Improvement of chloroperoxidase stability by covalent immobilization on chitosan membranes

Chloroperoxidase (CPO) from Caldariomyces fumago was optimally covalently immobilized on chitosan membranes pretreated with 0.8 M glutaraldehyde at pH 3.5 to give 3.18 mg CPO g⁻¹ support. Using monochlorodimedone (MCD) as assay substrate, the immobilized-CPO retained 40% activity at 50°C after 40 min whereas free CPO retained only 0.02%. The residual activity for immobilized-CPO was 99 and 58% compared with 68 and 43% for free CPO in the presence of 1.5 M urea and 300 μM H₂O₂, respectively, after 20 h.     

Chloroperoxidase production by Caldariomyces fumago biofilms

Chloroperoxidase (CPO) is a versatile enzyme, which is secreted by the marine fungus Caldariomyces fumago (Leptoxyphium fumago). However, the application of the enzyme is hampered by its high price, which is due to the costly, labor‐intensive purification process. One challenge of the downstream process is the removal of a coproduced black pigment that forms a complex with the active enzyme. While strain development can be considered as an option to reduce the synthesis of the interfering pigment, the metabolism of the microorganism can be altered alternatively by using the biofilm growth mode of the fungus. The aim of this study was to reduce pigment formation during CPO synthesis. We investigated for the first time CPO production during C. fumago biofilm growth initiated through the presence of different microstructured stainless steel surfaces (material number: 1.4571; AISI 316Ti). CPO production by C. fumago was similar when grown as a biofilm or in suspension, whereas pigment formation was drastically reduced by cells grown on moderately structured surfaces (R_a = 0.13 ± 0.02 μm). The possibilities of biofilm growth for changing cell properties and for continuous fermentation are discussed.     

Continuous and Batch Production of Chloroperoxidase by Mycelial Pellets of Caldariomyces fumago in an Airlift Fermentor

Batch and continuous production of the extracellular heme glycoprotein chloroperoxidase (CPO) was studied with an airlift fermentor. We induced Caldariomyces fumago CMI 89362 to form pellets by transferring a small inoculum volume in preculture prior to growth in a 1-liter fermentor. Continuous replacement of the fructose-salts medium (dilution rate, 0.008 h⁻¹) supported continuous CPO formation at an average concentration of 128 ± 10 mg of CPO liter⁻¹ for 8 days. Optimum CPO production rates averaged 1.2 ± 0.1 mg of CPO h⁻¹ at dilution rates below 0.033 h⁻¹. Varying the carbohydrate content of the feed solution or the time of starting the feed did not significantly alter the amount of CPO produced. Batch fermentation in the airlift fermentor resulted in maximum CPO concentrations of 280 ± 80 mg of CPO liter⁻¹, although on two separate occasions CPO concentrations reached 400 to 450 mg liter⁻¹, which was double the amount obtained by free hyphae in shake flask culture.     

Fast and efficient purification of chloroperoxidase from C. fumago

Chloroperoxidase (CPO) from Caldariomyces fumago is a highly versatile and synthetically important enzyme. Nevertheless, the actual technical application is limited, mainly due to the high costs for purified preparations. Here, a novel fast and very efficient method for the purification of CPO has been developed. It involves separation of CPO from black fungal pigment and most side proteins in aqueous biphasic systems followed by a single chromatographic step. A residual yield of ∼70.4% and a specific activity of 2900 U/mg were obtained. Sufficient purity for technical application was already achieved after biphasic extraction, where CPO recovery from culture broth yielded about 100%. Time required for purification ranges between 30 min and 1 day depending on the desired degree of purity. Thus, a protocol is presented that reduces consumption of time and material and enhances the enzyme quality.     

Inactivation of chloroperoxidase by arginine

Inactivation of chloroperoxidase (CPO) from Caldariomyces fumago by arginine was investigated. It was found that the red native CPO solution was turned into a stable green species with a concomitant shift of the Soret band from 398 to 425 nm in the presence of arginine. The green CPO lost almost all of its catalytic activity, and this inactivation was irreversible.Differential UV–vis spectrophotometry was used to examine the binding properties of arginine to CPO. The formation of CPO-arginine (1:1) complex was highly pH-dependent. Fluorescence investigation revealed the exposure degree of prosthetic group increased. Kinetic analysis indicated that CPO has both a high affinity and specificity to arginine.This inactivation may be caused mainly by the binding of guanidinium group in arginine to the acid–base catalytic group Glu183 in CPO. The change of surrounding environment around heme induced by the interaction of heme propionates with arginine and the occupying of the sixth axial ligand position of heme iron by hydroxyl are also reasons bringing on this inactivation.     

