Protein production using recombinant yeast in an immobilized-cell-film airlift bioreactor

A recombinant Saccharomyces cerevisiae C468/pGAC9 (ATCC 20690), which expresses Aspergillus awamori glucoamylase gene under the control of the yeast enolase I (ENO1) promoter and secretes glucoamylase into the extracellular medium, was used as a model system to investigate the effect of cell immobilization on bioreactor culture performance. Free suspension cultures in stirred-tank and airlift bioreactors confirmed inherent genetic instability of the recombinant yeast. An immobilized-cell-film airlift bioreactor was developed by employing cotton cloth sheets to immobilize the yeast cells by attachment. Enhanced enzyme productivity and production stability in the immobilized-cell system were observed. Experimental data indicated that the immobilized cells maintained a higher proportion of plasmid-bearing cells for longer periods under continuous operation. The higher plasmid maintenance with immobilized cells is possibly due to reduced specific growth rate and increased plasmid copy number. Double-selection pressure was used to select and maintain the recombinant yeast. The selected strain showed better production performance than the original strain. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 241-251, 1997.     

Production of dextransucrase by Leuconostoc mesenteroides immobilized in calcium-alginate beads: I. Batch and fed-batch fermentations

In batch fermentation Leuconostoc mesenteroides immobilized in calcium alginate beads produced a total dextransucrase activity equal to about 93% of that by free, suspended bacterial cells under comparable conditions in a bubble column reactor. Continuous sucrose feeding (5 g/L h) to the immobilized-cell culture in the airlift bioreactor increased production of enzymatic activity by about 107% compared with ordinary batch operation of this reactor. About 14% of the enzymatic activity produced by the immobilized cells appears as soluble activity in the cell-free broth compared with about 40% in case of free cells. In an airlift bioreactor, both the soluble and the intact (sorbed and entrapped) enzymatic activity produced by the immobilized bacterial cells was about 34% greater under automatic pH control, compared to that produced in a bubble column reactor with only manual pH control. During formation of dextran by intact enzyme within cells and beads, declines are observed in apparent enzymatic activity.     

The continuous hydrolysis of geniposide to genipin using immobilized β-glucosidase on calcium alginate gel

Summary The reaction velocity of immobilized -glucosidase was approximated by the first-order reaction kinetics. A plug flow reactor was used for continuous hydrolysis of geniposide with this immobilized enzyme. The activity of this immobilized enzyme was retained 100% for 600 h. The amount of genipin formed by using the immobilized enzyme was 17 fold that formed using the native enzyme without reuse. Using immobilized enzyme, purity and yield of genipin, which is a hydrolyzate of geniposide, was improved comparing with the native enzyme.     

Continuous production ofL-malic acid by immobilizedBrevibacterium ammoniagenes cells

Summary Continuous production ofL-malic acid from fumaric acid using immobilized microbial cells was investigated. Several microorganisms having fumarase activity were immobilized into a polyacrylamide gel lattice. Among the microorganisms tested, immobilizedBrevibacterium ammoniagenes IAM 1645 showed the highest enzyme activity, but produced an unwanted by-product, succinic acid. Conditions for suppression of this side reaction were investigated, and bile extract treatment of immobilized cells was found to be effective.The bile extract treatment of immobilized cells also resulted in a marked increase of reaction rate forL-malic acid formation.No difference was observed between the native enzyme and immobilized cells in optimal pH and temperature of the enzyme reaction.The effect of temperature on the reaction rate and the stability of fumarase activity of an immobilized cell column were investigated under conditions of continuous enzyme reaction. The decay of enzyme activity during continuous enzyme reaction was expressed by an exponential relationship. Half-life of the fumarase activity of the immobilized cell column at 37°C was calculated to be 52.5 days.Presented at the Annual Meeting of the Society of Fermentation Technology, Japan, Osaka, Japan, October 30, 1975.     

