固定化乳酸乳球菌连续生产Nisin的研究

以海藻酸钙为材料 ,固定乳酸乳球菌 (Lactococcuslactissubsp .lactis)SM5 2 6 ,研究不同条件对Nisin合成的影响。结果表明 ,利用 2 %海藻酸钠在 1 0mmol LCaCl2 条件下 ,得到的固定化细胞颗粒稳定性较好 ,可维持 90h无破裂 ;在发酵过程中SYS3培养基中的无机盐成分尤其磷酸盐对固定化颗粒有破坏作用 ;用mSYS3培养基代替SYS3 ,通过 72h三批次循环的半连续培养 ,Nisin活性为 85 0IU mL ,无明显的细胞渗漏现象。连续化生产 70h ,Nisin活性达 1 1 5 0IU mL ,相当于游离细胞的发酵水平。     

Effect of environmental growth conditions on plasmid stability, plasmid copy number, and catechol 2,3-dioxygenase activity in free and immobilized Escherichia coli cells

In order to better understand the high plasmid stability in immobilized recombinant E. coli cells, the effects of dilution rate on the pTG201 plasmid stability, the copy number, and the catechol 2,3-dioxygenase (encoded by XyIE gene) production were, at first, studied in free E. coli W3101 continuous cultures in minimal media. It was found that decreasing specific growth rate increased the plasmid copy number and the catechol 2,3-dioxygenase activity but the stability decreased. In continuous culture with immobilized cells, an increase was shown in plasmid copy number and catechol 2,3-dioxygenase activity probably due to the distribution of growth in the gel beads. Besides mechanical properties of gel beads which may allow limited cell divisions, the increase in plasmid copy number is involved in enhanced plasmid stability in immobilized cells. In the same way, an experiment conducted in LB medium dealing with competition between pTG201-free and pTG201-containing E. coli B cells was described. It was shown that the competition was not more pronounced in gel bead compared to a free system. The effects of nutritional limitations on pTG201 plasmid stability and catechol 2,3-dioxygenase activity during chemostat cultivations in free and immobilized E. coli B cells were also investigated. It was found that immobilization of cells increased the stability of pTG201 even under glucose, nitrogen, or phosphate limited cultures. However in the case of magnesium depleted culture, pTG201 was shown to be relatively instable and a decrease in viable cell number during the immobilized continuous culture was observed. By contrast to the free system, the catechol 2,3-dioxygenase activity increased in immobilized cells under all culture conditions used.     

Agitation rate effects on plasmid stability in immobilized and free-cell continuous cultures of recombinant E. coli.

Escherichia coli B/pTG201 recombinant cells were immobilized by entrapment in a carrageenan gel and cultivated in nonselective media to investigate the effect of agitation rate on plasmid stability, biomass concentration, and enzyme productivity. These parameters were studied in continuous cultures for free and immobilized cells, respectively. Immobilized recombinant cells exhibit an increase in the stability of the plasmid pTG201 compared to free cells, even under conditions where the tendency of plasmid stability for free cells decreased generally more rapidly under a higher agitation rate. Intensive agitation, resulting also in a strong shear stress, greatly reduced cell concentration within gel beads throughout the course of growth. Higher enzyme expression of catechol 2–3, dioxygenase was also obtained in leaked cells due to better maintenance of plasmid stability and higher plasmid copy number with regard to free cells. Enzyme productivity of leaked and free cells in minimal medium decreased with the increase in agitation rate, due to decreased plasmid stability; however, in LB medium, it increased in the presence of higher agitation rate related to important cell concentration.     

Degradation of methyl tert-butyl ether by gel immobilized Methylibium petroleiphilum PM1

Cells of Methylibium petroleiphilum PM1 were immobilized in gel beads to degrade methyl tert-butyl ether (MTBE). Calcium alginate, agar, polyacrylamide and polyvinvyl alcohol were screened as suitable immobilization matrices, with calcium alginate demonstrating the fastest MTBE-degradation rate. The rate was accelerated by 1.8-fold when the beads had been treated in physiological saline for 24h at 28 degrees C. MTBE degradation in mineral salts medium (MSM) was accompanied by the increase of biomass. The half-life of MTBE-degradation activity for the encapsulated cells stored at 28 degrees C was about 120 h, which was obviously longer than that of free cells (approximately 36 h). Efficient reusability of the beads up to 30 batches was achieved in poor nutrition solution as compared to only 6 batches in MSM. The immobilized cells could be operated in a packed-bed reactor for degradation of 10 mg L(-1) MTBE in groundwater with more than 99% removal efficiency at hydraulic retention time of 20 min. These results suggested that immobilized cells of PM1 in bioreactor might be applicable to a groundwater treatment system for the removal of MTBE.     

