Effects of air pressure oscillation amplitude on oxygen transfer rate and biomass productivity in a solid-state fermenter

The modified sulfite oxidation method was adapted for estimation of the overall oxygen transfer rate in a pressure oscillating, solid-state fermenter. At 4.5 atm and 30 °C, the oxygen transfer rate reached 717 mmol kg^–1 initial dry matter h^–1 in this system against 37 mmol kg^–1 initial dry matter h^–1 in a static tray fermenter. At 30 °C and 3 atm, Azotobacter vinelandii grew on wheat straw and reached 4.7×10¹⁰ c.f.u. g^–1 substrate dry matter after 36 h, while only 8.2×10⁹ c.f.u. g^–1 substrate dry matter was obtained in a static tray system.     

Hydrogen accumulation by H2-uptake negative strains of Rhizobium

Summary Hydrogen evolution from root nodules has been reported to decrease the efficiency of the nitrogen fixing system. Mutants ofRhizobium meliloti andRhizobium leguminosarum were selected which were deficient in H₂-uptake capacity (Hup^–). The relative efficiency of the nitrogen fixation for both species assessed with C₂H₂ reduction was 0.66.The hydrogen production was monitored using a simple root incubation method. As such, hydrogen production up to 3.83 and 15.57 ml.day^–1.g^–1 plant dry weight were recorded forPisum sativum — Rhizobium leguminosarum 4.20 Hup^– andMedicago sativa — Rhizobium meliloti 1.5 Hup^– respectively. In a closed container (250 ml), hydrogen concentrations up to 20% (v/v) could be reached in the root phase ofMedicago sativa in a time period of 320 hours.     

Chitinase production by Beauveria felinaRD 101: optimization of parameters under solid substrate fermentation conditions

Major parameters affecting the production of chitinase by Beauveria felinaRD 101 under solid substrate fermentation conditions have been optimized. Wheat bran moistened with 100 MS-HCl medium adjusted to pH 5.0, inoculated with 1 × 10¹⁰ conidia g^–1 initial dry bran and incubated at 28 °C for 6 days produced maximum chitinase activity of 6.34 U g^–1 initial dry substrate.     

Ethanol tolerance in free and sol-gel immobilised Saccharomyces cerevisiae

The tolerance of sol-gel immobilised and free Saccharomyces cerevisiae to ethanol was studied. The effects of ethanol preincubation time showed that the specific death velocity decreased from 2×10⁵ c.f.u. min^–1 for free cells to 2×10⁴ c.f.u. min^–1 for immobilised cells thus indicating that immobilised yeast was far less sensitive to the ethanol damage. The specific glucose consumption of immobilised and free cells on a per cell basis was 3×10^–12 g cell^–1 h^–1 and 9×10^–12 g cell^–1 h^–1, respectively.     

A simple method for mass isolation of protoplasts from species of Monostroma, Enteromorpha and Ulva (Chlorophyta, Ulvales)

A simple enzyme mixture containing 2% Cellulase Onozuka R–10 and1% Macerozyme R–10 prepared in deionised water supplemented with 3% NaCland 1 mM CaCl₂ was developed for isolating rapidlyprotoplasts from different species of Monostroma,Enteromorpha and Ulva. The yield fordifferent species of Monostroma ranged from 9.6 ×10⁶ to 10.2 × 10⁶ cells g^–1f. wt thallus, and forEnteromorpha from 3.48 × 10⁶ to 11.7× 10⁶ cells g^–1 f. wt and forUlva from 4.58 × 10⁶ to 26.8 ×10⁶ cells g^–1 f. wt. The overallregeneration rate of the protoplasts isolated was usually > 90% and showednormal morphogenesis. The method yields rapid mass production of viableprotoplasts with high regeneration rates.     

Interspezifische Transformationen zwischen Agrobacterium tumefaciens und Rhizobium leguminosarum

Zusammenfassung Als weiterer Beweis für die Transformierbarkeit von Agrobacterium tumefaciens und Rhizobium leguminosarum werden wechselseitige Transformationsversuche durchgeführt und dabei die Resistenz gegen Streptomycin bzw. gegen ein Sulfonamid (Marbadal) als Selektionsmaterial benutzt. Die ermittelten Transformationsraten liegen in der Größenordnung von 4–7 · 10^-6 bzw. 13 bis 16 · 10^-6.

