Genetic engineering of doxorubicin production in Streptomyces peucetius: a review

The genetics and biochemistry of daunorubicin and doxorubicin production by Streptomyces peucetius is reviewed, with a focus on how such information can be used for the genetic engineering of strains having improved titers of these two antitumor antibiotics. Received 23 February 1999/ Accepted in revised form 22 March 1999     

Enhanced production of a thermostable mannanase by immobilized cells of <Emphasis Type="Italic">Bacillus</Emphasis><Emphasis Type="Italic">subtilis</Emphasis> on various membranes

Cells of the thermophilic Bacillus subtilis WY34 were immobilized on various formaldehyde-activated polymer membranes and the immobilized cells were used for the production of thermostable mannanase in flasks. The results showed that polyethersulfone membranes (PES) and nylon-6 membranes were the most suitable supports for cell immobilization to produce the mannanase. Moreover, PES and nylon-6 membranes immobilized cells provided 1.78- and 1.74-fold higher mannanase activity compared to the control after 4 days of cultivation, respectively. The immobilized cells on PES and nylon-6 membranes had good stability and retained 131.5 and 114.3% of ability of enzyme production even after six cycles of repeated batch fermentation, respectively. Active cell growth was observed by scanning electron microscopy (SEM) after 16 days (four cycles) repeated batch cultivation. Therefore, the membrane-immobilized cells of B. subtilis WY34 can be proposed as an effective biocatalyst for repeated usage for production of the thermostable mannanase.     

Ultrahigh-cell-density heterotrophic cultivation of the unicellular green microalga Scenedesmus acuminatus and application of the cells to photoautotrophic culture enhance biomass and lipid production

Although production of biodiesels from microalgae is proved to be technically feasible, a commercially viable system has yet to emerge. High-cell-density fermentation of microalgae can be coupled with photoautotrophic cultivation to produce oils. In this study, by optimizing culturing conditions and employing a sophisticated substrate feed control strategy, ultrahigh-cell-density of 286 and 283.5 g/L was achieved for the unicellular alga Scenedesmus acuminatus grown in 7.5-L bench-scale and 1,000-L pilot-scale fermenters, respectively. The outdoor scale-up experiments indicated that heterotrophically grown S. acuminatus cells are more productive in terms of both biomass and lipid accumulation when they are inoculated in photobioreactors for lipid production as compared to the cells originally grown under photoautotrophic conditions. Technoeconomic analysis based on the pilot-scale data indicated that the cost of heterotrophic cultivation of microalgae for biomass production is comparable with that of the open-pond system and much lower than that of tubular PBR, if the biomass yield was higher than 200 g/L. This study demonstrated the economic viability of heterotrophic cultivation on large-scale microalgal inocula production, but ultrahigh-productivity fermentation is a prerequisite. Moreover, the advantages of the combined heterotrophic and photoautotrophic cultivation of microalgae for biofuels production were also verified in the pilot-scale.     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-lactic acid from a mixture of xylose and glucose by co-cultivation of lactic acid bacteria

The production of optically pure lactic acid in a high yield from xylose or a mixture of xylose and glucose, which is a model hydrolysate of lignocellulose, is described. In a single cultivation, Enterococcus casseliflavus produced 38 g/l of lactic acid with an optical purity of 96% enantiomeric excess (ee) and 6.4 g/l of acetic acid from 50 g/l of xylose when MRS medium was used. When a mixture of 50 g/l of xylose and 100 g/l of glucose was used as the carbon source in a cultivation of E. casseliflavus alone, glucose was converted to lactic acid in the early phase of the cultivation but xylose was hardly consumed. In a co-cultivation where E. casseliflavus and Lactobacillus casei specific for glucose were simultaneously inoculated, little or no lactic acid was produced after the glucose was almost consumed. A co-cultivation with two-stage inoculation (in which E. casseliflavus was added at a cultivation time of 40 h after L. casei cells were inoculated) resulted in complete consumption of 50 g/l of xylose and 100 g/l of glucose. In the co-cultivation, 95 g/l of lactic acid with a high optical purity of 96% ee was obtained at 192 h. Such a co-cultivation using two microorganisms specific for each sugar is considered to be one promising cultivation technique for the efficient production of lactic acid from a sugar mixture derived from lignocellulose.     