Agitation rate effects on plasmid stability in immobilized and free-cell continuous cultures of recombinant E. coli

Escherichia coli B/pTG201 recombinant cells were immobilized by entrapment in a carrageenan gel and cultivated in nonselective media to investigate the effect of agitation rate on plasmid stability, biomass concentration, and enzyme productivity. These parameters were studied in continuous cultures for free and immobilized cells, respectively. Immobilized recombinant cells exhibit an increase in the stability of the plasmid pTG201 compared to free cells, even under conditions where the tendency of plasmid stability for free cells decreased generally more rapidly under a higher agitation rate. Intensive agitation, resulting also in a strong shear stress, greatly reduced cell concentration within gel beads throughout the course of growth. Higher enzyme expression of catechol 2–3, dioxygenase was also obtained in leaked cells due to better maintenance of plasmid stability and higher plasmid copy number with regard to free cells. Enzyme productivity of leaked and free cells in minimal medium decreased with the increase in agitation rate, due to decreased plasmid stability; however, in LB medium, it increased in the presence of higher agitation rate related to important cell concentration.     

Continuous stereospecific Δ-3-keto-steroid reduction by PAAH bead-entrapped Clostridium paraputrificum cells

The development of a continuous anaerobic process for stereospecific Δ⁴-3-keto-steroid reduction by immobilized Clostridium paraputrificum cells cells is described. Following a study on conditions for cell growth and sporulation, spores of C. paraputrificum were aseptically immobilized in PAAH beads. Conditions for cell growth and induction in the immobilized state were determined, as well as the medium composition required to maintain a stabilized immobilized cell population. The effect of the concentration of ethylene glycol added as selected cosolvent on reaction kinetics, substrate solubility, specific activity, and cell growth, was investigated. A 10% (v/v) cosolvent input provided maximal activity along with enhanced solubility of the steroidal substrate. It was shown that cell growth was enhanced in the presence of the added cosolvent in addition to its effect on substrate solubility and enzymic activity. The immobilized cells readily performed Δ⁴, as well as 3-keto steroid reduction of several steroids, including ADD, AD, 16-dehydroprogesterone, progesterone, and hydrocortisone. It was shown that repeated batch-wise reduction cycle—in the presence of the cosolvent—resulted in rapid loss of activity, while the continuous uninterrupted process permitted the attaining of full bioconversion level, maintained stable for at least the period of 5 days of continuous operation tested.     

Hydrogen peroxide degradation by immobilized cells of alkaliphilic Bacillus halodurans

Whole cells of Bacillus halodurans LBK 261 were used as a source of catalase for degradation of hydrogen peroxide. The organism, B. halodurans grown at 55°C and pH 10, yielded a maximum catalase activity of 275 U g^-1 (wet wt.) cells. The catalase in the whole cells was active over a broad range of pH with a maximum at pH 8-9. The enzyme was optimally active at 55°C, but had low stability above 40°C. The whole cell biocatalyst exhibited a K_m of 6.6 mM for H₂O₂ and V_max of 707 mM H₂O₂ min^-1 g^-1 wet wt. cells, and showed saturation kinetics at 50 mM H₂O₂. The cells were entrapped in calcium alginate and used for H₂O₂ degradation at pH 9 in batch and continuous mode. In the batch process, the immobilized preparation containing 1.5 g (wet wt.) cells could be recycled at least four times for complete degradation of the peroxide in 50 mL solution at 25°C. An excess of immobilized biocatalyst could be used in a continuous stirred tank reactor for an average of 9 days at temperatures upto 55°C, and in a packed bed reactor (PBR) for 5 days before the beads started to deform.     

Phytate degradation by immobilized<Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> phytase in soybean-curd whey

Saccharomyces cerevisiae CY phytase-producing cells were immobilized in calcium alginate beads and used for the degradation of phylate. The maximum activity and immobilization yield of the immobilized phytase reached 280 mU/g-bead and 43%, respectively. The optimal pH of the immobilized cell phytase was not different from that of the free cells. However, the optimum temperature for the immobilized phytase was 50°C, which was 10°C higher than that of the free cells; pH and thermal stability were enhanced as a consequence of immobilization. Using the immobilized phytase, phytate was degraded in a stirred tank bioreactor. Phytate degradation, both in a buffer solution and in soybean-curd whey mixture, showed very similar trends. At an enzyme dosage of 93.9 mU/g-phytate, half of the phytate was degraded after 1 h of hydrolysis. The operational stability of the immobilized beads was examined with repeated batchwise operations. Based on 50% conversion of the phytate and five times of reuse of the immobilized beads, the specific degradation (g phytate/g dry cell weight) for the immobilized phytase increased 170% compared to that of the free phytase.     

