Development of a fermentation process for production of an alginate G-lyase from Klebsiella pneumoniae

A high-density-cell fermentation process for production of an exracellular alginat lyase from Klebseilla pneumoniae on a defined medium has been developed. The process employs a strategy using two carbon sources. One low-molecular-mass, low-viscosity carbon source (sucrose) with high water solubililty is used as the main carbons source for growth, while the high-molecular-mass and viscoous alginate in low concentration is used as an inducer for enzyme synthesis. The repression of algiante lyase production by sucrose and the growth inhibition that we observed at increased levels of ammonia were circumvented by a computer-assisted fed-batch addition of the carbon sources (succrose and alginate) and by supplying nitrogen source as ammonia in the pH control. No enzyme production was observed when dissolved oxygen limited growth at an oxygen uptake rate of 40%–50% of the maximum uptake rate. An optimal composition of the feeding solution (12.5 g alginate and 587.5 g sucrose 1^–1) was found both for the maximum final concentration of enzyme (1330 U 1^–1) and for the maximum volumetric rate of enzyme production (67 U 1^–1 h^–1). The enzyme production dependes of the growth rate in the linear growth phase, giving a maximum enzyme concentration at the highest growth rate tested. The final enzyme concentration shows a fiveflod increase compare with previously reproted daata where alginate was used as a carbon source. In addition, the ratio of alginate lyase by a factor of apporximately 15. A doubling in extracellular specific activity of the enzyme was observed, a property of significant interest, especially for purification of the enzyme. On the othr hand, the final dry cell weight concentration of the bacteria also increased by a factor of 15–20 thus giving a relatively lower specific productivity of 0.4 U (g cell dry weight)^–1 h^–1.     

Production of an amylase-degrading raw starch by Gibberella pulicaris

An endophytic fungus, Gibberella pulicaris, produced an amylase which degraded raw starches from cereals and other crops including raw potato, sago, tapioca, corn, wheat and rice starch. In each case, glucose was the main product. Among the raw starches used, raw potato starch gave the highest enzyme activity (85 units mg^–1 protein) and raw wheat starch the lowest (49 units mg^–1 protein). The highest amylase production (260 units mg^–1 protein) was achieved when the concentration of raw potato starch was increased to 60 g l^–1. Optimum hydrolysis was at 40°C and pH 5.5.     

Ethanol Production from Colpomenia sinuosa by an Alginate Fermentation Strain Meyerozyma guilliermondii

With the consumption of energy and the spread of COVID-19, the demand for ethanol production is increasing in the world. The industrial ethanol fermentation microbes cannot metabolize the alginate component of macro algae, which affects the ethanol yield. In this research, the ethanol production process from macro algae by an alginate fermentation yeast Meyerozyma guilliermondii, especially the pretreatment process of Colpomenia sinuosa, was studied. At the same time, the experimental design of Box-Behnken was carried out to achieve the optimum fermentation performance. The concentration of KH₂PO₄ (A: 2–6 g.L⁻¹), pH (B: 4–7), reaction time (C: 60–120 h) and temperature (D: 24–34 °C) were variable input parameters. During the ethanol production process, the algae powder was firstly mixed with water at 90 °C for 0.5 h. Later the fermentation culture medium was prepared and then it was fermented by the yeast Meyerozyma guilliermondii to produce ethanol. And the optimal fermentation parameters were as follows: fermentation temperature of 28 °C, KH₂PO₄ dosage of 4.7 g.L⁻¹, initial pH of 6, and fermentation time of 99 h. The ethanol yield reached 0.268 g.g⁻¹ (ethanol to algae), close to the predicted value of model. The generation of alginate lyase during the fermentation of algae was also examined. The highest alginate lyase activity reached 46.42 U.mL⁻¹.     