Mammalian cell cultivation using nutrients extracted from microalgae

Mammalian cells have been used in various research fields. More recently, cultured cells have been used as the cell source of “cultured meat.” Cell cultivation requires media containing nutrients, of which glucose and amino acids are the essential ones. These nutrients are generally derived from grains or heterotrophic microorganisms, which also require various nutrients derived from grains. Grain culture, in turn, requires many chemical fertilizers and agrochemicals, which can cause greenhouse gas emission and environmental contamination. Furthermore, grain production is greatly influenced by environmental changes. In contrast, microalgae efficiently synthesize various nutrients using solar energy, water, and inorganic substances, which are widely used in the energy sector. In this study, we aimed to apply nutrients extracted from microalgae in the culture media for mammalian cell cultivation. Glucose was efficiently extracted from Chlorococcum littorale or Arthrospira platensis using sulfuric acid, whereas 18 of the 20 proteinogenic amino acids were efficiently extracted from Chlorella vulgaris using hydrochloric acid. We further investigated whether nutrients present in the algal extracts could be used in mammalian cell cultivation. Although almost all C2C12 mouse myoblasts died during cultivation in a glucose- and amino acid-free medium, the cell death was rescued by adding algal extract(s) into the nutrient-deficient media. This indicates that nutrients present in algal extracts can be used for mammalian cell cultivation. This study is the first step toward the establishment of a new cell culture system that can reduce environmental loads and remain unaffected by the impact of environmental changes.     

Cell engineering of <Emphasis Type="Italic">Escherichia coli</Emphasis> allows high cell density accumulation without fed-batch process control

A set of mutations in the phosphoenolpyruvate:carbohydrate phosphotransferase system (PTS) was used to create Escherichia coli strains with a reduced uptake rate of glucose. This allows a growth restriction, which is controlled on cellular rather than reactor level, which is typical of the fed-batch cultivation concept. Batch growth of the engineered strains resulted in cell accumulation profiles corresponding to a growth rate of 0.78, 0.38 and 0.25 h⁻¹, respectively. The performance of the mutants in batch cultivation was compared to fed-batch cultivation of the wild type cell using restricted glucose feed to arrive at the corresponding growth profiles. Results show that the acetate production, oxygen consumption and product formation were similar, when a recombinant product was induced from the lacUV5 promoter. Ten times more cells could be produced in batch cultivation using the mutants without the growth detrimental production of acetic acid. This allows high cell density production without the establishment of elaborate fed-batch control equipment. The technique is suggested as a versatile tool in high throughput multiparallel protein production but also for increasing the number of experiments performed during process development while keeping conditions similar to the large-scale fed-batch performance.     

Animal component‐free Agrobacterium tumefaciens cultivation media for better GMP‐compliance increases biomass yield and pharmaceutical protein expression in Nicotiana benthamiana

Transient expression systems allow the rapid production of recombinant proteins in plants. Such systems can be scaled up to several hundred kilograms of biomass, making them suitable for the production of pharmaceutical proteins required at short notice, such as emergency vaccines. However, large‐scale transient expression requires the production of recombinant Agrobacterium tumefaciens strains with the capacity for efficient gene transfer to plant cells. The complex media often used for the cultivation of this species typically include animal‐derived ingredients that can contain human pathogens, thus conflicting with the requirements of good manufacturing practice (GMP). We replaced all the animal‐derived components in yeast extract broth (YEB) cultivation medium with soybean peptone, and then used a design‐of‐experiments approach to optimize the medium composition, increasing the biomass yield while maintaining high levels of transient expression in subsequent infiltration experiments. The resulting plant peptone Agrobacterium medium (PAM) achieved a two‐fold increase in OD₆₀₀ compared to YEB medium during a 4‐L batch fermentation lasting 18 h. Furthermore, the yields of the monoclonal antibody 2G12 and the fluorescent protein DsRed were maintained when the cells were cultivated in PAM rather than YEB. We have thus demonstrated a simple, efficient and scalable method for medium optimization that reduces process time and costs. The final optimized medium for the cultivation of A. tumefaciens completely lacks animal‐derived components, thus facilitating the GMP‐compliant large‐scale transient expression of recombinant proteins in plants.     