亚栖热菌透性化细胞的耦合固定化研究

将海藻酸盐凝胶包埋法与交联法和聚电解质静电自组装覆膜法相耦合,对含有海藻糖合酶活性的亚栖热菌的透性化细胞进行了固定化研究。结果表明,利用重氮树脂和聚苯乙烯磺酸钠对海藻酸凝胶微球交替覆膜,可以显著提高凝胶微球在磷酸盐缓冲液中的稳定性,以碳二亚胺对固定化细胞进行交联处理则可以提高固定化细胞中海藻糖合酶的热稳定性。透性化细胞经包埋－交联－覆膜耦合固定化后,酶活回收率为32％,最适酶反应pH值由6.5左右升至7.0左右,最适反应温度未变,仍为60℃。所得固定化细胞间歇反应时,催化麦芽糖转化为海藻糖的转化率可达60％,重复使用4次（每次50℃、反应24h）,酶活损失小于20％,转化率可保持在50％以上。     

Biofilm of Pseudomonas C12B on glass support as catalytic agent for continuous SDS removal

The purpose of this work was to investigate the biodegradation of Sodium dodecylsulphate, a common surfactant used in commercial detergent formulations, by immobilized cells of the surfactant-degrading bacterium Pseudomonas C12B. Cells were immobilized by adsorption on porous glass beads with either unmodified or silanized surface. Data showed a direct relation between the SDS concentration in the medium and formation of the biofilm on glass beads. Bioreactors with Pseudomonas C12B cells immobilized on both types of porous glass beads were prepared. Both types showed equivalent efficiency to remove SDS. This biocatalyst was also effective to remove anionic surfactants from commercial dishwashing liquid (Jar) and shampoo (Clear) under continuous operation.     

Influence of oxygen supply on the stability of recombinant plasmid pTG201 in immobilized E. coli cells

Summary Cells of Escherichia coli K12, carrying the recombinant plasmid pTG201, were immobilized in -carrageenan gel in order to improve the following plasmid parameters: (i) maintenance of a high level of plasmid copy number, (ii) good plasmid stability and (iii) good expression of plasmid encoded gene. The experiments were carried out on LB medium without antibiotic selection in continuous and batch cultures supplied with air or pure oxygen. Parallel experiments with free cells were also performed. In all the cases immobilized cells presented better plasmid stability parameters than free cells. Best results were obtained with immobilized cells supplied with pure oxygen. In this case, an average plasmid copy number of 60 and a value of plasmid-carrying cells close to 100% were maintained with little change during more than 200 generations. In addition, an optical microscopy analysis is proposed to allow the quantitation of cell growth in gel beads.     

PVA-biocatalyst with entrapped viable Bacillus subtilis cells

Bacillus subtilis cells were entrapped in polyvinyl alcohol (PVA)-cryogel beads without decay in their viability and capability of secretion of proteolytic enzymes (metalloproteinase and subtilisin). Conditions for preparation of the PVA-biocatalyst with suitable stability and viability of B. subtilis cells were optimized. Diffusion of various compounds into the cryogel (sliced beads) has been monitored on-line using image analysis system. Optimal working conditions and kinetic constants for hydrolysis of proteins catalyzed by the PVA-biocatalyst containing whole B. subtilis cells were estimated. The PVA-biocatalyst was applied in the hydrolysis of casein. The productivity of the biocatalyst (expressed as an amount of liberated aromatic amino acids) reached a maximal level of 12 mg g⁻¹ h⁻¹. Composition of mixture of peptides was dependent on pH, concentrations of Na⁺ and glucose, and in the reaction milieu. Protein hydrolysates of desired composition can be obtained using B. subtilis viable cells immobilized in PVA-gel. Incubation of the immobilized cells in a nutrient medium with casein successfully regenerated proteolytic activity of the biocatalyst.     

