Ligninolytic enzyme production and the ability of decolourisation of Poly R-478 in packed-bed bioreactors by Phanerochaete chrysosporium

The production of ligninolytic enzymes by the fungus Phanerochaetechrysosporium BKM-F-1767 (ATCC 24725) in packed-bed tubular bioreactors, operating in semi-solid-state conditions, was studied. Three types of carriers were assayed: cubes of polyurethane foam, cubes of nylon sponge and chopped corncob, in order to determine the more suitable one to produce ligninolytic enzymes by this fungus. The cultivations were carried out in discontinuous and in continuous mode. For discontinuous cultivation, maximum individual manganese-dependent peroxidase (MnP) activities of 1593, 1371 and 346 U/l were achieved in the bioreactors filled with cubes of nylon sponge, cubes of polyurethane foam and with corncob, respectively. On the other hand, lignin peroxidase (LiP) activities about 100 U/l were found in the two former and around 200 U/l in the latter. Moreover, laccase, was detected in all cultures, with average values of 30 U/l. Nonetheless, continuous mode cultivation led to lower ligninolytic enzyme activities than those produced in discontinuous, except in the case of the corncob. Furthermore, the decolourisation of the dye Poly R-478 by the above-mentioned cultures was investigated. The percentage of biological decolourisation reached was about 70% in the bioreactor filled with cubes of nylon sponge whereas it was rather low in the others (around 30%).     

Optimized fed-batch fermentation of L-β-hydroxy isobutyric acid by Yarrowia lipolytica

Yarrowia lipolytica KCCM50506, which transforms isobutyric acid to L-#-hydroxy isobutyric acid (L-#-HIBA), was screened. Chemostat cultures were carried out in jar fermentors at dilution rates of 0.02 h^у to 0.12 h^у. L-#-HIBA fermentation-regulating factors were determined to be specific growth rate, and concentrations of glucose and isobutyric acid in fermentor from analysis of steady-state data. The specific productivity of L-#-HIBA increased as the specific growth rate increased, apparently as a growth-associated type of product formation. A fed-batch culture was carried out under optimum conditions where the concentrations of glucose and isobutyric acid in the fermentor were maintained at 23 g l^у and 9 g l^у, respectively. The concentrations of cells and L-#-HIBA obtained at the end of fermentation were 20 g l^у and 49 g l^у, respectively, corresponding to 2.0 and 2.7 times more than concentrations in batch culture.     

Stainless steel sponge: a novel carrier for the immobilisation of the white-rot fungus Trametes hirsuta for decolourization of textile dyes

Alginate beads, polyurethane foam, nylon sponge and stainless steel sponge were tested as carrier materials for the white-rot fungus Trametes hirsuta for laccase production under submerged fermentation conditions. Stainless steel sponge was the best carrier material leading to the highest laccase activities of up to 800 U/l after 8 days of cultivation. These values are higher than those reported to date operating with inert supports and without inducer addition. In a 1-l bioreactor containing T. hirsuta immobilised on stainless steel sponge laccase activities of about 2200 U/l were obtained when the culture medium was supplemented with 1 mM copper sulphate. There were no operational problems with this system during culturing time. The textile dye Indigo Carmine was almost totally degraded in 3 days by T. hirsuta grown in this bioreactor, while Lanaset Marine was degraded in two successive batches, reaching in the first batch a decolourization percentage of about 82% in 15 h and in the second one by 71% in 28 h. Results obtained after inhibition of growth of T. hirsuta by antibiotics indicated that dye decolourization could not exclusively be attributed to laccase activity.     

Effect of shear on morphology and erythromycin production in Saccharopolyspora erythraea fermentations

A complex medium was used to investigate the effects of shear on the S. erythraea fermentation at 7-l scale. Maximum biomass was 11.1 - 0.5 g l^у at 1250 rpm (tip speed = 4.45 ms^у), whereas it was 12.7 - 0.2 g l^у at 350 rpm (tip speed = 1.07 ms^у). Specific erythromycin production was not stirrer speed dependent in the range of 350 to 1000 rpm and decreased by 10% at stirrer speed of 1250 rpm. Morphological measurements using image analysis showed that the major axis of the mycelia (both freely dispersed and clumps) decreased after the end of the rapid growth phase to a relatively constant value (equilibrium size) dependent on the stirrer speed. The mechanical properties of the cell wall were examined by disruption of fermentation broth in homogeniser and it was shown that mechanical strength of the cell wall increased in a large extent during deceleration phase.     