Production of saponions and polysaccharide in the presence of lactoalbumin hydrolysate in <Emphasis Type="Italic">Panax quinquefolium</Emphasis> L. cells cultures

In this article, ginsenosides and polysaccharide contents in suspension cells and native roots of Panax quinquefolium L. were studied. In order to enhance the contents of ginsenosides and polysaccharide in P. quinquefolium suspension cells, we tested the effects of lactoalbumin hydrolysate on the growth of P. quinquefolium suspension cell, synthesis of ginsenosides and polysaccharide in flask and bioreactor. In flask culture, cells growth ratio was significantly enhanced by the addition of lower concentration of lactoalbumin hydrolysate. Addition of 100 mg L⁻¹ lactoalbumin hydrolysate significantly enhanced the contents of total saponins (5.44 mg g⁻¹ DW) and the contents were 3.89-fold over the control group. Addition of lactoalbumin hydrolysate significantly promoted the accumulation of polysaccharide, except 200 mg L⁻¹ lactoalbumin hydrolysate. The highest total saponins yield (36.72 mg L⁻¹ DW) and polysaccharide yield (0.83 g L⁻¹ DW) were obtained at 100 mg L⁻¹ lactoalbumin hydrolysate. In a 5-L stirred tank bioreactor, the highest contents of total saponins and TRb group ginsenosides were achieved on day 26, while the effect of lactoalbumin hydrolysate on the contents of TRg group ginsenosides were insignificant. This result suggests that lactoalbumin hydrolysate might have triggered the enzyme activities for the synthesis of TRb group ginsenosides. Overall, the highest total saponins yield (31.37 mg L⁻¹ DW) and polysaccharide yield (1.618 g L⁻¹ DW) were obtained on day 26 and day 24 respectively and the polysaccharide yield was 1.95-fold higher than the shake flask culture (0.83 g L⁻¹ DW). These results provided theoretical reference for two-stage culture in suspension cells of P. quinquefolium in bioreactor.     

Overexpression and characterization of cyprosin B in transformed suspension cells of <Emphasis Type="Italic">Cynara cardunculus</Emphasis>

Cynara cardunculus suspension cells were transformed by particle bombardment to overexpress the cypro11 gene coding for cyprosin B. Green fluorescent protein, used as a visual reporter through mgfp4-ER gene, facilitates the screening of transformed cells at the initial stages when antibiotics cause generalized cell death. mgfp4-ER lacks a cryptic intron and has an endoplasmic reticulum target sequence, these traits conferring an adequate use as screenable marker for transformed cells. Selected transformed cells, grown in a bioreactor, produced 3.8 g dcw l⁻¹ of biomass, 80 mg l⁻¹ of total protein and 2,060 U ml⁻¹ of enzymatic activity. Specific activity of cyprosin B, purified by anionic-exchange chromatography, was 215 U mg⁻¹ with a purification degree of 8.3-fold. The cyprosin B activity is optimal at 42°C for pH 5.1 and is inhibited by pepstatin A. The results encourage the overexpression of cypro11 gene in transformed C. cardunculus cells leading to high yields of cyprosin B production in bioreactor, which can be considered adequate for industrial production.     

Factors affecting the production of <Emphasis Type="SmallCaps">l</Emphasis>-xylulose by resting cells of recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis>

Factors affecting the production of the rare sugar l-xylulose from xylitol using resting cells were investigated. An E. coli BPT228 strain that recombinantly expresses a gene for xylitol dehydrogenase was used in the experiments. The ratio of xylitol to l-xylulose was three times lower in the cytoplasm than in the medium. The effects of pH, temperature, shaking speed, and initial xylitol concentration on l-xylulose production were investigated in shaking flasks using statistical experimental design methods. The highest production rates were found at high shaking speed and at high temperature (over 44°C). The optimal pH for both productivity and conversion was between 7.5 and 8.0, and the optimal xylitol concentration was in the range 250–350 g l⁻¹. A specific productivity of 1.09 ± 0.10 g g⁻¹ h⁻¹ was achieved in a bioreactor. The response surface model based on the data from the shake flask experiments predicted the operation of the process in a bioreactor with reasonable accuracy.     