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Interspecific transformations of Agrobacterium tumefaciens and Rhizobium leguminosarum

Summary As further proof for the transformability of Agrobacterium tumefaciens and Rhizobium leguminosarum reciprocal transformation assays were performed using the resistence against streptomycin resp. against a sulfonamide (Marbadal) as selection marker. The transformations rates are 4–7×10^-6 resp. 13–16×10^-6.

     

A solid-state bioreactor coupled with forced aeration and pressure oscillation

A novel design of a solid-state bioreactor, operated with periodic pressure oscillation coupled with forced aeration through the medium, gave efficient control of temperature. The evaluation of the bioreactor assembly with respect to temperature and cellulase production by Penicillium decumbens JUA10 showed that, at 4 atm and the bed depth of 6 cm, the maximal temperature variation in the reactor was +1.5 °C at a set value of 30 °C compared with +6.8 °C in a static tray system. The highest cellulase and -glucosidase activities were 15 IU g^–1 and 51 IU g^–1 substrate dry matter at 96 h, respectively, while only 10 IU g^–1 and 24 IU g^–1 were obtained in the static tray culture system.     

Studies on the respiration of efficient and inefficient strains of Rhizobium

Summary In a pot culture experiment using sterilised soil, growth and nitrogen content of Berseem (Trifolium alexandrinum) inoculated with 15 strains of Rhizobium trifolii and of pea (Pisum sativum) inoculated with 10 strains of Rhizobium leguminosarum were found to vary considerably depending on the strains of the respective Rhizobium used. Out of the 15 strains of Rhizobium trifolii, 6 strains were found to be highly efficient (increasing the nitrogen content by more than 70 per cent over the control-uninoculated) and the rest as either moderately efficient (increase in N by 30–50 per cent) or inefficient (increase in N by 4 to 20 per cent) strains. Similarly, out of the 10 strains of Rhizobium leguminosarum 5 strains were found to be highly efficient, 1 moderately efficient and the rest were more or less inefficient strains.The respiration rate (l O₂ consumed per hour per mg dry cells) of efficient and inefficient strains of Rhizobium trifolii and Rhizobium leguminosarum in glucose, maltose and mannitol substrate did not bear any relation to their efficiency. However, the stimulation of the respiratory rate of the Rhizobium strains due to the addition of glycine to the glucose substrate was found to be significantly more in case of efficient strains of Rhizobium trifolii and Rhizobium leguminosarum than those of the inefficient ones.The data presented in the paper is taken from the thesis submitted by the Senior author, to the P. G. School, IARI, N. Delhi, in 1968, for Ph. D. degree.     

Production,formulation and antagonistic activity of the biocontrol like-yeast <Emphasis Type="Italic">Aureobasidium pullulans</Emphasis> against <Emphasis Type="Italic">Penicillium expansum</Emphasis>

Aureobasidium pullulans (de Bary) Arnaud (Ach 1-1) was grown in a glucose fed-batch fermentor to 106 g dry wt l⁻¹ in 48 h. The cells were dried in a fluidized bed dryer with a final viability of 62%. After 7 months at 4°C, the viability was 28% of the initial value (= 2.3 × 10¹⁰ c.f.u. g⁻¹ dry matter). A protection level of 89% was achieved with the biomass preparation at 1 × 10⁸ c.f.u. ml⁻¹ after 28 and 7 days for apples stored respectively at 5 and 25°C against Penicillium expansum. Our process is suitable to produce large quantities of the strain Ach 1-1 as biological control agent for apple preservation.     