Isolation and biochemical characterization of a new NADH oxidase from Lactobacillus brevis

A new NADH oxidase, useful for the regeneration of NAD⁺, was isolated and characterized from Lactobacillus brevis. In crude extracts the activity was from 10–15 U mg^–1. After purification by four chromatographic steps, an activity of 116 U mg^–1 was obtained with 14% yield. Highest activity was from pH 5.5–7 and at 40°C. The enzyme requires dithiothreitol to prevent oxidative deactivation. The K _m value for NADH was 24 M.     

L-Lactic acid production from raw cassava starch in a circulating loop bioreactor with cells immobilized in loofa (Luffa cylindrica)

l-Lactic acid was produced from raw cassava starch, by simultaneous enzyme production, starch saccharification and fermentation in a circulating loop bioreactor with Aspergillus awamori and Lactococcus lactis spp. lactis immobilized in loofa sponge. A. awamori was immobilized directly in cylindrical loofa sponge while the L. lactis was immobilized in a loofa sponge alginate gel cube. In the loofa sponge alginate gel cube, the sponge serves as skeletal support for the gel with the cells. The alginate gel formed a hard outer layer covering the soft porous gel inside. By controlling the rate and frequency of broth circulation between the riser and downcomer columns, the riser could be maintained under aerobic condition while the downcomer was under anaerobic condition. Repeated fed-batch l-lactic acid production was performed for more than 400 h and the average lactic acid yield and productivity from raw cassava starch were 0.76 g lactic acid g^–1 starch and 1.6 g lactic acid l^–1 h^–1, respectively.     

Pyruvate metabolism of the hyperthermophilic archaebacterium Pyrococcus furiosus

The hyperthermophilic anaerobe Pyrococcus furiosus was found to grow on pyruvate as energy and carbon source. Growth was dependent on yeast extract (0.1%). The organism grew with doublings times of about 1 h up to cell densities of 1–2×10⁸ cells/ml. During growth 0.6–0.8 mol acetate and 1.2–1.5 mol CO₂ and 0.8 mol H₂ were formed per mol of pyruvate consumed. The molar growth yield was 10–11 g cells(dry weight)/mol pyruvate. Cell suspensions catalyzed the conversion of 1 mol of pyruvate to 0.6–0.8 mol acetate, 1.2–1.5 mol CO₂, 1.2 mol H₂ and 0.03 mol acetoin. After fermentation of [3-¹⁴C]pyruvate the specific radioactivities of pyruvate, CO₂ and acetate were equal to 1:0.01:1. Cellfree extracts contained the following enzymatic activities: pyruvate: ferredoxin (methyl viologen) oxidoreductase (0.2 U mg^-1, T=60°C, with Clostridium pasteurianum ferredoxin as electron acceptor; 1.4 U mg^-1 at 90°C, with methyl viologen as electron acceptor); acetyl-CoA synthetase (ADP forming) [acetyl-CoA+ADP+Piacetate+ATP+CoA] (0.34 U mg^-1, T=90°C), and hydrogen: methyl viologen oxidoreductase (1.75 U mg^-1). Phosphate acetyl-transferase activity, acetate kinase activity, and carbon monoxide:methyl viologen oxidoreductase activity could not be detected. These findings indicate that the archaebacterium P. furiosus ferments pyruvate to acetate, CO₂ and H₂ involving only three enzymes, a pyruvate:ferredoxin oxidoreductase, a hydrogenase and an acetyl-CoA synthetase (ADP forming).Non-standard abbreviations DTE dithioerythritol - MV methyl viologen - MOPS morpholinopropane sulfonic acid - Tricine N-tris(hydroxymethyl)-methylglycine Part of the work was performed at the Laboratorium für Mikrobiologie, Fachbereich Biologie, Philipps-Universität, Karlvon-Frisch-Strasse, W-3550 Marburg/Lahn, Federal Republic of Germany     

Effects of surface hydrophobicity on the catalytic iron ion retention in the active site of two catechol 1,2-dioxygenase isoenzymes