Improvement of efficiency of genetic transformation for <Emphasis Type="Italic">Dunaliella salina</Emphasis> by glass beads method

Dunaliella salina has been exploited as a new type of bioreactor due to its unique advantages. However, this bioreactor application was restricted for absence of a high-efficiency and stable transformation method at present. In the present study, the cells of D. salina were transformed by glass beads. The results of histochemical staining revealed that the GUS gene was successfully expressed in the positive transformants, and PCR and PCR-Southern blot analysis further demonstrated that the bar gene was integrated into the D. salina genome. Moreover, the three transformation methods, including glass beads, bombardment particle and electroporation, were compared for screening a high-efficiency transformation method for gene engineering of D. salina. The results showed that transformation efficiency of the glass beads was the highest, approximately 10² transformants/μg DNA. It is concluded that the established glass beads method has been demonstrated to be an optimal transformation way for D. salina.     

Bioreactor type affects the accumulation of phenolic acids and flavonoids in microshoot cultures of Schisandra chinensis (Turcz.) Baill.

Microshoots of the East Asian medicinal plant species Schisandra chinensis (Chinese magnolia vine) were grown in bioreactors characterized by different construction and cultivation mode. The tested systems included two continuous immersion systems—a cone-type bioreactor (CNB) and a cylindric tube bioreactor (CTB), a nutrient sprinkle bioreactor (NSB), and two temporary immersion systems (TIS)—RITA® and Plantform. Microshoots were grown for 30 and 60 days in the MS medium enriched with 1 mg l^?1 NAA and 3 mg l^?1 BA. The accumulation of two groups of phenolic compounds: phenolic acids and flavonoids in the bioreactor-grown S. chinensis biomass, was evaluated for the first time. In the microshoot extracts, seven phenolic acids: chlorogenic, gallic, p–hydroxybenzoic, protocatechuic, syringic, salicylic and vanillic, and three flavonoids: kaempferol, quercitrin and rutoside, were identified. The highest total amount of phenolic acids (46.68 mg 100 g^?1 DW) was recorded in the biomass maintained in the CNB for 30 days. The highest total content of flavonoids (29.02 mg 100 g^?1 DW) was found in the microshoots maintained in the NSB for 30 days. The predominant metabolites in all the tested systems were: gallic acid (up to 10.01 mg 100 g^?1 DW), protocatechuic acid (maximal concentration 16.30 mg 100 g^?1 DW), and quercitrin (highest content 21.00 mg 100 g^?1 DW).

     

Enhancing oxidation activity and stability of iso-1-cytochrome c and chloroperoxidase by immobilization in nanostructured supports

The immobilization of enzymes in inorganic materials has been widely used because it can produce an enhancement of the catalytic stability and enzymatic activity. In this article, the effect of the immobilization of iso-1-cytochrome c (CYC-Sc) from Saccharomyces cerevisiae and chloroperoxidase (CPO) from Caldariomyces fumago on the enzyme stability and catalytic oxidation of styrene was studied. The immobilization was carried out in three silica nanostructured supports with different pore size MCM-41 (3.3 nm), SBA-15 (6.4 nm) and MCF (12.1 nm). The adsorption parameters and leaching degree of immobilized enzymes were determined. Catalytic parameters of immobilized and free enzymes were determined at different temperatures (20–60 °C) and in different acetonitrile/water mixtures (15–85% of acetonitrile). The results show that there is low leaching of the enzymes in the three supports assayed and the adsorption capacity (q_max) was higher as the pore size of the support increased. The pore size also produces the enhancement of peroxidase activities on the styrene oxidation. Thus, CPO adsorption into SBA-15 and MCF showed remarkable thermal and solvent stabilities at 40 °C showing a total turnover numbers of 48,000 and 54,000 times higher than free CPO, respectively. The enhancement of activity and stability doubtless is interesting for the potential industrial use of peroxidases.     

Immobilization of Chloroperoxidase on Aminopropyl-Glass

Chloroperoxidase (CPO) purified from Caldariomyces fumago CMI 89362 was covalently bound to aminopropyl-glass by using a modification of an established method. Acid-washed glass was derivatized by using aminopropyltriethoxysilane, and the enzyme was ionically bound at low ionic strength. Further treatment with glutaraldehyde covalently linked the enzyme to the glass beads in an active form. No elution of bound activity from glass beads could be detected with a variety of washings. The loading of enzyme protein to the glass beads was highest, 100 mg of CPO per g of glass, at high reaction ratios of CPO to glass, but the specific activity of the immobilized enzyme was highest, 36% of theoretical, at low enzyme-to-carrier ratios. No differences in the properties of the soluble and immobilized enzymes could be detected by a number of criteria: their pH-activity and pH-stability profiles were similar, as were their thermal stabilities. After five uses, the immobilized enzyme retained full activity between pH 6.0 and 6.7.     