Physiological energetics of the protobranch bivalve <Emphasis Type="Italic">Yoldia hyperborea</Emphasis> in a cold ocean environment

Yoldia hyperborea is a deposit-feeding circumpolar protobranch that also inhabits muddy sediments of the cold water boreal system of Conception Bay, Newfoundland, Canada. Little is known about this species, despite its wide distribution and frequent high density in the benthos. The present work deals with oxygen consumption and ammonia excretion under cold ambient conditions. Y. hyperborea showed low basal metabolism [0.051 ml O₂ h^у·(g dry weight)^у, T=у°C] and low ammonia excretion rates [4.212 µg·NH₄-N·h^у·(g dry weight)^у, T=у°C]. Low metabolic activity could prove a useful strategy during periods of low food availability. In addition, Y. hyperborea was able to regulate its O₂ consumption rate at very low pO₂ levels, which may be advantageous for a species that may experience periods of hypoxia.     

Effect of veratryl alcohol and manganese (IV) oxide on ligninolytic activity in semi solid cultures of Phanerochaete chrysosporium

An inert carrier (nylon sponge), a non-inert carrier (barley straw) and the addition of veratryl alcohol or manganese (IV) oxide to the cultures were used to study the production of ligninolytic enzymes by Phanerochaete chrysosporium BKM-F-1767 (ATCC 24725) during semi solid state fermentation conditions. By supplementing the medium with these compounds we could stimulate the ligninolytic system of this fungus. The different carriers employed and the effect of adding veratryl alcohol or manganese (IV) oxide to the cultures were compared in order to determine the best system to produce high activities of ligninolytic enzymes. Lignin peroxidase (LiP) activities higher than 500 U/L and manganese-dependent peroxidase (MnP) activities about 1100 U/L were achieved.     

Hypoxia affects root sodium and chloride concentrations and alters water conductance in salt-treated jack pine (<Emphasis Type="Italic">Pinus banksiana</Emphasis>) seedlings

The effects of NaCl were studied in 6-month-old jack pine (Pinus banksiana Lamb.) seedlings growing in solution culture under hypoxic (approximately 2 mg l^у O₂) and well-aerated (approximately 8 mg l^у O₂) conditions. The results showed that hypoxia led to further reduction of stomatal conductance (g_s) in plants treated with 45 mM NaCl. This effect was likely due to a reduction in root hydraulic conductance by both stresses. When applied individually or together, neither 45 mM NaCl nor hypoxia affected cell membrane integrity of needles as measured by tissue electrolyte leakage. Hypoxia did not alter shoot Na⁺ and Cl^m concentrations in NaCl-treated plants. However, root Na⁺ concentrations were lower in NaCl-treated hypoxic plants, suggesting that hypoxia affected the ability of roots to store Na⁺. Hypoxia also induced root electrolyte leakage from NaCl-treated and control plants. The higher root Cl^m concentrations compared with Na⁺ and the positive correlation between root Cl^m concentrations and electrolyte leakage suggest that Cl^m played a major role in salt injury observed in jack pine seedlings. Roots of well-aerated plants treated for 1 week with NaCl contained almost two-fold higher concentration of total non-structural carbohydrates compared with plants from other experimental treatments and these concentrations decreased in subsequent weeks. We suggest that under prolonged hypoxic conditions, roots lose the ability to prevent Cl^m uptake resulting in the increase in root Cl^m concentration, which has damaging effects on root cell membranes.     

A novel fiber optic probe for on-line monitoring of biomass concentrations

A fiber optic biomass probe for on-line measurement of biomass concentration was designed. Results of biomass concentration monitoring experiments with suspended cells of baker's yeast as well as an experimental cultivation of S. cerevisiae are presented. The device was able to observe biomass concentrations of 14 g l^у S. cerevisiae. By means of correlations the capability of estimating the biomass concentration from the probe signal is demonstrated.     