The different behaviour of two isozymes (IsoA and IsoB) of catechol 1,2-dioxygenase (C1,2O) from Acinetobacter radioresistenss13 on a hydrophobic interaction, Phenyl-Sepharose chromatographic column, prompted us to investigate the role of superficial hydrophobicity on structural-functional aspects for such class of enzymes. The interaction of 8-anilino-1-naphtalenesulphonate (ANS), a fluorescent probe known to bind to hydrophobic sites in proteins, revealed that the two isoenzymes have a markedly different hydrophobicity degree although a similar number of hydrophobic superficial sites were estimated (2.65 for IsoA and 2.18 for IsoB). ANS is easily displaced by adding the substrates catechol or 3-methylcatechol to the adduct, suggesting that the binding sites are in the near surroundings of the catalytic clefts. The analysis of the hydropathy profiles and the possible superficial cavities allowed to recognize the most feasible region for ANS binding.The lower hydrophobicity detected in the near surroundings of the catalytic pocket of IsoB supports its peculiarity to lose the catalytic metal ions more easily than IsoA. As previously suggested for other metalloenzymes, the presence of more hydrophilic and/or smaller residues near to the active site of IsoB is expected to increase the metal ligands mobility thus increasing the metal ion dissociation rate constants, estimated to be 0.078 h^–1 and 0.670 h^–1 for IsoA and IsoB respectively. Abbreviations: C1,2O – catechol dioxygenase; ANS – 8-anilino-1-naphthalenesulphonate; PHO – phenol hydroxylase oxygenase     

Production of laccase byBotrytis cinerea and fermentation studies with strain F226

After induction, seven strains ofBotrytis cinerea released into the culture broth considerable amounts of laccase in a brief production time. The set-up of a suitable production process was studied with a selected strain in a 10-L fermenter. The optimum fermentation conditions were a 3% inoculum with a high degree of sporulation, a simple medium containing 20 g L^–1 of glucose and 2 g L^–1 of yeast extract at pH 3.5, 2 g L^–1 gallic acid as inducer, added after 2 days of growth, an agitation speed of 300 rpm, an aeration rate of 1.2 vvm and a temperature of 24°C. By optimizing the culture conditions, the enzyme activity reached 28 U ml^–1 in 5 days with a specific activity of 560 U mg^–1 protein. The best procedure to obtain a suitable crude enzyme preparation was concentration of the supernatant medium to 10% of the initial volume by ultrafiltration, followed by a fractional precipitation with ethanol. The optimum pH and temperature for laccase activity were 5.5 and 40°C, respectively, with syringaldazine as the substrate.     

Regulation of phospho(enol)-pyruvate-and oxaloacetate-converting enzymes in Corynebacterium glutamicum

The presence and properties of the enzymes involved in the synthesis and conversion of phospho(enol)pyruvate (PEP) and oxaloacetate (OAA), the precursors for aspartate-derived amino acids, were investigated in three different Corynebacterium strains. This study revealed the presence of both PEP carboxykinase 0.29 mol·min^–1·mg^–1 of protein [units (U)·mg^–1] and PEP synthetase (0.13 U·mg^–1) in C. 2 glutamicum as well as pyruvate kinase (1.4 U·mg^–1) and PEP carboxylase (0.16 U·mg^–1). With the exception of PEP carboxykinase these activities were also present in glucose-grown C. flavum and C. lactofermentum. Pyruvate carboxylase activity was not detected in all three species cultivated on glucose or lactate. At least five enzyme activities that utilize OAA as a substrate were detected in crude extracts of C. glutamicum: citrate synthase (2 U·mg^–1), malate dehydrogenase (2.5 U·mg^–1), glutamate: OAA transaminase (1 U·mg^–1), OAA-decarboxylating activity (0.89 U·mg^–1) and the previously mentioned PEP carboxykinase (0.29 U·mg^–1). The partially purified OAA-decarboxylase activity of C. glutamicum was completely dependent on the presence of inosine diphosphate and Mn²⁺, had a Michaelis constant (K _m) of 2.0mm for OAA and was inhibited by ADP and coenzyme A (CoA). Examination of the kinetic properties showed that adenine nucleotides and CoA derivatives have reciprocal but reinforcing effects on the enzymes catalyzing the interconversion of pyruvate, PEP and OAA in C. glutamicum. A model for the regulation of the carbon flow based on these findings is presented.Correspondence to: M. S. M. Jetten     

Production ofPseudomonas putida cells with high aspartase activity

Summary In an optimized fermentation withPseudomonas putida, specific activity of aspartase in the cells reaches 500 IU.mg^–1 in batch culture, and 1600 IU.ml^–1 in fed batch.     