Daunorubicin forms a specific complex with a secreted serine protease of Streptomyces peucetius

Daunorubicin forms specific complex with an extracellular protease in the Streptomyces peucetius culture. The drug-protein complex co-migrates in non-denaturing PAGE as a red band. De novo peptide sequencing by nano-LC–ESI–MS/MS and MASCOT analysis identified the daunorubicin binding protein as serine protease precursor. The same protease precursor was purified sans the daunorubicin, from the mutant named ΔDPSAmut, which is deficient in daunorubicin production. Daunorubicin was added to ΔDPSAmut culture and the protease readily formed the daunorubicin-protease complex. Ability of serine protease precursor to form a selective complex with daunorubicin was confirmed by this study. Selective binding of protease to daunorubicin was seen as self-resistance determinant for the organism to survive toxic levels of the drug outside the cell. Daunorubicin-protease complex placed on S. peucetius lawn did not produce clearing zone around it, whereas daunorubicin purified from the complex did produce the clearing zone. Thereby it is concluded that the protease sequesters daunorubicin to prevent its entry into cells. Sequestration of daunorubicin by extracellular protease helps the organism to maintain a steady state sub-inhibitory level of drug around the cells. A new self-resistance determinant is reported here.     

Fed-batch cultivation for the production of clavulanic acid by an immobilized Streptomyces clavuligerus mutant

In order to obtain high productivity of clavulanic acid, a newly-introduced carrier, polyurethane pellet (PUP) Z97-020 was used for the immobilization process. In a stirred-tank bioreactor, batch cultivation by Streptomyces clavuligerus KK immobilized on PUP Z97-020 gave about 3100 mg of clavulanic acid per litre, representing an increase of 200% in productivity compared with that by fed-batch cultivation of free cells (1500 mg/l). However, the clavulanic acid produced rapidly decomposed due to the pH change during batch cultivation. Fed-batch cultivation by immobilized S. clavuligerus KK gave an excellent level of clavulanic acid up to 3250 mg/l, a productivity increase of 220% compared with that by fed-batch cultivation of free cells. These results suggest that immobilization with PUP Z97-020 is a more effective process for the production of clavulanic acid and that the maintenance of pH by fed-batch cultivation with glycerol as a limiting substrate prevents the clavulanic acid from decomposing during the fermentation.     

Production of casein hydrolysates by extracellular acid proteinases of immobilized Humicola lutea cells

Casein hydrolysis was studied during the cultivation of immobilized Humicola lutea cells producing acid proteinases. By monitoring the cultivation with time, various casein hydrolysates could be obtained, from partially modified proteins (yield 80%) with improved emulsion properties to peptones (yield > 50%) with a degree of hydrolysis >40%. The casein from the fermentation medium appeared to be simultaneously a nitrogen source, an inducer of proteinase biosynthesis, and a substrate for the production of casein hydrolysates. Casein (4%) and glucose (2%) ensured optimal cultivation conditions. The fungal cells, immobilized in calcium alginate beads, required a short cultivation time and demonstrated comparable hydrolysis of casein during five to seven reuses in batch mode. Correspondence to: B. Tchorbanov     

The DrrC protein of Streptomyces peucetius, a UvrA-like protein, is a DNA-binding protein whose gene is induced by daunorubicin