Continuous biotransformation of glycopeptide antibiotic A40926 in a cascade of three airlift bioreactors using immobilized Actinoplanes teichomyceticus cells

Immobilized cells of Actinoplanes teichomyceticus ATCC 31121 were used to selectively cleave the acyl group of A40926 yielding the deacylated form of the molecule. The feasibility of this particular biotransformation in a series of three perfectly mixed airlift bioreactors with immobilized cells was examined. A continuously operated airlift cascade was designed using a model for a series of reactors with immobilized biocatalyst beads obeying Michaelis–Menten kinetics. In independent experimental runs the cascade bioreactor system was operated continuously for 56 days with an overall conversion of 99%. Model estimates for reactor volumes and relative conversions were found to be in a good agreement with the experimental results.     

Stability and reactivity of liposome‐encapsulated formate dehydrogenase and cofactor system in carbon dioxide gas‐liquid flow

Formate dehydrogenase from Candida boidinii (CbFDH) is potentially applicable in reduction of CO₂ through oxidation of cofactor NADH into NAD⁺. For this, the CbFDH activity needs to be maintained under practical reaction conditions, such as CO₂ gas‐liquid flow. In this work, CbFDH and cofactor were encapsulated in liposomes and the liposomal enzymes were characterized in an external loop airlift bubble column. The airlift was operated at 45°C with N₂ or CO₂ as gas phase at the superficial gas velocity U_G of 2.0 or 3.0 cm/s. The activities of liposomal CbFDH/cofactor systems were highly stable in the airlift regardless of the type of gas phase because liposome membranes prevented interactions of the encapsulated enzyme and cofactor molecules with the gas‐liquid interface of bubbles. On the other hand, free CbFDH was deactivated in the airlift especially at high U_G with CO₂ bubbles. The liposomal CbFDH/NADH could catalyze reduction of CO₂ in the airlift giving the fractional oxidation of the liposomal NADH of 23% at the reaction time of 360 min. The cofactor was kept inside liposomes during the reaction operation with less than 10% of leakage. All of the results obtained demonstrate that the liposomal CbFDH/NADH functions as a stable catalyst for reduction of CO₂ in the airlift. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Poly(L-lactide)-degrading enzyme production by Actinomadura keratinilytica T16-1 in 3 L airlift bioreactor and its degradation ability for biological recycle

The optimal physical factors affecting enzyme production in an airlift fermenter have not been studied so far. Therefore, the physical parameters such as aeration rate, pH, and temperature affecting PLA-degrading enzyme production by Actinomadura keratinilytica strain T16-1 in a 3 l airlift fermenter were investigated. The response surface methodology (RSM) was used to optimize PLA-degrading enzyme production by implementing the central composite design. The optimal conditions for higher production of PLA-degrading enzyme were aeration rate of 0.43 vvm, pH of 6.85, and temperature at 46° C. Under these conditions, the model predicted a PLA-degrading activity of 254 U/ml. Verification of the optimization showed that PLA-degrading enzyme production of 257 U/ml was observed after 3 days cultivation under the optimal conditions in a 3 l airlift fermenter. The production under the optimized condition in the airlift fermenter was higher than un-optimized condition by 1.7 folds and 12 folds with un-optimized medium or condition in shake flasks. This is the first report on the optimization of environmental conditions for improvement of PLA-degrading enzyme production in a 3 l airlift fermenter by using a statistical analysis method. Moreover, the crude PLA-degrading enzyme could be adsorbed to the substrate and degraded PLA powder to produce lactic acid as degradation products. Therefore, this incident indicates that PLA-degrading enzyme produced by Actinomadura keratinilytica NBRC 104111 strain T16-1 has a potential to degrade PLA to lactic acid as a monomer and can be used for the recycle of PLA polymer.     

