acclimatized P. putida DSM 548 (pJP4) in batch experiments at varying initial o-cresol concentrations (from 50 to 500 mg/L). The kinetic parameters of o-cresol aerobic biodegradation were estimated by using the Haldane substrate inhibition equation. The biodegradation kinetics of o-cresol was investigated. In batch culture reactors, the Maximum specific growth rate (μmax), Monod constant (Ks) and the inhibition constant (Ki) were established as 0.519 h-1, 223.84 mg/L and 130.883 mg/L, respectively. o-cresol biodegradation in a batch-recirculation bioreactor system by immobilized P. putida was also studied. The recycled packed bed reactor system, which was composed of Ca-alginate beads and pumice on which cells immobilized, has been performed to determine possible stability for further developments.

Glucosyltransferase production by Klebsiella sp. K18 and conversion of sucrose to palatinose using immobilized cells / Produção de glicosiltransferase por Klebsiella sp. K18 e conversão de sacarose em palatinose utilizando células imobilizadas

The strain Klebsiella sp. K18 produces the enzyme glucosyltransferase and catalyses the conversion of sucrose to palatinose, an alternative sugar that presents low cariogenicity. Response Surface Methodology was successfully employed to determine the optimal concentration of culture medium components. Maximum glucosyltransferase production (21.78 U mL-1) was achieved using the optimized medium composed by sugar cane molasses (80 g L-1), bacteriological peptone (7 g L-1) and yeast extract (20 g L-1), after 8 hours of fermentation at 28ºC. The conversion of sucrose to palatinose was studied utilizing immobilized cells in calcium alginate. The effects of the alginate concentration (2-4%), cell mass concentration (20-40%) and substrate concentration (25-45%) were evaluated and the yield of palatinose was approximately 62.5%.

A linhagem Klebsiella sp. K18 produz a enzima glicosiltransferase que catalisa a conversão de sacarose em palatinose, um açúcar alternativo que apresenta baixa cariogenicidade. Metodologia de Superfície de Resposta foi empregada com sucesso para determinar a concentração ótima dos componentes do meio de cultivo. A máxima produção deglicosiltransferase (21,78 U mL-1) foi obtida utilizando o meio de cultivo otimizado composto por melaço de cana de açúcar (80 g L-1), peptona bacteriológica (7 g L-1) e extrato de levedura (20 g L-1), após 8 horas de fermentação a 28ºC. A conversão desacarose em palatinose foi estudada utilizando células imobilizadas em alginato de cálcio. Os efeitos da concentração de alginato (2-4%), concentração de massa celular (20-40%) e concentração de substrato (25-45%) foram avaliados e a porcentagem de palatinose foi de aproximadamente 62,5%.