Effects of water extracts of a composted manure-straw mixture on the plant pathogen Botrytis cinerea

Manure-straw mixtures were composted and water extracts, made by incubating compost in water for 3 to 18 days, were assessed for antagonistic activity against Botrytis cinerea, using a range of tests. Extracts of all ages inhibited conidial germination on glass slides and reduced mycelial growth on agar. Mixing extracts of all ages with droplets of suspensions of B. cinerea conidia on detached Phaseolus bean leaves suppressed lesion development, but only 3- to 8-day-old extracts had an effect when sprayed onto leaves 2 days before inoculation. Extracts contained a large and varied microbial population of actinomycetes (0.3 to 2.4×10⁵ c.f.u.ml^–1), bacteria (1.5 to 5.6×10¹⁰ c.f.u.ml^–1), filamentous fungi (25.0 to 45.5 c.f.u. ml^–1) and yeasts (26.1 to 62.6 c.f.u.ml^–1). Eight- and 18-day-old extracts lost activity completely on filter sterilization or autoclaving. Weekly sprays of 8-day-old extracts onto lettuce in the glasshouse had no effect on the incidence of grey mould, but significantly reduced its severity and increased marketable yield. The use of compost extracts in biocontrol of plant diseases and their possible mode of action is discussed.M.P. McQuilken and J.M. Whipps are and J.M. Lynch was with the Microbiology and Crop Protection Department, Horticulture Research International, Littlehampton BN17 6LP, UK; J.M. Lynch is now with the School of Biological Sciences, University of Surrey, Guildford GU2 5XH, UK.     

Degradation of 2-methylnaphthalene by free and immobilized cells of Pseudomonas sp. strain NGK1

A Pseudomonas sp. strain NGK1 (NCIM 5120) capable of utilizing 2-methylnaphthalene (2-MN) was immobilized in various matrices namely, polyurethane foam (PUF), alginate, agar and polyvinyl alcohol (PVA) (1.5 × 10¹² c.f.u. g^–1 beads). The degradation rates of 25 and 50 mM 2-MN by freely suspended cells (2 × 10¹¹ c.f.u. ml^–1) and immobilized cells in batches, semi-continuous with shaken culture and continuous degradation in a packed-bed reactor were compared. The PUF-immobilized cells achieved higher degradation of 25 and 50 mM of 2-MN than freely suspended cells and the cells immobilized in alginate, agar or PVA. The PVA- and PUF-immobilized cells could be reused for more than 30 and 20 cycles respectively, without losing any degradation capacity. The effect of dilution rates on the rate of degradation of 25 and 50 mM 2-MN with freely suspended and immobilized cells were compared in the continuous system. Increase in dilution rate increased the degradation rate only up to 1 h^–1 in free cells with 25 mM 2-MN and no significant increase was observed with 50 mM 2-MN. With immobilized cells, the degradation rate increased with increase in dilution rate up to 1.5 h^–1 for 25 mM and 1 h^–1 for 50 mM 2-MN. These results revealed that the immobilized cell systems are more efficient than freely suspended cells for biodegradation of 2-MN.     

Factors which influence the sedimentation characteristics of Torulopsis glabrata after growth in a recirculation system

Summary Some environmental affects on cell aggregation described in the literature are briefly summarized. By means of a biomass recirculation culture (Contact system), using the yeast Torulopsis glabrata, the aggregation behavior of cells in static and in dynamic test systems is described. Sedimentation times required to obtain 50 g · l^–1 yeast dry matter in static systems were always higher than in dynamic ones.In addition to, influencing the biomass yield, the specific growth rate of the yeast also affected cell aggregation. The specific growth rate and therefore the aggregation could be regulated by the biomass recirculation rate as well as by the sedimenter volume.Abbreviations f_o Overflow flow rate (l·h^–1) - f_R Recycle flow rate (l·h^–1) - f_t0t Total flow rate through the fermenter (l·h^–1) - g Gram - h Hour - D_R Fermenter dilution rate due to recycle (h^–1) - D_S Fermeter dilution rate due to substrate (h^–1) - D_tot Total fermenter dilution rate (h^–1) - l Liter - Specific growth rate (h^–1) - P_F Fermenter productivity (g·l^–1·h^–1) - P_FS Overall productivity (g·l^–1·h^–1) - R_pM Rates per minute - RS Residual sugar content in the effluent with respect to the substrate concentration (%) - Y Yield of biomass with respect to sugar concentration (%) - Sed 50 Sedimentation time to reach a YDM of 50 g·l^–1 (min) - V Volume (l) - V_F Fermenter volume (l) - V_Sed Sedimenter volume (l) - VVM Volumes per volume and minute - X_F YDM in the fermenter (g·l^–1) - X_F YDM in the recycle (g·l^–1) - X_S Yeast dry matter due to substrate concentration (g·l^–1) - YDM Yeast dry matter (g·l^–1)     