Stabilizing hyperactivated lecitase structures through physical treatment with ionic polymers

Lecitase Ultra has been covalently immobilized on cyanogen bromide cross-linked 4% agarose (CNBr) beads, maintaining 70% of the initial activity. The activity of the immobilized enzyme was improved in the presence of Triton X-100, sodium dodecyl sulfate (SDS), and cetyltrimethyl ammonium bromide (CTAB) (e.g., up to 800% when using CTAB). However, CTAB and Triton X-100 presented a negative effect on enzyme stability even at low concentrations, and SDS cannot be used for a long time at 1% concentration. To maintain the hyperactivated conformation of the enzyme in the absence of detergent, ionic polymers were added during incubation of the immobilized enzyme in the presence of detergents. Coating the immobilized enzyme with polyethylenimine in aqueous buffer (PEI) produced a 3-fold increase in enzyme activity. However, in the presence of 0.1% SDS (v/v), this coating produced a 50-fold increase in enzyme activity. Using PEI and 0.01% (v/v) CTAB, the Lecitase activity decreased to 10%. Using irreversible inhibitors, it could be shown that the PEI/SDS-CNBr-Lecitase preparation allowed its catalytic Ser to be more accessible to the reaction medium than the unmodified CNBr-Lecitase.     

Semicontinuous and continuous production of penicillin-G by Penicillium chrysogenum cells immobilized in kappa-carrageenan beads

Conidia of Penicillium chrysogenum were immobilized in K-carrageenan beads and then incubated in a growth-supporting medium to yield a penicillin producing immobilized cell mass. These in situ grown immobilized cells were used for the semicontinuous (replacement cultures)and continuous (fluidized bioreactor culture) production of penicillin-G. When periodically replaced into a minimal production medium, immobilized cells exhibited a half-life for penicillin production which was ninefold greater than that exhibited by free cells. The half-life of penicillin production and the yield of penicillin from glucose in such a replacement culture were greatly affected by the frequency of replacement and by the production medium's pH and concentration of glucose, phosphate, and trace metal nutrients. A penicillin-producing continuous flow bioreactor (150 mL), employing immobilized cells, was operated for up to 16 days. The best specific penicillin productivity (1.2 mg/g cells/h)yield from glucose (7.0 mg/g glucose) and half-life of production (15 days) were obtained when the feed medium contained 10 g/L of glucose, the pH was maintained at 7.0, the relative dissolved oxygen concentration was ca. 40%; and the residence time was 20 h.     

Continuous ethanol production from Jerusalem artichoke tubers. II. Use of immobilized cells of Kluyveromyces marxianus

Kluyveromyces marxianus UCD (FST) 55-82 cells were immobilized in Na alginate beads and used in a packed-bed bioreactor system for the continuous production of ethanol from the extract of Jerusalem artichoke tubers. Volumetric ethanol productivities of 104 and 80 g ethanol/ L/h were obtained at 80 and 92% sugar utilization, respectively. The maximum volumetric ethanol productivity of the immobilized cell bioreactor system was found to be 15 times higher than that of an ordinary-stirred-tank (CST) bioreactor using cells of K. marxianus. The immobilized cell bioreactor system was operated continuously at a constant dilution rate of 0.66 h(-1) for 12 days resulting in only an 8% loss of the original immobilized cell activity, which corresponds to an estimated half-life of ca. 72 days. The maximum specific ethanol productivity and maximum specific sugar uptake rate of the immobilized cells were found to be 0.55 g ethanol/g/biomass/h and 1.21 g sugars/g biomass/h, respectively.     

Comparison of ferric iron generation by different species of acidophilic bacteria immobilized in packed-bed reactors

Flooded packed-bed bioreactors, prepared by immobilizing four different species of acidophilic iron-oxidizing bacteria on porous glass beads, were compared for their ferric iron-generating capacities when operated in batch and continuous flow modes over a period of up to 9 months, using a ferrous iron-rich synthetic liquor and acid mine drainage (AMD) water. The bacteria used were strains of Acidithiobacillus ferrooxidans, Leptospirillum ferrooxidans, a Ferrimicrobium-like isolate (TSTR) and a novel Betaproteobacterium (isolate PSTR), which were all isolated from relatively low-temperature mine waters. Three of the bacteria used were chemoautotrophs, while the Ferrimicrobium isolate was an obligate heterotroph. Greater biomass yields achievable with the Ferrimicrobium isolate resulted in greater iron oxidation efficiency in the newly commissioned bioreactor containing this bacterium, though long-term batch testing with organic carbon-free solution resulted in similar maximum iron oxidation rates in all four bioreactors. Two of the bioreactors (those containing immobilized L. ferrooxidans and Ferrimicrobium TSTR) were able to generate significantly lower concentrations of ferrous iron than the others when operated in batch mode. In contrast, when operated as continuous flow systems, the bioreactor containing immobilized PSTR was superior to the other three when challenged with either synthetic or actual AMD at high flow rates. The least effective bacterium overall was At. ferrooxidans, which has previously been the only iron-oxidizer used in the majority of reports describing ferric iron-generating bioreactors. The results of these experiments showed that different species of iron-oxidizing acidophiles have varying capacities to oxidize ferrous iron when immobilized in packed-bed bioreactors, and that novel isolates may be superior to well-known species.     