Comparison of two membrane – photobioreactors, with free or immobilized cells, for the production of pigments by a marine diatom

The present study concerns the value enhancement of the microalga Haslea ostrearia. This marine diatom bears the peculiarity of synthesizing and secreting in the culture medium a blue-green pigment named "marennine". Anticancer research, cosmetics and aquaculture are the fields concerned with the utilizations of this hydrosoluble pigment. The aim of the study is to compare the pigment productivity obtained with two types of photobioreactors. In the first process, cells are free and recycled in a bioreactor combined with a membrane ultrafiltration equipment (external loop). In the second system, cells are entrapped in a tubular agar gel layer in a photobioreactor of original design. The influence of nitrate concentration and renewal rate is examined. Experiments, conducted on long term periods (up to 40 d) without any external contamination, revealed that marennine productivities of more than 5-7 mg 10⁹ cell^у d^у can be reached with both bioreactors. The advantages and drawbacks of each process design are also discussed.     

Estimation of axial dispersion in horizontal rotating tubular bioreactor by means of a structured model

A horizontal rotating tubular bioreactor (HRTB) is designed as the combination of a "thin layer bioreactor" and a "biodisc" reactor. The investigation of mixing in HRTB was done by the temperature step method in a wide range of process conditions [residence time (t_z=360036000 s) and bioreactor rotation speed (n=0.0830.917 s^у)]. In all experiments heat losses were detected. A mathematical model based on "tank in series" concept was developed to describe the mixing in HRTB - a "spiral flow" model (SFM) which has incorporated heat losses. However, the simulations of SFM could be used for calculation of temperature response curves for the case when there is no heat losses. These corrected curves were used then to estimate Bodenstein number as a parameter of standard dispersion model (SDM). The obtained Bodenstein numbers were in the range 10-17. The simulations showed that SFM was more capable to describe the mixing in HRTB giving better fitting with experimental measurements than SDM, indicating that mixing pattern in HRTB is too complex to be described with this relatively simple, one-parameter model.     

Fed-batch cultivation of Acetobacter suboxydans for the microbial oxidation of D-sorbitol to L-sorbose

Microbial oxidation of D-sorbitol to L-sorbose is commercially important since it is the only biochemical process in Vitamin-C manufacture. The main bottleneck in the batch oxidation of D-sorbitol is that the process is severely inhibited by sorbitol. By conducting fed-batch fermentation, the inherent substrate inhibition present in batch fermentation can be eliminated. Batch fermentation with an initial sorbitol concentration of 200 g l^у featured a productivity of 14.2 g l^у h^у and a final sorbose concentration of 200 g l^у. Fed-batch fermentation conducted by feeding nutrients containing 600 g l^у of sorbitol at a constant feed rate of 0.36 l h^у yielded a productivity of 17.7 g l^у h^у and a final sorbose concentration of 320 g l^у.     

Influence of k L a on bioconversion of rice straw hemicellulose hydrolysate to xylitol

The effect of overall oxygen mass transfer coefficient (k_La) on the conversion of xylose to xylitol by Candida guilliermondii FTI 20037 was investigated in batch experiments. Rice straw hemicellulose hydrolysate obtained by acid hydrolysis was employed as a xylose-rich medium. The results showed that this bioconversion strongly depended on the aeration rate. The maximum volumetric productivity (0.52 g/l h^у) and the highest xylitol yield (0.73 g/g) were achieved at an overall oxygen mass transfer coefficient of 15 h^у. Under these conditions 80% efficiency in relation to theoretical yield was attained.     

Effect of Corn steep liquor supplementation and scale up on Lactococcus starter production

Summary Three Lactococcus strains (Lactococcus ssp. lactis var. diacetylactis, Lactococcus ssp. lactis cremoris and Lactococcus ssp. lactis var. lactis) isolated from the Tunisian lben were grown at constant pH on CSL medium in stirred fermentors for lactic starters production. The agitation required to homogenate alkali used to pH control should be low because it affects the Lactococcus growth. Scale up from 20-liter fermentor to 400-liter fermentor was carried out at constant impeller tip speed below 150 cm s^у. The CSL supplementation and fed-batch with glucose increased the yield in the upper 10¹⁰ cfu/ml. The consumed glucose during fermentation was converted into lactic acid and cell. Before fed-batch, the maximum specific growth rate of Lactococcus ssp. lactis var. diacetylactis was around 1 h^у and the number of cells increased 20 to 40 times according to inoculum size. After fed-batch, the glucose consumption rate remains constant but specific growth rate decreased and number of cell trebled only.     

