Production of Penicillin G acylase from Bacillus sp.: Effect of medium components

A Bacillus sp. producing a high level of intracellular penicillin G acylase (PAC) was isolated. The PAC production in this strain was induced by phenylacetic acid. Various carbon and nitrogen sources were evaluated for their effect on growth and PAC production at 28 °C and pH 7.0. Cells grown in medium supplemented with sucrose as carbon source and tryptone as nitrogen source produced maximum activity of 6.45 and 8.92 U mg^–1, respectively. Maximum concentration of PAC (10.1 Umg^–1) was produced by the cells grown in the medium containing sucrose and tryptone, which was twofold higher than the production in basal medium.     

Development of a process for large-scale chromatographic purification of an alginate lyase from Klebsiella pneumoniae

Summary A process for purification of an alginate lyase, produced extracellularly by fermentation of Klebsiella pneumoniae, has been developed. The process includes two chromatographic steps and is well suited to large-scale operation. By hydrophobic interaction chromatography on Phenyl-Sepharose FF, followed by anion exchange chromatography on Q-Sepharose FF in a negative mode, the specific activity was increased from 0.09 units (U) mg ^–1 to more than 50 U mg^–1. Due to an extremely low product concentration in the fermentation broth, and large amounts of contaminating proteins, the chromatographic adsorbents had low capacities with respect to alginate lyase. By adsorption on the cation exchanger S-Sepharose FF, the capacity was so low that the enzyme could not be concentrated. The binding capacity of Phenyl-Sepharose FF was approximately 20-fold higher, and a three to tenfold concentration was obtained. The first stage of the process, hydrophobic interaction chromatography, has been applied to the isolation of alginate lyase from fermentation batches of 180 l. Several runs have resulted in a purified product with an average quantity of 30 000–35 000 U per fermentation, and an average specific activity of 4.5 U mg^–1. Although the raw material employed in this work has been particularly unfavourable, the process developed will also be applicable to raw materials with higher product concentrations. Offprint requests to: I. M. Aasen     

Mixed carbon source control strategy for enhancing alginate lyase production by marine Vibrio sp. QY102

Medium and culture conditions for alginate lyase production by marine Vibrio sp. QY102 were first optimized using statistical methods including Plackett–Burman design and central composite design. Then, fermentation in 5-L bioreactor showed that alginate acted as easily used carbohydrate for Vibrio sp. QY102, while starch extended its growth phase and stabilized pH variations. Thus, a novel strategy using mixed carbon sources was proposed that starch supported growth while enzyme synthesis was induced by pulse feedings of solid alginate. The optimized process followed that Vibrio sp. QY102 grew on starch until the end of the logarithmic growth phase, and then solid alginate was added as 1 g/L every 3 h. Meanwhile, initial pH 5.0 and natural pH during fermentation was favorable for alginate lyase production. After optimization, the highest alginate lyase production reached 52.8 U/mL, which was 329 % higher than the control. Finally, fermentation scale-up was performed in 30-L bioreactor and the maximum alginate lyase production was obtained as 46.8 U/mL.     

Preliminary studies on the growth of Pseudomonas sp. BA2 and the production of L-aminoacylase

Summary The bacterial strain Pseudomonas sp. BA2 did not develop l-aminoacylase activity in the absence of N-acetyl-dl-alanine. The maximum growth rate and enzyme production were obtained when the acetylated amino acid was used as the sole carbon and nitrogen source. A maximum biomass of A₆₆₀=1.543, after 24 h of cultivation, was obtained. The l-aminoacylase activity reached the maximum value (5.6 U ml^–1 broth) in the stationary growth phase.     

Invertase production by Aspergillus niger in submerged and solid-state fermentation

Three Aspergillus nigerstrains were grown in submerged and solid state fermentation systems with sucrose at 100 g l^–1. Average measurements of all strains, liquid vs solid were: final biomass (g l^–1), 11 ± 0.3 vs 34 ± 5; maximal enzyme titres (U l^–1) 1180 ± 138 vs 3663 ± 732; enzyme productivity (U l^–1h^–1) 20 ± 2 vs 87 ± 33 and enzyme yields (U/gX) 128 ± 24 vs 138 ± 72. Hence, better productivity in solid-state was due to a better mould growth.     