Improvement of succinate production by overexpression of a cyanobacterial carbonic anhydrase in Escherichia coli

Succinate fermentation was investigated in Escherichia coli strains overexpressing cyanobacterium Anabaena sp. 7120 ecaA gene encoding carbonic anhydrase (CA). In strain BL21 (DE3) bearing ecaA, the activity of CA was 21.8 U mg⁻¹ protein, whereas non-detectable CA activity was observed in the control strain. Meanwhile, the activity of phosphoenolpyruvate carboxylase (PEPC) increased from 0.2 U mg⁻¹ protein to 1.13 U mg⁻¹ protein. The recombinant bearing ecaA reached a succinate yield of 0.39 mol mol⁻¹ glucose at the end of the fermentation. It was 2.1-fold higher than that of control strain which was just 0.19 mol mol⁻¹ glucose. EcaA gene was also introduced into E. coli DC1515, which was deficient in glucose phosphotransferase, lactate dehydrogenase and pyruvate:formate lyase. Succinate yield can be further increased to 1.26 mol mol⁻¹ glucose. It could be concluded that the enhancement of the supply of HCO₃⁻ in vivo by ecaA overexpression is an effective strategy for the improvement of succinate production in E. coli.     

Production of L-tartaric acid by immobilized bacterial cells Nocardia tartaricans

Nocardia tartaricans converted sodium cis-epoxysuccinate to L-tartrate. The highest cis-epoxysuccinate hydrolase activity (37.7 U mg^–1) was obtained with 0.02% (w/v) sodium deoxycholate, but this inactivated the cells. Immobilized N. tartaricans in pectate gel showed higher enzyme activity (51 U mg ^–1) compare to the free cells (8.9 U mg ^–1). After 450 days, the immobilized cells still possessed 0.65 U mg ^–1, i.e. 30% of the initial enzyme activity.     

Nitrite uptake by Chlamydomonas reinhardtii cells immobilized in calcium alginate

When an initial cell loading of about 30–40 µg chlorophyll (Chl)·g^–1 gel and alginate suspension of 3% (w/v) were used for immobilization of Chlamydomonas reinhardtii, the resulting cell beads showed optimum nitrite uptake rate, at 30° C and pH 7.5, of 14 µmol NO _inf2 ^sup– ·mg^–1 Chl·h^–1, the photosynthetic and respiratory activities being about 120 µmol O₂ produced·mg^–1 Chl·h^–1, and 40 µmol O₂ consumed ·mg^–1 Chl·h^–1, respectively. The nitrite uptake activity required CO₂ in the culture and persisted after 8 days of cells immobilization, or in the presence of 0.2 mm ammonium in the medium. Our data indicate that alginate-entrapped C, reinhardtii cells may provide a stable and functional system for removing nitrogenous contaminants from waste-waters.Correspondence to: C. Vílchez     

Biocatalytic properties of lipase in crude latex from babaco fruit (Carica pentagona)

Biocatalytic activities in proteolysis, lipolysis and interesterification reactions were studied for crude latex from the subtropical plant Carica pentagona. The results reveal that crude Carica pentagona latex exhibits equivalent proteolytic activities (5.73 units mg^–1) and lipolytic activities (1.01 units mg^–1) compared to the well-known Carica papaya, the commercially source for papain (4.57 units mg^–1 and 0.90 units mg^–1 respectively). Therefore, in interesterification reactions, Carica pentagona latex shows interesting lipase properties (0.77 units mg^–1) higher than commercial Carica papaya latex (0.28 units mg^–1).     