聚乙烯醇-明胶复合膜固定化重组大肠杆菌NAD激酶的研究

为提高烟酰胺腺嘌呤二核苷酸(NAD)激酶的稳定性,采用复合膜对NAD激酶进行固定化研究。选用聚乙烯醇(PVA)、聚乳酸(PLA)、海藻酸钠(SA)和明胶(GEL)膜材料固定化NAD激酶。通过单因素实验确定最佳固定化条件为:PVA∶GEL为4∶1,加酶量为0.6 mL,固定化时间为6h,固定化温度为35℃,此时酶活力回收率达到最高值84%。固定化酶酶学性质分析结果表明,与游离酶进行比较,固定化后NAD激酶的最适温度由50℃提高至55℃,最适pH由8.0降至7.0,NAD激酶的热稳定性和pH稳定性均得到显著提高,但固定化酶的亲和力降低。固定化NAD激酶重复利用6次后,酶活性依然可维持初始酶活性的75%以上,表明聚乙烯醇-明胶复合膜固定化酶具有良好的操作稳定性。     

尼龙网固定化果胶酶的制备及其性质研究

用尼龙网作载体,经3-二甲氨基丙胺活化,用戊二醛将果胶酶固定化。所得固定化酶Km值与自然酶接近;对温度的稳定性有较大的提高,100℃保温30min才能使其失活。固定化酶在较宽的pH范围内能保持其正常活力,它对金属离子抑制剂的耐受性有较显著的提高,用0.5％果胶溶液作底物,重复使用10次后酶活力保留44％。固定化果胶酶与自然酶相比较,对不同果汁的澄清效果不同。固定化果胶酶在无保护剂存在的条件下,室温放置四个月活力不减少。     

Batch production of deacetyl 7-aminocephalosporanic acid by immobilized cephalosporin-C deacetylase

Bacillus subtilis SHS0133 cephalosporin-C deacetylase (CAH) overexpressed in Escherichia coli was immobilized on an anion-exchange resin, KA-890, using glutaraldehyde. The activity yield of immobilized enzyme was approximately 55% of the free enzyme. The pH range for stability of the immobilized enzyme (pH 5–10) was broader than that for free enzyme. The K_m^app value of immobilized enzyme for 7-aminocephalosporanic acid (7-ACA) was similar to that of the free enzyme. This immobilized enzyme obeyed Michaelis–Menten kinetics similar to those of the free enzyme. A batch-type reactor with a water jacket was employed for deacetylation of 7-ACA using CAH immobilized on KA-890. Ten kilograms of 7-ACA were completely converted to deacetyl 7-ACA at pH 8.0 within 90 min. The reaction kinetics agreed well with a computer simulation model. Moreover, the immobilized enzyme exhibited only a slight loss of the initial activity even after repeated use (52 times ) over a period of 70 days. This reaction will thus be useful for the production of cephalosporin-type antibiotics.     

Effect of immobilized enzyme deactivation in fixed- and fluid-bed reactors

A two-parameter theoretical model is developed to evaluate the effect of immobilized enzyme deactivation on substrate conversion in fixed- and fluid-bed reactors under diffusion-free conditions. The method describes a simple reaction in which three different immobilized enzyme deactivation forms are considered, and an expression is developed to evaluate the effect of immobilized enzyme deactivation on yield in a consecutive reaction. Comparison of reactor performances for the two reactor types reduces to a comparison of the appropriate dimensionless parameters. The practical implications of the development are illustrated through an example.     

Immobilization of Escherichia coli cells containing aspartase activity with kappa-carrageenan. Enzymic properties and application for L-aspartic acid production.

Whole cells of Escherichia coli having high aspartase (L-asparate ammonialyase, EC 4.3.1.1) activity were immobilized by entrapping into a kappa-carrageenan gel. The obtained immobilized cells were treated with glutaraldehyde or with glutaraldehyde and hexamethylenediamine. The enzymic properties of three immobilized cell preparations were investigated, and compared with those of the soluble aspartate. The optimum pH of the aspartase reaction was 9.0 for the three immobilized cell preparations and 9.5 for the soluble enzyme. The optimum temperature for three immobilized cell preparations was 5--10 degrees C higher than that for the soluble enzyme. The apparent Km values of immobilized cell preparations were about five times higher than that of the soluble enzyme. The heat stability of intact cells was increased by immobilization. The operational stability of the immobilized cell columns was higher at pH 8.5 than at optimum pH of the aspartase reaction. From the column effluents, L-aspartic acid was obtained in a good yield.     