Effect of culture conditions on astaxanthin production by a mutant of Phaffia rhodozyma in batch and chemostat culture

Temperature and pH had only a slight effect on the astaxanthin content of a Phaffia rhodozyma mutant, but influenced the maximum specific growth rate and cell yield profoundly. The optimum conditions for astaxanthin production were 22°C at pH 5.0 with a low concentration of carbon source. Astaxanthin production was growth-associated, and the volumetric astaxanthin concentration gradually decreased after depletion of the carbon source. The biomass concentration decreased rapidly during the stationary growth phase with a concomitant increase in the cellular content of astaxanthin. Sucrose hydrolysis exceeded the assimilation rates of D-glucose and D-fructose and these sugars accumulated during batch cultivation. D-Glucose initially delayed D-fructose uptake, but D-fructose utilization commenced before glucose depletion. In continuous culture, the highest astaxanthin content was obtained at the lowest dilution rate of 0.043 h^–1. The cell yield reached a maximum of 0.48 g cells·g^–1 glucose utilized between dilution rates of 0.05 h^–1 and 0.07 h^–1 and decreased markedly at higher dilution rates. Correspondence to: J. C. Du Preez     

Modelling the production of nisin by Lactococcus lactis in fed-batch culture

Nisin production in batch culture and fed-batch cultures (sucrose feeding rates were 6, 7, 8, and 10 g l^–1 h^–1, respectively) by Lactococcus lactis subsp. lactis ATCC 11454 was investigated. Nisin production showed primary metabolite kinetics, and could be improved apparently by altering the feeding strategy. The nisin titer reached its maximum, 4,185 IU ml^–1, by constant addition of sucrose at a feeding rate of 7 g l^–1 h^–1; an increase in 58% over that of the batch culture (2,658 IU ml^–1). Nisin biosynthesis was affected strongly by the residual sucrose concentration during the feeding. Finally, a mathematical model was developed to simulate the cell growth, sucrose consumption, lactic acid production and nisin production. The model was able to describe the fermentation process in all cases.     

一株产褐藻胶裂解酶的需钠弧菌筛选及酶解产物分析

[背景]褐藻胶裂解酶种类丰富、降解机制多样,是高效环保降解褐藻胶、制备褐藻寡糖的工具酶,成为褐藻植物高值化开发利用的研究热点.[目的]从海泥中筛选获得褐藻胶裂解酶高效产酶菌株,确定菌株发酵产酶最优条件,鉴定和分析酶降解产物,进而解析该酶的降解特性.[方法]以褐藻胶为唯一碳源,从海带养殖场附近海泥中筛选菌株,通过形态学观...     

Chondrus crispus (Gigartinaceae,Rhodophyta) tank cultivation: optimizing carbon input by a fixed pH and use of a salt water well

The injection of exogenous carbon into intensively cultivated algal tanks is necessary to insure a maximum growth rate by stabilizing the dissolved inorganic carbon (DIC) pool, but represents the major part of the cultivation cost (ca. 73%). This study was conducted in paddle-wheel tanks ranging in size from 260 m² to 1000 m². Additional carbon was provided by carbon dioxide mixed into the incoming sea water through a tubular reactor. Production vs pH was analysed on 120 growth measurements covering two years of continuous cultivation. Whereas production peaked at pH 8.0–8.2, the economic optimum for pH regulation was in the range 8.4–8.5, where CO₂ injection was greatly reduced (–29%) for only a slight decrease in production (–4%). Expressed as a function of pH level, the specific carbon injection (g c gdw^–1 of Chondrus produced) showed an inverse exponential relationship, whereas gross photoconversion ratio (gdw mol photons^–1) varied according to a second degree equation with a low amplitude. The photoconversion ratio was not improved when the culture was maintained at a DIC concentration higher than the natural equilibrium (0.64 ± 0.11 gdw mol photons^–1 at 2.35 mM and 0.65 ± 0.15 gdw mol photons^–1 at 3.19 MM).A complementary source of carbon was found in underground salt water with a high and stable DIC concentration (10.15 ± 0.25 mmole Cl^–1). The mixing of the well water with natural sea water allowed another economy of CO₂ (–20% at pH 8.5) and nutrients (–12%), the total unitary cost of production being cut by about 17%.     