Continuous production of lignin peroxidase by immobilized Phanerochaete chrysosporium in a pilot scale bioreactor

Lignin peroxidase was continuously produced by nylon-web or polyurethane immobilized Phanerochaete chrysosporium ATCC 24725 in a modified Biostate E® bioreactor, agitated either with the air and oxygen flow alone or in combination with a mechanical stirrer. Lignin peroxidase production started rapidly, and activities as high as ∼600 U l⁻¹ were reached as early as in 3 days. At best a total activity yield of ∼10 000 U was obtained during one week's continuous production with the maximum activity of ∼750 U l⁻¹ with nylon-web immobilized fungus, veratryl alcohol as an activator, and 2,2-dimethylsuccinate as buffer, although the relatively inexpensive benzyl alcohol and sodium tartrate peformed satisfactorily as the activator and buffer, respectively.     

Joint aerobic biodegradation of wastewater from table olive manufacturing industries and urban wastewater

Wastewater generated in the elaboration of table olives has been treated using activated sludge from a municipal wastewater plant after adequate acclimation. To avoid bactericide properties of some chemical structures present in this type of effluents, synthetic urban wastewater has been used to dilute the original wastewater. The main parameters affecting efficiency of biological processes have been studied. Thus, initial biomass concentration, temperature up to 303 K (upper working temperature limit = 313 K) and initial substrate concentration exerted a positive influence on COD degradation rate. The optimum pH was found to be around 7, experiencing a slight inhibition on cell activity at pH 4. Under the experimental conditions investigated other parameters like polyphenol content, absorbance at 254 nm and total organic carbon were also reduced to some extent. Only nitrates amount was increased after the biological process took place. A kinetic model based on Monod equation was proposed and applied to experimental results. The maximum specific growth rate was calculated by means of the aforementioned kinetic model. The value of this parameter as a function of temperature was fitted to an Arrhenius expression, w_max = 9.43 2 10¹⁰ exp(72021/RT) h^у (R in J mol^у K^у283 K < T < 303 K, pH , 7-10).     

Comparative study of the fermentation of D-glucose/D-xylose mixtures with Pachysolen tannophilus and Candida shehatae

We have performed a comparative analysis of the fermentation of the solutions of the mixtures of D-glucose and D-xylose with the yeasts Pachysolen tannophilus (ATCC 32691) and Candida shehatae (ATCC 34887), with the aim of producing bioethanol. All the experiments were performed in a batch bioreactor, with a constant aeration level, temperature of 30v°C, and a culture medium with an initial pH of 4.5. For both yeasts, the comparison was established on the basis of the following parameters: maximum specific growth rate, biomass productivity, specific rate of substrate consumption (q_s) and of ethanol production (q_E), and overall ethanol and xylitol yields. For the calculation of the specific rates of substrate consumption and ethanol production, differential and integral methods were applied to the kinetic data. From the experimental results, it is deduced that both Candida and Pachysolen sequentially consume the two substrates, first D-glucose and then D-xylose. In both yeasts, the specific substrate-consumption rate diminished over each culture. The values q_s and q_E proved higher in Candida, although the higher ethanol yield was of the same order for both yeasts, close to 0.4 kg kg^у.     

Clearance rates in the Arctic bivalves <Emphasis Type="Italic">Hiatella arctica</Emphasis> and <Emphasis Type="Italic">Mya </Emphasis>sp.

Filtration was studied in two Arctic clams, Hiatella arctica and Mya sp., collected in Young Sound, Northeast Greenland. Clearance rates were determined as a function of ambient temperature and algal cell concentration, using the clearance method and feeding with a unicellular flagellate. For both species, clearance rates increased with increasing temperature from <у up to 4-8°C. At higher temperatures, filtration ceased and the clams closed their valves. Clearance rates were also determined in temperate specimens of H. arctica collected on the west coast of Sweden. For these specimens, clearance rates increased with increasing temperature from 0 to 18-20°C. When weight-specific clearance rates were compared between the two populations and between species, there were no differences at 1°C. Clearance rates in Arctic H. arctica were maximal at algal cell concentrations corresponding to 2.5-8 µg chlorophyll a l^-1. Temperature compensation in Arctic bivalves is discussed and it is concluded that adaptations to constant low temperatures consist of a lower minimum temperature, for active filtration. Low clearance rates due to low temperatures did not seem to limit growth, under the prevailing conditions in Young Sound.     