Degradation of benzene by a Rhodococcus sp. using immobilized cell systems

The continuous degradation of benzene by a Rhodococcus sp. using free and immobilized cell systems was compared. Cell entrapment in calcium and strontium alginate beads and adhesion on support materials such as glass beads were found to be unsatisfactory. Degradation of benzene by cells immobilized in either ceramic or cellulose carriers proved to be more efficient than its non-immobilized counterpart. A retention time of 36 h was required to effect a 97% degradation of benzene using suspended free cells while cells immobilized on cellulose or ceramic carriers effected 97% degradation at 24 and 18 h, respectively. Recycling of the ceramic carriers was also possible and resulted in an even shorter retention time of 12h to effect a 97% degradation of benzene. Cell adhesion on the support materials was confirmed by scanning electron microscopy.     

The production of ethanol by immobilized yeast cells

Saccharomyces cerevisiae cells were immobilized in calcium alginate beads for use in the continuous production of ethanol. Yeasts were grown in medium supplemented with ethanol to selectively screen for a culture which showed the greatest tolerance to ethanol inhibition. Yeast beads were produced from a yeast slurry containing 1.5% alginate (w/v) which was added as drops to 0.05M CaCl₂ solution. To determine their optimum fermentation parameters, ethanol production using glucose as a substrate was monitored in batch systems at varying physiological conditions (temperature, pH, ethanol concentration), cell densities, and gel concentration. The data obtained were compared to optimum free cell ethanol fermentation parameters. The immobilized yeast cells examined in a packed-bed reactor system operated under optimized parameters derived from batch-immobilized yeast cell experiments. Ethanol production rates, as well as residual sugar concentration were monitored at different feedstock flow rates.     

Studies on the enhanced production of extracellular lipase by Staphylococcus epidermidis

Staphylococcus epidermidis isolated from spoiled frozen marine fish samples exhibited optimum lipase activity of 8.1 U within 72 h in batch fermentation. Inducible effect of different sugars, nitrogen sources, salts and metal ions were studied on enzyme production. Trybutyrin induced the enzyme production by twofold. Addition of lactose in the production medium further improved lipase production. Sodium chloride increased lipase production whereas the presence of metals in the media had an inhibitory effect. Cells of immobilized S. epidermidis in agar beads (3%) increased lipase production compared with free cells. The optimum temperature and pH for enzyme activity was 20 degrees C and 7.0 respectively. Lipase retained its 85% stability at pH 6.0 and at 40 degrees C. Immobilized cells with high lipolytic activity and stability may provide commercial advantages over conventional methods of lipase production.     

Continuous alpha-amylase production using Bacillus amyloliquefaciens adsorbed on an ion exchange resin

Summary A method for the continuous production of extracellular alpha amylase by surface immobilized cells of Bacillus amyloliquefaciens NRC 2147 has been developed. A large-pore, macroreticular anionic exchange resin was capable of initially immobilizing an effective cell concentration of 17.5 g DW/1 (based on a total reactor volume of 160 ml). The reactor was operated continuously with a nutrient medium containing 15 g/l soluble starch, as well as yeast extract and salts. Aeration was achieved by sparging oxygen enriched air into the column inlet. Fermentor plugging by cells was avoided by periodically substituting the nutrient medium with medium lacking in both soluble starch and yeast extract. This fermentor was operated for over 200 h and obtained a steady state enzyme concentration of 18700 amylase activity units per litre (18.7 kU/l), and an enzyme volumetric productivity of 9700 amylase activity units per litre per hour (9.7 kU/l-h). Parallel fermentations were performed using a 2 l stirred vessel fermentor capable of operation in batch and continuous mode. All fermentation conditions employed were identical to those of the immobilized cell experiments in order to assess the performance of the immobilized cell reactor. Batch stirred tank operation yielded a maximum amylase activity of 150 kU/l and a volumetric productivity of 2.45 kU/l-h. The maximum cell concentration obtained was 5.85 g DW/l. Continuous stirred tank fermentation obtained a maximum effluent amylase activity of 6.9 kU/l and a maximum enzyme volumetric productivity of 2.73 kU/l-h. Both of these maximum values were observed at a dilution rate of 0.345 l/h. The immobilized cell reactor was observed to achieve larger volumetric productivities than either mode of stirred tank fermentation, but achieved an enzyme activity concentration lower than that of the batch stirred tank fermentor.