DrrC, a daunorubicin resistance protein with a strong sequence similarity to the UvrA protein involved in excision repair of DNA, is induced by daunorubicin in Streptomyces peucetius and behaves like an ATP-dependent, DNA binding protein in vitro. The refolded protein obtained from expression of the drrC gene in Escherichia coli was used to conduct gel retardation assays. DrrC bound a DNA segment containing the promoter region of a daunorubicin production gene only in the presence of ATP and daunorubicin. This result suggests that DrrC is a novel type of drug self-resistance protein with DNA binding properties like those of UvrA. Western blotting analysis with a polyclonal antiserum generated against His-tagged DrrC showed that the appearance of DrrC in S. peucetius is coincident with the onset of daunorubicin production and that the drrC gene is induced by daunorubicin. These data also showed that the DnrN and DnrI regulatory proteins are required for drrC expression. The level of DrrA, another daunorubicin resistance protein that resembles ATP-dependent bacterial antiporters, was regulated in the same way as that of DrrC.     

Physical Factors and Reuse Affect the Production of Cholesterol Oxidase in Reactors Containing Calcium Alginate-Immobilized Rhodococcus equi No. 23

Summary Some physical factors including initial pH of medium, cultivation temperature and shaking speed as well as reuse affecting the production of cholesterol oxidase (CholOx) in reactors containing calcium alginate-immobilized cells of Rhodococcus equi No. 23 were investigated. Results revealed that the free cells showed the maximum CholOx in the culture with an initial pH of 5.0, while culture inoculated with immobilized cells exhibited a broad pH range, 6.0–9.0, for maximum CholOx production. The immobilized and free cells produced the maximum CholOx in the culture incubated at 30 and 25°C, respectively. The CholOx production decreased upon increasing the cultivation temperature. Increasing CholOx activity was also noted for both immobilized and free cells of R. equi No. 23 in the culture with increasing shaking speed. Under the optimal culture conditions, that were established, a higher maximum CholOx production of 0.94 unit/ml was found for immobilized R. equi No. 23 compared to that of 0.84 unit/ml for free cells after 48 h of cultivation. Furthermore, no gel leakage was noted after re-use of the calcium alginate-immobilized R. equi No. 23 for seven consecutive 48 h batch culture. The CholOx production in the seventh cycle was about 60.4% of that obtained in the first cycle.     

Kinetics of daunorubicin transport by P-glycoprotein of intact cancer cells.

Drug permeation across the plasma membrane of multidrug-resistant cells depends on the kinetics of the P-glycoprotein-mediated pump activity as well as on the passive permeation of the drug. We here demonstrate a method to characterize kinetically the pump in intact cells. To this purpose, we examined the membrane-transport properties of daunorubicin in various sensitive cancer cell lines and in their multidrug resistant (MDR) counterparts. First, we determined the passive permeability coefficient for daunorubicin. Then, using a flow-through system, the drug flux into the cell was measured after inhibition of the P-glycoprotein-mediated efflux pump. Combining the two results allowed us to calculate the intracellular free concentration of the drug. In the steady-state, the pump rate must equal the net rate of passive diffusion of the drug and, therefore, the same experiments gave us the pumping rate of daunorubicin. These experiments were then repeated at various extracellular drug concentrations. By plotting the pumping rate versus the intracellular drug concentration, we then characterized the P-glycoprotein kinetically. Four independent methods were used to measure the passive permeability coefficient for the cell line A2780. Similar values were obtained. Maximal pump rates (Vmax) showed a good correlation with the amount of P-glycoprotein in the cell lines used. We obtained saturation curves for the variation of the pump rates with the intracellular daunorubicin concentrations. These curves were typical for positive cooperativity, which provides evidence that at least two binding sites for daunorubicin are present on the active transport system of daunorubicin. The apparent Km values for P-glycoprotein-mediated transport, the intracellular free cytosolic daunorubicin concentrations at half-maximal velocity for the cell lines used, were approximately 1.5 microM. Except for the cell lines with the highest amount of P-glycoprotein, the passive efflux rate of daunorubicin proved to be a substantial part of the total daunorubicin efflux rate for the cell lines used. In cell lines with relatively low levels of P-glycoprotein, passive daunorubicin efflux was even the main route of daunorubicin transport from the cells, determining the intracellular steady-state concentrations of daunorubicin.     