响应面法优化褐藻胶降解菌Cobetia sp.20发酵培养基

为了提高褐藻胶降解菌株Cobetia sp.20产褐藻胶裂解酶的能力,利用响应面法优化其发酵产褐藻胶裂解酶的培养基。首先利用单因素法分别对发酵培养基中的不同碳源、碳源添加量、不同氮源、氮源添加量以及氯化钠添加量、磷酸二氢钾添加量、硫酸镁添加量和pH进行探究,研究各因素对产酶的影响。在单因素实验的基础上,通过Plackett-Burman试验确定Cobetia sp.20发酵培养基中影响产酶的主要因素。通过响应面试验建立回归方程。研究结果表明,Cobetia sp.20最优发酵培养基配方为褐藻胶15.00 g/L、硫酸铵7.50 g/L、氯化钠15.00 g/L、硫酸镁0.50 g/L、磷酸二氢钾5.30 g/L、硫酸亚铁0.01 g/L、pH值7.58。优化后酶活为142.79 U/mL,比优化前提高了26.36%。褐藻胶裂解酶活的提高,为褐藻胶裂解酶的工业化生产提供了参考。     

Effects of nutritional factors on the formation of Anthraquinones in callus cultures of Rheum ribes

Rheum ribes L. (Polygonaceae) is the source of one of the most important crude drugs in Asiatic regions .The medicinal character of rhubarb is due to its anthraquinone content . Different parts of sterile seedlings were cultured on MS medium to study the generation of callus. The explants were cultured with different ranges of plant growth regulators and the best range of plant growth regulators for generation of callus was IBA (1 mg l^–1) and BA (1 mg l^–1). The content of anthraquinones were determined by HPLC . The concentration of sucrose, vitamins and Myo-inositol and ratio of NO₃ to NH₄ in the medium was changed and growth rate and content of 2 anthraquinones was determined . The growth rate of callus declined with increased rate of secondary metabolites production. Myo-inositol 100 mg l^–1 in the medium increased anthraquinone content and in medium that had NO₃/NH₄:1/1 the maximum content of anthraquinone was obtained.     

Stimulation of berberine secretion and growth in cell cultures of Thalictrum minus

Summary An endo-pectate lyase (PL; EC 4.2.2.2), originally cloned fiom the phytopathogenic bacterium Erwinia chrysanthemi EC16, was expressed in recA ^– E. coli strain DK1, purified to a single band by isoelectric focusing and used to induce berberine production in established plant suspension cultures of Thalictrum minus L. subsp. saxatile. Addition of 10^–9M pectate lyase c (PLc) stimulated berberine production and enhanced secretion of the alkaloid into the medium. A lower concentration of PLc, 10^–11M, stimulated a transient two-fold increase in cell growth rate relative to untreated cultures. Parallel changes in L-phenylalanine ammonia lyase (PAL; EC 4.3.1.5) activity with the rate of berberine synthesis and the inverse relationship between cell growth and berberine synthesis imply that berberine synthesis is stress-related in this cell line.     

Regulation of heparinase synthesis in Flavobacterium heparinum

The effect of various carbon, nitrogen and sulfur sources on the production of heparinase by Flavobacterium heparinum in defined medium in the presence and absence of heparin as the inducer has been studied. Carbon catabolite repression has been observed in defined medium containing one of several carbon sources including simple sugars, alcohols and organic acids. Fed batch fermentations result in 10 g/l of cells and heparinase titers as high as 100,000 U/l by avoiding carbon catabolite repression. Growth on heparin as a sole carbon source resulted in both a high growth rate of 0.12 h^–1 and a high specific activity of 18 U/mg. Specific heparinase activity was markedly reduced when the end products of heparin catabolism were used as carbon, nitrogen or sulfur sources in defined medium. In defined medium with a low sulfate concentration, of less than 10^–3 M, specific activities as high as 8 U/mg have been observed even in the absence of the normally required inducer, heparin.     