Specific detection of an oil-degrading bacterium, Corynebacterium sp. IC10, in sand microcosms by PCR using species-specific primers based on 16S rRNA gene sequences

A species-specific PCR technique to detect an oil-degrading bacterium, Corynebacterium sp. IC10, released into sand microcosms is described. PCR primers, specific to strain IC10, were designed based on 16S rRNA gene sequences and tested against both closely and distantly related bacterial strains using four primer combinations involving two forward and two reverse primers. Two sets of them were specific to the strain IC10 and Corynebacterium variabilis and one set was selected for further analysis. The PCR amplification was able to detect 1 pg template DNA of strain IC10 and 1.2×10⁴ c.f.u. of IC10 ml wet sand^–1 in the presence of 3×10⁸ Escherichia coli cells. In non-sterile sand microcosms seeded with the strain IC10, the sensitivity of detection decreased to 9.6×10⁵ c.f.u. ml wet sand^–1. The detection sensitivity thus depends on the complexity of background heterogeneous DNA of environmental samples. The assay is suitable for detection of Corynebacterium sp. IC10 in laboratory microcosms, however, cross reaction with non-oil degrading coryneforms may prohibit its use in uncharacterized systems.     

Influence of growth conditions on production of capsular and extracellular polysaccharides byRhizobium leguminosarum

The influence of growth rate and medium composition on exopolymer production byRhizobium leguminosarum was studied. When grown in medium containing 10g/l mannitol and 1g/l glutamic acid,Rhizobium leguminosarum biovartrifolii TA-1 synthesized up to 2.0g/l of extracellular polysaccharide (EPS), and up to 1.6g/l of capsular polysaccharide (CPS). Under non-growing cell conditions in medium without glutamic acid, CPS synthesis by strain TA-1 could proceed to 2.1g/l, while EPS-production remained relatively low (0.8g/l). Maximal CPS-yield was 2.9g CPS/l medium in a medium containing 20g/l mannitol and 2g/l glutamic acid. TheEPS-deficient strain R. leguminosarum RBL5515,exo4::Tn5 was able to produce CPS to similar levels as strain TA-1, but CPS-recovery was easier because of the low viscosity of the medium and growth of the cells in pellets. With strain TA-1 in nitrogen-limited continuous cultures with a constant biomass of 500mg cell protein/l, EPS was the most abundant polysaccharide present at every dilution rate D (between 0.12 and 0.02 h^–1). The production rates were 50–100mg/g protein/h for EPS and 15–20mg/g protein/h for CPS. Only low amounts of cyclic -(1,2)-glucans were excreted (10–30 mg/l) over the entire range of growth rates.Abbreviations bv biovar - CPS capsular polysaccharide - EPS extracellular polysaccharide - HM_r high molecular mass - LM_r low molecular mass - YEMCR Yeast Extract-Mannitol-Congo Red agar     

Nitrous oxide production by nitrogen-fixing,fast-growing Rhizobia

Rhizobium trifolii, R. leguminosarum, andR. hedysarum, grownex planta under anoxic conditions in a chemically defined medium, evolve N₂O from NO₃ ^–, NO₂ ^–, and (NH₄)₂NO₃. The amount of nitrous oxide formed after 96 hours is about 0.2M×mg^–1 cells d.w. Large availability of organic matter enhances the production of N₂O from nitrate by free-livingR. trifolii in peat/sand mixtures. Denitrification of the above species andR. meliloti was detected also in planta. Nitrous oxide production increases almost linearly from 10–45M×mg^–1 nodules d.w. when nitrogen-fixing plants are exposed to increasing concentrations of nitrate (1–12M).     