Biotechnological aspects of the production of the anticancer drug podophyllotoxin

The natural lignan podophyllotoxin, a dimerized product of two phenylpropanoid moieties which occurs in a few plant species, is a pharmacologically important compound for its anticancer activities. It is used as a precursor for the chemical synthesis of the anticancer drugs etoposide, teniposide and etopophose. The availability of this lignan is becoming increasingly limited because of the scarce occurrence of its natural sources and also because synthetic approaches for its production are still commercially unacceptable. Biotechnological production using cell culture may be considered as an alternative source. Selection of the best performing cell line, its maintenance and stabilization are necessary prerequisites for its production in bioreactors and subsequent scale-up of the cultivation process to the industrial level. Scale-up of growth and product yield depends on a multitude of factors, such as growth medium, physicochemical conditions, seed inoculum, type of reactor and processing conditions. The composition of the growth medium, elicitors and precursors, etc. can markedly influence the production. Optimum levels of parameters that facilitate high growth and product response in cell suspensions of Podophyllum hexandrum have already been determined by statistical design. P. hexandrum cells have successfully been cultivated in a 3-l stirred-tank bioreactor under low shear conditions in batch and fed-batch modes of operation. The batch kinetic data were used to identify the mathematical model which was then used to develop nutrient-feeding strategies for fed-batch cultivation to prolong the productive log phase of cultivation. An improvement in the production of podophyllotoxin to 48.8 mg l^–1 in a cell culture of P. hexandrum was achieved, with a corresponding volumetric productivity of 0.80 mg l^–1 day^–1, when the reactor was operated in continuous cell-retention mode. Efforts are being made to further enhance its production levels by the development of hairy root culture or by varying the channeling of precursors towards the desired biosynthetic pathway by molecular approaches.     

Poly-3-hydroxybutyrate production byAzotobacter chroococcum

Thirty-seven soil isolates and mutants ofAzotobacter chroococcum tested for poly-3-hydroxybutyrate (PHB) production using Sudan black B staining method were found to be positive. One mutant showed a higher number of PHB-producing cells and maximum number of granules per cell. Using 2% glucose and 15 mmol/L ammonium acetate, PHB production was found to be maximum at 36 and 48 h of growth under submerged cultivation and under stationary cultivation, respectively. PHB production was found to be higher on sucrose and commercial sugar (as carbon sources) as compared to glucose and mannitol. As commercial sugar is cheaper than sucrose it was selected as carbon source for PHB production, that being found to be maximum at 1% concentration. Inorganic nitrogen sources seemed to have no stimulatory effect on the production of PHB. However, ammonium acetate (15 mmol/L) was found to be best for PHB production. Peptone (0.2 %) gave a better yield of PHB under both growth conditions. Using all optimized conditions, PHB production was studied in ten selected strains. Two of them were found to be best PHB producers under both growth conditions, one producing 621 and 740 μg/g dry mass under submerged cultivation and under stationary cultivation, respectively, while the second one produced 589 and 733 μg/g.     