Culture conditions for the production of pectinolytic enzymes by the white-rot fungus Trametes trogii on a laboratory scale

Different cultural parameters that regulate pectinolytic enzyme production in vitro by Trametes trogii were studied. When grown in a medium containing pectin, T. trogii produced extracellular polymethylgalacturonase, polygalacturonase and pectin lyase but no pectate lyase activity. No significant differences in the maximum enzyme activities measured were observed with the addition of xylan, carboxymethylcellulose or both to the medium containing pectin. The addition of glucose to that medium considerably decreases all the activities studied, and in a medium with glucose as the sole carbon source no galacturonase activity could be measured, and pectin lyase activity was at its minimum. The low synthesis of pectin lyase in cultures containing glucose suggests that this enzyme is constitutive in contrast to the polygalacturonases that were not detected. The increase in pectin concentration stimulated growth and enzyme production. The highest specific activities were attained with the greatest concentration tested (15 g/l). Casamino acids were the best nitrogen source for enzyme production. Maximum growth was measured at pH 3.3; pH values of around 4.5 stimulated enzyme production, but high pectinase activities were also detected in media with more alkaline initial pH values (6.2 for galacturonases and 6.6 for lyases), probably owing to the specific induction of particular isoforms. In the range of 23 to 28°C, good results were obtained in growth as well as in enzyme production. The addition of Tween 80 promoted growth and gave the highest yield of polymethylgalacturonase and pectin lyase (0.37 and 36.2 E.U./ml, respectively). The highest polygalacturonase activity (1.1 E.U/ml) was achieved with polyethylene glycol. Tween 20 and Triton X-100 inhibited growth and pectinase production.     

The isolation and characterisation of a salicylate-hydroxylase-producing strain of Pseudomonas putida

Summary A salicylate-hydroxylase-producing strain of Pseudomonas putida with an unusual capability to grow at toxic levels of salicylate up to 10 g l^–1 has been isolated. It grew well under continuous culture conditions, with optimum growth at pH 6.5 and a temperature of 25° C. The use of an ammonium salt as a nitrogen source, instead of nitrate, resulted in a 30–40% increase in its biomass yield coefficient. Optimum growth under continuous culture conditions was achieved using 4 g l^–1 salicylate at 25° C, pH 6.5 and 0.2 h^–1 dilution rate. High salicylate hydroxylase enzyme activity [236 units (U) l^–1] and productivity (424.8 U h^–1) were obtained at a dilution rate of 0.45 h^–1 using a mineral medium containing 4 g l^–1 of salicylate. Operating under continuous culture conditions with oxygen limitation and a slight accumulation of residual salicylate (0.2 g l^–1) resulted in a decrease in culture performance and enzyme productivity. Correspondence to: R. Marchant     

Mass production of lipase by fed-batch culture of Pseudomonas fluorescens

Summary High concentration production of an extracellular enzyme, lipase, was achieved by a fed-batch culture of Pseudomonas fluorescens. During the cultivation, temperature, pH and dissolved oxygen concentration wwre maintained at 23°C, 6.5 and 2–5 ppm, respectively. Olive oil was used as a carbon source for microbial growth. To produce lipase effectively the specific feed rate of olive oil had to be maintained in a range of 0.04–0.06 (g oil) · (g dry cell)^-1 · h^-1. The CO₂ evolution rate was monitored to estimate the requirement of olive oil. The ratio of feed rate of olive oil to the CO₂ evolution rate was varied in the range of 20–60 g oil/mol CO₂. The higher value of the ratio accelerated microbial growth, but did not favour lipase production. Once the high cell concentration of 60 g/l had been achieved, the ratio was changed from 50 to 30 g oil/mol CO₂ to accelerate the lipase production. By this CO₂-dependent method a very high activity of lipase, 1980 units/ml, was obtained. Both the productivity and yield of lipase were prominently increased compared with a conventional batch culture.     

Isolation and characterization of an alginate lyase from Klebsiella aerogenes

The bacterium Klebsiella aerogenes (type 25) produced an inducible alginate lyase, whose major activity was located intracellularly during all growth phases. The enzyme was purified from the soluble fraction of sonicated cells by ammonium sulfate precipitation, anion- and cation-exchange chromatography and gel filtration. The apparent molecular weight of purified alginate lyase of 28,000 determined by gel filtration and of 31,600 determined by sodium dodecyl sulfate-polyacrylamide gel electrophoresis indicated that the active enzyme was composed of a single polypeptide. The alginate lyase displayed a pH optimum around 7.0 and a temperature optimum around 37°C. The purified enzyme depolymerized alginate by a lyase reaction in an endo manner releasing products which reacted in the thiobarbituric acid assay and absorbed strongly in the ultraviolet region at 235 nm. The alginate lyase was specific for guluronic acidrich alginate preparations. Propylene glycol esters of alginate and O-acetylated bacterial alginates were poorly degraded by the lyase compared with unmodified polysaccharide. The guluronate-specific lyase activity was applied in an enzymatic method to detect mannuronan C-5 epimerase in three different mucoid (alginate-synthesizing) strains of Pseudomonas aeruginosa. This enzyme which converts polymannuronate to alginate could not be demonstrated either extracellularly or intracellularly in all strains suggesting the absence of a polymannuronate-modifying enzyme in P. aeruginosa.Abbreviations poly(ManA) (1–4)--D-mannuronan - poly(GulA) (1–4)--L-guluronan - TBA 2-thiobarbituric acid     