Respiratory stimulus in Rhizobium sp. by legume lectins

High molecular weight lectins (> 100 kDa) from seeds of the legumes Canavalia brasiliensis (CnBr), Cratylia floribunda (CFL), Phaseolus vulgaris (PHA) and Vatairea macrocarpa (VML), temporarily stimulate the respiration of Rhizobium tropici-CIAT899 and R. etli-CFN42. These stimulants were significant (P < 0.05) in bacterial suspensions (> 2.85 mg dry biomass ml^–1), having at least 6200 molecules of lectins per bacteria. The VML (20 g ml^–1), induced specific O₂ demand of 2.3–2.5 M O₂ min^–1 mg dry biomass^–1, in CFN42 and CIAT899, respectively. However, CnBr, CFL and PHA induced smaller demands of O₂ (5×), in both strains. The order of affinities of the lectins was approximately VML > PHA > CFL > CnBr, with regard to respiratory stimuli in CIAT899 strain. The co-administration of 10 g VML ml^–1 and 9.8 M galactose, in CIAT899 suspensions, reduced the respiratory stimuli significantly in relation to the treatment with VML alone. These respiratory stimuli, induced by the lectins, increase the significance of the interaction lectin × Rhizobium in terms of bacterial physiology. Its understanding could be important in relation to bacterial symbiotic behaviour.     

Ethylene metabolism in Pisum sativum L.: Kinetic parameters,the effects of propylene,silver and carbon dioxide and comparison with other systems

The kinetic parameters of in vivo ethylene metabolism by seedlings of Pisum sativum L. cv. Alaska have been determined. The oxidation of ethylene to CO₂, (Ox) and the incorporation of ethylene into the tissue (TI) were both shown to display Michaelis-Menten kinetics (K_m Ox = 0.9 × 10^–6 M liquid phase, V_max Ox = 2.4 × 10^–10 moles g^– dry mass h^–1 K_m TI = 1.6 × 10^–6 M liquid phase, V_max TI = 4.5 × 10^–10 moles g^–1 dry mass h^–1). Propylene competitively inhibited both Ox (K_i = 7.0 × 10^–6 M) and TI (K_i = 3.7 × 10^–7 M). A system comparable to Ox was absent from imbibed cotyledons of Vicia faba L. cv. Aquadulce even at saturating concentrations of ethylene similar to those used in kinetic analysis on Pisum. Silver ions were shown to inhibit TI but promoted Ox, while carbon dioxide inhibited Ox but promoted TI. Kinetic data on both these effects are presented. Data on the effect of a range of concentrations of CO₂ on TI and Ox are also presented.To whom editorial correspondence should be sent     

Fed-batch production of baker's yeast using millet (Pennisetum typhoides) flour hydrolysate as the carbon source

A fermentation medium based on millet (Pennisetum typhoides) flour hydrolysate and a four-phase feeding strategy for fed-batch production of baker's yeast,Saccharomyces cerevisiae, are presented. Millet flour was prepared by dry-milling and sieving of whole grain. A 25% (w/v) flour mash was liquefied with a thermostable 1,4--d-glucanohydrolase (EC 3.2.1.1) in the presence of 100 ppm Ca²⁺, at 80°C, pH 6.1–6.3, for 1 h. The liquefied mash was saccharified with 1,4--d-glucan glucohydrolase (EC 3.2.1.3) at 55°C, pH 5.5, for 2 h. An average of 75% of the flour was hydrolysed and about 82% of the hydrolysate was glucose. The feeding profile, which was based on a model with desired specific growth rate range of 0.18–0.23 h^–1, biomass yield coefficient of 0.5 g g^–1 and feed substrate concentration of 200 g L^–1, was implemented manually using the millet flour hydrolysate in test experiments and glucose feed in control experiments. The fermentation off-gas was analyzed on-line by mass spectrometry for the calculation of carbon dioxide production rate, oxygen up-take rate and the respiratory quotient. Off-line determination of biomass, ethanol and glucose were done, respectively, by dry weight, gas chromatography and spectrophotometry. Cell mass concentrations of 49.9–51.9 g L^–1 were achieved in all experiments within 27 h of which the last 15 h were in the fedbatch mode. The average biomass yields for the millet flour and glucose media were 0.48 and 0.49 g g^–1, respectively. No significant differences were observed between the dough-leavening activities of the products of the test and the control media and a commercial preparation of instant active dry yeast. Millet flour hydrolysate was established to be a satisfactory low cost replacement for glucose in the production of baking quality yeast.Nomenclature C _ox Dissolved oxygen concentration (mg L^–1) - CPR Carbon dioxide production rate (mmol h^–1) - C _s0 Glucose concentration in the feed (g L^–1) - C _s Substrate concentration in the fermenter (g L^–1) - C _s.crit Critical substrate concentration (g L^–1) - E Ethanol concentration (g L^–1) - F _s Substrate flow rate (g h^–1) - i Sample number (–) - K _e Constant in Equation 6 (g L^–1) - K _o Constant in Equation 7 (mg L^–1) - K _s Constant in Equation 5 (g L^–1) - m Specific maintenance term (h^–1) - OUR Oxygen up-take rate (mmol h^–1) - q _ox Specific oxygen up-take rate (h^–1) - q _ox.max Maximum specific oxygen up-take rate (h^–1) - q _p Specific product formation rate (h^–1) - q _s Specific substrate up-take rate (g g^–1 h^–1) - q _s.max Maximum specific substrate up-take rate (g g^–1 h^–1) - RQ Respiratory quotient (–) - S Total substrate in the fermenter at timet (g) - S ₀ Substrate mass fraction in the feed (g g^–1) - t Fermentation time (h) - V Instantaneous volume of the broth in the fermenter (L) - V ₀ Starting volume in the fermenter (L) - V _si Volume of samplei (L) - x Biomass concentration in the fermenter (g L^–1) - X ₀ Total amount of initial biomass (g) - X _t Total amount of biomass at timet (g) - Y _p/s Product yield coefficient on substrate (–) - Y _x/e Biomass yield coefficient on ethanol (–) - Y _x/s Biomass yield coefficient on substrate (–) Greek letters Moles of carbon per mole of yeast (–) - Moles of hydrogen atom per mole of yeast (–) - Moles of oxygen atom per mole of yeast (–) - Moles of nitrogen atom per mole of yeast (–) - Specific growth rate (h^–1) - _crit Critical specific growth rate (h^–1) - _E Specific ethanol up-take rate (h^–1) - _max.E Maximum specific ethanol up-take rate (h^–1)     