Studies on neomycin production using immobilized cells of<Emphasis Type="Italic">S marinensis</Emphasis> NUV-5 in various reactor configurations: A technical note

Conclusion  Stirred tank, fluidized bed, and airlift reactors produced similar neomycin activity with immobilized cells. Packed bed reactor clearly under performed, probably because of insufficient aeration or mixing. Neomycin production using immobilized cells in fermentors requires good mixing and aeration.     

Isomaltose formation by free and immobilized dextransucrase

The acceptor reaction of dextransucrase from Leuconostoc mesenteroides NRRL-B512F with glucose as acceptor is of technical interest for isomaltooligosaccharide (IMOs) synthesis. Different experimental conditions were investigated for free and immobilized enzyme. The data for oligosaccharide formation up to a degree of polymerization 4 were correlated with a model developed earlier, and optimal reaction conditions for immobilized dextransucrase design and application were identified for later continuous application. Furthermore, stability was investigated for free and immobilized enzyme including stabilization by sugars.     

A feasible enzymatic process for D-tagatose production by an immobilized thermostable L-arabinose isomerase in a packed-bed bioreactor

To develop a feasible enzymatic process for d-tagatose production, a thermostable l-arabinose isomerase, Gali152, was immobilized in alginate, and the galactose isomerization reaction conditions were optimized. The pH and temperature for the maximal galactose isomerization reaction were pH 8.0 and 65 degrees C in the immobilized enzyme system and pH 7.5 and 60 degrees C in the free enzyme system. The presence of manganese ion enhanced galactose isomerization to tagatose in both the free and immobilized enzyme systems. The immobilized enzyme was more stable than the free enzyme at the same pH and temperature. Under stable conditions of pH 8.0 and 60 degrees C, the immobilized enzyme produced 58 g/L of tagatose from 100 g/L galactose in 90 h by batch reaction, whereas the free enzyme produced 37 g/L tagatose due to its lower stability. A packed-bed bioreactor with immobilized Gali152 in alginate beads produced 50 g/L tagatose from 100 g/L galactose in 168 h, with a productivity of 13.3 (g of tagatose)/(L-reactor.h) in continuous mode. The bioreactor produced 230 g/L tagatose from 500 g/L galactose in continuous recycling mode, with a productivity of 9.6 g/(L.h) and a conversion yield of 46%.     

Continuous production of 4-ethylguaiacol by immobilized cells of salt-tolerant Candida versatilis in an airlift reactor

The effects of pH, temperature, aeration, and residence time on the continuous production of 4-ethyl-guaiacol (4-EG), which is one of the characteristic aroma components in soy sauce, by immobilized cells of the salt-tolerant yeast Candida versatilis were investigated using an airlift reactor. The optimum pH and temperature were about 4.0 and 30–33°C, respectively. The amount of 4-EG in the liquid was constant even during alterations of nitrogen/air ratio in the supplied gas. A large amount of 4-EG (over 20 ppm) was produced at a residence time from 5 to 28 h and 1–3 ppm of 4-EG, which was the optimum concentration in conventional soy souce, was produced at a shorter residence time of 0.5 h. The 4-EG production by immobilized C. versatilis cells using the airlift reactor was stable for 40 d. It was found that the immobilized cell method was effective for the production of 4-EG by C. versatilis cells.     