Conversion of cellulose into fungal cell mass

Summary Chaetomium cellulolyticum (ATCC 32319) was cultivated on glucose, Avicel and/or Sigmacell in a 20-1 stirred tank batch reactor. The substrate (cellulose) concentration, the cell mass concentration (through protein and/or nitrogen content), reducing sugar concentration, the enzyme activity, the alkali consumption rate, the dissolved O₂ and CO₂ concentrations in the outlet gas were measured. The specific growth rate, the substrate yield coefficient, cell productivity, the oxygen consumption rate, the CO₂ production rate and the volumetric mass transfer coefficient were determined. At the beginning of the growth phase the oxygen utilization rate exhibits a sharp maximum. This maximum could be used to start process control. Because of the long lag phase periodic batch operation is recommended.Symbols CP cell protein concentration (g l^–1) - FPA FP enzyme activity (IU l^–1) - GP dissolved protein concentration (g l^–1) - IU international unit of enzyme activity - k_La volumetric mass tranfer coefficient (h^–1) - LG alkali (1 n NaOH) consumption (ml) - LGX specific alkali consumption rate per cell mass (ml g^–1 h^–1) - P cell mass productivity (g l^–1 h^–1) - specific oxygen consumption rate per cell mass (g g^–1 h^–1) - Q aeration rate (volumetric gas flow rate per volume of medium, vvm) (min^–1) - N impeller speed (revolution per minute, rpm) (min^–1) - S substrate concentration (g l^–1) - S⁰ S at t_F=0 (g l^–1) - S₀ S in feed (g l^–1) - SR acid consumption (ml) - TDW total dry weight (g l^–1) - T temperature (° C) - t_F cultivation time (h) - U substrate conversion - X cell mass concentration (g l^–1) - Y_X/S vield coefficient - specific growth rate (h^–1) - _m maximum specific growth rate (h^–1)     

Cellulase production by Trichoderma reesei (RUT-C30) in fed-batch culture

Summary Fed-batch cultures of Trichoderma reesei RUT-C30 attained quasi-steady state conditions, in respect of biomass concentration and enzyme production rate, commensurate with a specific cell maintenance coefficient of 0.029 g cellulose.g biomass.^–1h^–1 and specific cellulase production rate of between 9.6 and 11.9 IU (filter paper activity).g biomass.^–1h^–1. A maximum enzyme yield of 57 IU.m1^–1 at an overall productivity of 201 IU.L.^–1h^–1 resulted from a cellulose feed rate of 1.0g.L.^–1h^–1.     

Production and Characterization of Amylase from Calvatia gigantea

α-Amylase (EC 3.2.1.1) was excreted by Calvatia gigantea in liquid growth media containing different sources of starch. Among the factors affecting enzyme production in shake flasks were the type and the concentration of starch and the nitrogen source supplied. Optimum cultural conditions for maximum enzyme production were: soluble starch concentration, 5%; inoculum size, 3.75 × 10⁵ conidia per ml; 5-day cultivation time at 28 to 30°C. The observed maximum yield of 81.3 U of saccharifying enzyme activity per ml of growth medium was the highest ever reported in the literature for submerged cultures. Partially purified enzyme functioned optimally at pH 4.5 to 5.5 and 53 to 58°C. The activation energy of enzymic hydrolysis of starch in the range of 20 to 40°C was 8,125 cal/mol (ca. 3.41 × 10⁴ J). The apparent K_m value of the enzyme at 25°C was 7.68 × 10⁻⁴ g/ml. Some of the properties of the enzyme under investigation were similar to those of α-amylases excreted from molds producing large amounts of the enzyme.