Production of poly(3-hydroxybutyrate) from whey by fed-batch culture of recombinant Escherichia coli in a pilot-scale fermenter

Production of poly(3-hydroxybutyrate) [P(3HB)] from wheyby fed-batch culture of recombinant Escherichia coli CGSC 4401 harboring a plasmid containing the Alcaligenes latus polyhydroxyalkanoate (PHA) biosynthesis genes was examined in a 30 l fermenter supplying air only. With lactose below 2 g l^–1, cells grew to 12 g dry cell l^–1 with 9% (w/w) P(3HB) content. Accumulation of P(3HB) could be triggered by increasing lactose to 20 g l^–1. By employing this strategy, 51 g dry cell l^–1 was obtained with a 70% (w/w) P(3HB) content after 26 h. The productivity was 1.35 g P(3HB) l^–1 h^–1. The same fermentation strategy was used in a 300 l fermenter, and 30 g dry cell l^–1 with 67% (w/w) P(3HB) content was obtained in 20 h.     

Competitive nodulation blocking of Afghanistan pea is determined by nodDABC and nodFE alleles in Rhizobium leguminosarum

Summary One well-defined competitive interaction amongst rhizobia is that between compatible and non-compatible strains of Rhizobium leguminosarum with respect to the nodulation of some primitive pea genotypes. The Middle Eastern pea cv Afghanistan is nodulated effectively can R. leguminosarum TOM, but its capacity to nodulate can be blocked if a mixed inoculation is made with R. leguminosarum PF₂. This PF₂ phenotype (Cnb) is encoded by its symbiotic plasmid and cosmid clones thereof. We found that Cnb is also encoded by the well-characterized Sym plasmid pRL1JI of R. leguminosarum strain 248. We have isolated and characterized a 6.9 kb HindIII fragment of pSymPF₂ which confers the Cnb⁺ phentoype on other (Cnb^–) rhizobia. A Tn5 site-directed Cnb^– mutant was constructed by homogenotization and was also found to be Nod^– on the European pea cv Rondo. DNA hybridization and complementation analysis indicated that the 6.9 kb Cnb⁺ fragment contained the nodD, nodABC and nodFE operons. Analysis of the Cnb phenotype of nod::Tn5 alleles of pRL1JI showed that mutations of nodC, nodD or nodE all abolished Cnb activity whereas mutants in nodI and nodJ reduced activity to 50% of the wild-type level.