Catalytic properties of the immobilized Aspergillus tamarii xylanase

Xylanase from Aspergillus tamarii was covalently immobilized on Duolite A147 pretreated with the bifunctional agent glutaraldehyde. The bound enzyme retained 54.2% of the original specific activity exhibited by the free enzyme (120 U/mg protein). Compared to the free enzyme, the immobilized enzyme exhibited lower optimum pH, higher optimum reaction temperature, lower energy of activation, higher K_m (Michaelis constant), lower V_max (maximal reaction rate). The half-life for the free enzyme was 186.0, 93.0, and 50.0 min for 40, 50, and 60°C, respectively, whereas the immobilized form at the same temperatures had half-life of 320, 136, and 65 min. The deactivation rate constant at 60°C for the immobilized enzyme is about 6.0 × 10⁻³, which is lower than that of the free enzyme (7.77 × 10⁻³ min). The energy of thermal deactivation was 15.22 and 20.72 kcal/mol, respectively for the free and immobilized enzyme, confirming stabilization by immobilization. An external mass transfer resistance was identified with the immobilization carrier (Duolite A147). The effect of some metal ions on the activity of the free and immobilized xylanase has been investigated. The immobilized enzyme retained about 73.0% of the initial catalytic activity even after being used 8 cycles.     

纳米磁性壳聚糖微球固定化酵母醇脱氢酶的研究

建立了以纳米级磁性壳聚糖微球(magnetic chitosan microspheres , M-CS)为载体固定化酵母醇脱氢酶(yeast alcohol dehydrogenase,YADH)的方法,优化了YADH的固定化条件,考察了固定化酶的性质。结果表明,M-CS 呈规则的圆球形,粒径在30nm 左右,具有较好的磁响应性。酵母醇脱氢酶固定化适宜条件为:50 mg 磁性壳聚糖微球,加入20mL 0.25 mg/mL 酵母醇脱氢酶(蛋白质含量)磷酸盐缓冲液(0.05 mol/L ,pH 7.0) ,在4 ℃固定2h。M-CS 容易吸附酵母醇脱氢酶,但吸附的酶量受载体与酶的比例、溶液的离子浓度、溶液pH的影响明显,而温度对吸附的酶量的影响则相对较弱。相对于游离的酵母醇脱氢酶,固定化酶的最适温度略有升高,可明显改善其热稳定性、酸碱稳定性、操作稳定性和贮存稳定性。     

Immobilization of Aspergillus oryzae tannase and properties of the immobilized enzyme

Tannase enzyme from Aspergillus oryzae was immobilized on various carriers by different methods. The immobilized enzyme on chitosan with a bifunctional agent (glutaraldehyde) had the highest activity. The catalytic properties and stability of the immobilized tannase were compared with the corresponding free enzyme. The bound enzyme retained 20·3% of the original specific activity exhibited by the free enzyme. The optimum pH of the immobilized enzyme was shifted to a more acidic range compared with the free enzyme. The optimum temperature of the reaction was determined to be 40 °C for the free enzyme and 55 °C for the immobilized form. The stability at low pH, as well as thermal stability, were significantly improved by the immobilization process. The immobilized enzyme exhibited mass transfer limitation as reflected by a higher apparent K_m value and a lower energy of activation. The immobilized enzyme retained about 85% of the initial catalytic activity, even after being used 17 times.     

Properties of a reversible soluble-insoluble cellulase and its application to repeated hydrolysis of crystalline cellulose

Cellulase was covalently immobilized on an enteric coating polymer, Eudragit L, that is reversibly soluble and insoluble depending on the pH of the medium. The hydrolysis of solid cellulose with the immobilized enzyme can take advantage of the soluble property of the immobilized enzyme itself at the most reactive pH value; on the other hand, recovery of the enzyme can take advantage of the insoluble property of the enzyme at other pH values. It was experimentally confirmed that 100% of immobilized enzyme activity in solution can be recovered by precipitation and by dissolving it again by alternative change of pH. After a period of hydrolysis, immobilized enzyme and unreacted cellulose were precipitated together to remove the product-the soluble sugar solution-by changing pH. Following this, a new buffer solution was added to the precipitate to dissolve it and resume the reaction. This was repeated several times. The hydrolysis rate of this process increased significantly compared with that of a batch process. Utilization of the reversible soluble-insoluble carrier for immobilizing enzyme is promising, not only for cellulose-cellulase systems, but also for other heterogeneous reaction systems.