Production of inulo-oligosaccharides from inulin by recombinant E. coli containing endoinulinase activity

To utilize intracellular endoinulinase for inulo-oligosaccharide (IOS) production from inulin, the endoinulinase gene (inu1) of Pseudomonas sp. was successfully cloned into the plasmid pBR322 by using EcoRI restriction endoinulinase and E. coli HB101 as a host strain. The endoinulinase from E. coli HB101/pKMG50 was constitutively expressed, showing similar reaction modes as compared to those of the original strain. However, some critical differences existed in optimal reaction conditions and oligosaccharide compositions between the two products catalyzed by the native enzyme of original strain and those by intact cells from recombinant cells. The IOS compositions produced by recombinant E. coli were quite different due to the diffusional restriction of the substrate and products within the cell wall. Optimal reaction conditions for batchwise production of IOS were as follow : optimum temperature, 55v°C; pH, 7.5; substrate concentration, 100 g/l inulin; enzyme dosage, 20 units/g substrate. Continuous production of IOS from inulin was also carried out at 50v°C using a bioreactor packed with the recombinant cells immobilized on calcium alginate gel. The optimal feed concentration and the feed flow rate were 100 g/l inulin and 0.6 h^у as a superficial space velocity, respectively. Under the optimum operation conditions, continuous production of IOS was successfully performed with productivity of 166.7 g/l·h for 15 days at 50v°C without significant loss of initial activity.     

Effect of continuous feeding of galactose on the production of recombinant glucose oxidase using Saccharomyces cerevisiae

A recombinant strain of Saccharomyces cerevisiae harboring GOD gene originated from Aspergillus niger was used for the production of extracellular glucose oxidase. The effect of continuous galactose feeding on the induction of GAL-10 promoter was examined in a 5 l bioreactor. The highest enzyme production level (164 U cm^х) was achieved at 96 h of cultivation. The production performance was compared with the results of fed-batch cultivations carried out in the same laboratory. Continuous feeding mode was found to be less productive due to excess ethanol formation and plasmid instability.     

Activity and batch operational stability of Candida rugosa lipase immobilized in different hydrophilic polyurethane foams during hydrolysis in a biphasic medium

The aim of this study was to investigate eventual relationships between some physico-chemical properties (e.g. porosity, aquaphilicity, partition coefficient for oleic acid and drying curves) of relatively hydrophilic polyurethane foams and the activity and batch operational stabiliy of Candida rugosa lipase immobilized within these foams. Two biocompatible polyurethane pre-polymers ("HYPOL FHP 2002^TM" and "Hypol FHP X4300^TM" from Hampshire Chemical GmbH, Germany) were tested as immobilization supports. The model reaction was the hydrolysis of crude olive residue oil in a biphasic aqueous/n-hexane medium. Drying curves under normal and reduced pressures suggested that water molecules are more strongly bound to the "FHP 2002" than to "FHP X4300" foams. This is in agreement with the higher aquaphilicity value estimated for the "FHP 2002" foam (3.7 vs 2.8). For every enzyme loading tested, hydrolysis efficiency was considerably higher for the lipase in "FHP X4300" foam when compared to the other counterpart. However, internal mass transfer limitations seem to be more severe with "FHP X4300" foams. Operational stability was evaluated in 10 consecutive batches (1 batch = 23 hours) for both immobilized preparations. A fast deactivation was observed for both biocatalysts. However, a slightly higher operational stability was observed for the lipase in "FHP 2002" foam. For the lipase in "FHP X4300" foam, the activity decay can be explained by a dramatic lipase leakage from the foam observed along successive batches. For the lipase in "FHP 2002" foam, no significant enzyme loss was observed along the reutilizations probably due to a higher number of multi-point attachment between the lipase and its support. In fact, activity and operational stability of Candida rugosa lipase in "FHP 2002" and "FHP X4300" foams appear to be related with the strength and/or the number of covalent binding between the enzyme and the support rather than to the physico-chemical properties evaluated in this work.