Liposomes as a Model for the Biological Membrane: Studies on Daunorubicin Bilayer Interaction

In this study the interaction of the antitumoral drug daunorubicin with egg phosphatidylcholine (EPC) liposomes, used as a cell membrane model, was quantified by determination of the partition coefficient (K _p). The liposome/aqueous-phase K _p of daunorubicin was determined by derivative spectrophotometry and measurement of the zeta-potential. Mathematical models were used to fit the experimental data, enabling determination of K _p. In the partition of daunorubicin within the membrane both superficial electrostatic and inner hydrophobic interactions seem to be involved. The results are affected by the two types of interaction since spectrophotometry measures mainly hydrophobic interactions, while zeta-potential is affected by both interpenetration of amphiphilic charged molecules in the bilayer and superficial electrostatic interaction. Moreover, the degree of the partition of daunorubicin with the membrane changes with the drug concentration, due mainly to saturation factors. Derivative spectrophotometry and zeta-potential variation results, together with the broad range of concentrations studied, revealed the different types of interactions involved. The mathematical formalism applied also allowed quantification of the number of lipid molecules associated with one drug molecule.     

Production of extracellular enzymes in continuous culture

The production of bacterial enzymes in batch fermentations is compared with results obtained in continuous culture. When studying the production of α-amylase inBacillus subtilis it was found that instability of the enzyme synthesis was due to nonhomogeneity of the population rather than to “the culture’s history” (i.e. succession of several physiological states necessary for the enzyme production). The plasmid contained in the production clone was found to be the factor responsible for the α-amylase production. Predominance of the production clone or of the nonproduction one depends on the cultivation conditions used. As compared with batch cultivation the continuous production yields higher enzyme concentrations under optimal conditions and the fermentor productivity may be four to five times higher.     

Enhanced continuous production of lovastatin using pellets and siran supported growth of Aspergillus terreus in an airlift reactor

Lovastatin, a hypocholesterolemic agent, is a secondary metabolite produced by filamentous microorganism Aspergillus terreus in submerged batch cultivation. Lovastatin production by pellets and immobilized siran cells was investigated in an airlift reactor. The process was carried out by submerged cultivation in continuous mode with the objective of increasing productivity using pellet and siran supported growth of A terreus. The continuous mode of fermentation improves the rate of lovastatin production. The effect of dilution rate and aeration rate were studied in continuous culture. The optimum dilution rate for pellet was 0.02 h⁻¹ and for siran carrier was 0.025 h⁻¹. Lovastatin productivity using immobilized siran carrier (0.0255 g/L/h) was found to be greater than pellets (0.022 g/L/h). The productivity by both modes of fermentation was found higher than that of batch process which suggests that continuous cultivation is a promising strategy for lovastatin production.     

Effects of conditions ofPenicillium funiculosum G-15 cultivation on production of extracellular glucose oxidase

Effects of conditions ofPenicillium funiculosum G-15 cultivation on the production of extracellular glucose oxidase were studied. The data showed that surface and submerged methods of cultivation can be used for obtaining a glucose oxidizing enzyme. The optimum conditions for submerged cultivation (25°C., initial pH 5.0, and aeration of 3 1/1 per min) and surface cultivation (temperature 25°C and initial pH 4.0) providing the maximum levels of glucose oxidase synthesis were determined.     

Improved production of heterologous protein from Streptomyces lividans

Summary Protein-secreting procaryotic host organisms are currently being sought as alternatives to Escherichia coli for recombinant processing. In this study we examined how manipulation of the cultivation conditions can enhance heterologous protein production by Streptomyces lividans. The recombinant S. lividans used in this study expressed and excreted a Flavobacterium enzyme capable of hydrolyzing organophosphates. Initial shake-flask studies demonstrated that supplementing Luria-Bertani medium with moderate amounts of glucose (30 g/l), led to improved enzyme production. In fermentor studies with controlled pH, a further twofold increase in production was observed when glucose was fed continuously as compared to batch cultivation. This improved production in the glucose-fed culture may be related to a reduced accumulation of acids. Continuous feeding of both glucose and tryptone led to a further sixfold increase in production. In addition to enhancing production 25-fold, the efficiency of enzyme production and the specific activity of the excreted enzyme were also improved by glucose and tryptone feeding. These results demonstrate that in addition to genetic manipulations, optimization of cultivation conditions can lead to significant improvements in the production of heterologous proteins from Streptomyces. Offprint requests to: G. F. Payne