Carbon source pulsed feeding to attain high yield and high productivity in poly(3-hydroxybutyrate) (PHB) production from soybean oil using <Emphasis Type="Italic">Cupriavidus necator</Emphasis>

Poly(3-hydroxybutyrate) (PHB) biosynthesis from soybean oil by Cupriavidus necator was studied using a bench scale bioreactor. The highest cell concentration (83 g l⁻¹) was achieved using soybean oil at 40 g l⁻¹ and a pulse of the same concentration. The PHB content was 81% (w/w), PHB productivity was 2.5 g l⁻¹ h⁻¹, and the calculated Y_p/s value was 0.85 g g⁻¹. Growth limitation and the onset of PHB biosynthesis took place due to exhaustion of P, and probably also Cu, Ca, and Fe.     

Semicontinuous and Continuous Production of Chloroperoxidase by Caldariomyces fumago Immobilized in k-Carrageenan

Three strains of Caldariomyces fumago were immobilized in 4% k-carrageenan and tested for semicontinuous production of chloroperoxidase (CPO). Over an 80-day period, growing in defined medium, C. fumago strains CMI 89362 and ATCC 11925 produced enzyme concentrations of 99 and 71 mg/liter, respectively, during six production periods of 12 to 14 days, while C. fumago DAOM 137632 produced only 24 mg of CPO per liter during six growth periods of 10 days. CPO production was unaffected by various regimens of washing between transfers. Mycelial growth was primarily restricted to the head surface, and bead size increased linearly with time. Attempts to restrict growth but maintain CPO production were unsuccessful. Pigment production, fructose utilization, and pH change in the immobilized cell cultures compared closely with the growth characteristics of free cell cultures. By using an airlift tower fermentor with an external loop run with continuous medium replacement of 20 ml/h (D = 0.016), strain CMI 89362 in bead form produced CPO at 40 mg/liter for 11 days.     

Identification of a Caldariomyces fumago Mutant Secreting an Inactive Form of Chloroperoxidase Lacking the Heme Group and N-Glycans

By mutant colony screening of Caldariomyces fumago a mutant was isolated which was slightly greenish on fructose minimal medium and grew slower in comparison to the wild type. The supernatant samples lacked the Soret band typical for the heme group of the CPO and nearly no CPO activity was detected. SDS-PAGE analysis of mutant culture supernatant samples showed production of a 38–40 kDa protein while wild type samples contain the 42 kDa CPO protein. Protein identification using nanoLC-ESI-MS/MS was performed and based on three peptides the protein in the mutant culture was identified as CPO. No differences in the CPO gene sequences of wild type and mutant were found indicating a post-translational defect in protein maturation. Deglycosylation experiments using CPO from wild type and mutant were carried out. After removing N-linked oligosaccharides from wild type CPO a protein band at 38–40 kDa was detected. Our results reveal that the mutant protein lacks the heme group as well as the N-glycans.     

Effect of culture medium composition on Trichoderma reesei’s morphology and cellulase production

The objective of this study was to determine how fungal morphology influences the volumetric cellulase productivity of Trichoderma reesei cultured in four media with lactose and lactobionic acid as fed-batch in a 7 L stirred tank bioreactor. The use of a cellulose–yeast extract culture medium yielded the highest enzyme production with a volumetric enzyme activity of 69.8 U L⁻¹ h⁻¹, and a maximum fungal biomass of 14.7 g L⁻¹. These findings were associated with the following morphological characteristics of the fungus: total mycelia was 98% of total mean projected area, mean hyphae length of 10 mm, mean hyphae volume of 45.1 mm³, mean hyphae diameter of 7.9 μm, number of branches 9, and number of tips per hypha 29. A positive correlation was found between the total mycelia, the number of tips and the volumetric enzyme productivity, indicating the weight of these variables on the enzyme productivity.     