Model aided design of repeated fed-batch penicillin fermentation

Structured models of antibiotic fermentation that quantify maturation and aging of product forming biomass are fitted to experimental data. Conditions of superiority of repeated fed batch cultivation are characterized on the basis of a performance criterion that includes penicillin productivity and costs of operation. Emphasis is placed on the relevance of such research to the model aided design of optimal cyclic operation.List of Symbols c IU/mg cost factor - D s^–1 dilution rate - J IU · cm^–3 · h^–1 net productivity - k _p IU · mg^–11 · h^–1 specific product formation rate - k _pm IU · mg^–1 · h^–1 maximum specific product formation rate - p IU/cm³ concentration of penicillin - T s final time of fermentation - t s fermentation time - X kg/m³ concentration of biomass dry weight - X ₁kg/m³ concentration of young, immature biomass - X ₂ kg/m³ concentration of mature product forming biomass - X _c kg/m³ biomass concentration of the end of growth phase - X _mkg/m³ maximum biomass concentration Greek Letters s^–1 specific maturation rate - s^–1 specific aging rate - s^–1 specific growth rate - _m s^–1 maximum specific growth rate - _p s^–1 specific growth rate during the product formation phase - s cycle time - % volume fraction of draw-off Abbreviations CC chemostat culture - RFBC repeated fed batch culture - RBC repeated batch culture     

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。     

Versicolorin A hemiacetal,hydroxydihydrosterigmatocystin, and aflatoxin G2a reductase activity in extracts fromAspergillus parasiticus

Versicolorin A hemiacetal was converted to versicolorin C in cell-free systems fromAspergillus parasiticus. The rate of reaction catalyzed by the 35–70% ammonium sulfate fraction was 0.43 nmol min^–1 mg^–1 with NADPH as cosubstrate and 0.17 nmol. min^–1 mg^–1 with NADH at 25°C at pH 7.4. The product from incubation of 17-hdyroxy-16,17-dihydrosterigmatocystin with the 35–70% ammonium sulfate fraction and NADPH was a polar compound which was converted to dihydrosterigmatocystin by 0.4 M HCl. The olar comound is proposed to be the 14,17-hydrated open-chain derivative of dihydrosterigmatocystin. Aflatoxin G_2a was also reduced in this system to a polar product tentatively identified as the 13,16-hydrated open-chain derivative of AFG₂. The reductase activity may be involved in the formation of reduced intermediates and aflatoxins in cultures ofA. parasiticus.     

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.     

Production of cellulases in batch culture using a mutant strain of Trichoderma reesei growing on soluble carbon source

Trichoderma reesei Rut-C30 is a highly derepressed mutant which synthesised active cellulases in culture media containing glucose and lactose as the only carbon sources. The maximum biomass, filter paper and specific filter paper activities for cell growth on 20 g glucose l^–1 were 20 g dry cell wt l^–1, 1.9 FPU ml^–1 and 4.8 FPU mg^–1 protein respectively, while on 40 g glucose l^–1 were 25 g dry cell wt l^–1, 4.5 FPU ml^–1 and 6.2 FPU mg^–1 protein, respectively. This strain had a higher specific filter paper activity (6.2 FPU mg^–1 protein) than was produced by other T. reesei mutants (3.6 FPU mg^–1 protein).     

Lactic acid production by aggregated continuous cultures of Lactobacillus acidophilus under aerobic conditions

Summary The ability of Lactobacillus acidophilus to aggregate, to produce lactic acid for a long term continuous fermentation process and to exist as aggregate cell cultures in a gas-lift reactor under aerobic conditions was studied. The main product of fermentation was lactic acid and only the traces of other end-products were determined. The highest fermentation efficiency of lactic acid was 98.6% and the highest productivity was 9.6 g.l^–1.h^–1 of lactic acid.