Cost-effective production of <Emphasis Type="Italic">Bacillus licheniformis</Emphasis> using simple netting bag solid bioreactor

A novel simple solid state fermentation method, netting bag bioreactor (Φ 120 × 800 mm), was developed and used to cultivate Bacillus licheniformis as probiotics. High spore yield (1.2 × 10¹¹ CFU/g dry substrate) has been obtained by using this method. Comparing to the tray bioreactor and the packed bed bioreactor for Bacillus fermentation, the netting bag method was more cost-effective, time- and space-saving and the material cost is also as low as ca. US $293 per 1,000 kg spores. Thus, netting bag SSF can be widely applied to produce probiotic bacteria in developing areas.     

Improved oxygen transfer and increased l-lactic acid production by morphology control of Rhizopus oryzae in a static bed bioreactor

Rhizopus oryzae was immobilized on a cotton matrix in a static bed bioreactor. Compared with free cells in a stirred tank bioreactor, immobilized R. oryzae in this bioreactor gave higher lactic acid production but lower ethanol production. The highest lactic acid production rate (2.09 g/L h) with the final concentration of 37.83 g/L from 70 g/L glucose was achieved when operating the bioreactor at 700 rpm and 0.5 vvm air. To better understand the relationship between shear effects (agitation and aeration) and R. oryzae morphology and metabolism, oxygen transfer rate, fermentation kinetics, and lactate dehydrogenase activity were determined. In immobilized cell culture, higher oxygen transfer rate and lactic acid production were achieved but lower lactate dehydrogenase activity was found as compared with those in free cell culture operated at the same conditions. These results clearly imply that mass transport was the rate controlling step in lactic acid fermentation by R. oryzae.     

Monoterpenes as novel substrates for oxidation and halo-hydroxylation with chloroperoxidase from Caldariomyces fumago

Chloroperoxidase (CPO) from Caldariomyces fumago was analysed for its ability to oxidize ten different monoterpenes with hydrogen peroxide as oxidant. In the absence of halide ions geraniol and, to a lesser extent, citronellol and nerol were converted into the corresponding aldehydes, whereas terpene hydrocarbons did not serve as substrates under these conditions. In the presence of chloride, bromide and iodide ions, every terpene tested was converted into one or more products. (1S)-(+)-3-carene was chosen as a model substrate for the CPO-catalysed conversion of terpenes in the presence of sodium halides. With chloride, bromide and iodide, the reaction products were the respective (1S,3R,4R,6R)-4-halo-3,7,7-trimethyl-bicyclo[4.1.0]-heptane-3-ols, as identified by ¹H and ¹³C nuclear magnetic resonance. These product formations turned out to be strictly regio- and stereoselective and proceeded very rapidly and almost quantitatively. Initial specific activities of halohydrin formation increased from 4.22 U mg⁻¹ with chloride to 12.22 U mg⁻¹ with bromide and 37.11 U mg⁻¹ with iodide as the respective halide ion. These results represent the first examples of the application of CPO as a highly efficient biocatalyst for monoterpene functionalization. This is a promising strategy for ‘green’ terpene chemistry overcoming drawbacks usually associated with cofactor-dependent oxygenases, whole-cell biocatalysts and conventional chemical methods used for terpene conversions.     

Bioreactor application on adventitious root culture of <Emphasis Type="Italic">Astragalus membranaceus</Emphasis>

Astragalus membranaceus is one of the most widely used traditional medicinal herbs in China, but the time required to generate a useful product in the field production is long. The growth of adventitious root cultures was compared between cultures grown in solid, liquid, or a 5-L balloon-type bubble bioreactor. The maximum growth ratio (final dry weight/initial dry weight) was determined for adventitious roots grown in the bioreactor. Studies carried out to optimize biomass production of adventitious roots compared adventitious root growth from various inoculum root lengths, inoculum densities, and aeration volume in the bioreactors. The maximum growth ratio occurred in treatments with a 1.5-cm inoculum root length, with 30 g (fresh weight) of inoculum per bioreactor or with an aeration volume of 0.1 vvm (air volume/culture medium volume per min). The polysaccharide, saponin, and flavonoid content of roots from bioreactor-grown cultures were compared to roots from field-grown plants grown for 1 and 3 yr. Total polysaccharide content of adventitious roots in the bioreactor (30.0 mg g⁻¹ dry weight (DW)) was higher than the roots of 1-yr-old (13.8 mg g⁻¹ DW) and 3-yr-old (21.1 mg g⁻¹ DW) plants in the field. Total saponin (3.4 mg g⁻¹ DW) and flavonoid (6.4 mg g⁻¹ DW) contents were nearly identical to 3-yr-old roots and higher than that of 1-yr-old roots under field cultivation.