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

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

Intensive rotifer cultures using chemostats

Continuous production of the rotifer Brachionus plicatilis rotundiformis (S-type) in an intensive chemostat culture system has been investigated. The production dynamics of rotifers in relation to different flow rates and feed regimes show that the growth rate and production depends on the type of algal feed and flow rate utilized in the culture system. It was possible to achieve a mean production of up to 318.84 × 10⁶ rotifers m^–3 d^–1 at a flow rate of 6 1 h^–1 in 100 1 chemostats and up to 261.21 × 10⁶ rotifers m^–3 d^–1 at a flow rate of 40 1 h –1 while using 1 m³ capacity rotifer chemostats as production units. The 3 fatty acid composition of rotifers while using Chlorella and Nannochloropsis in the culture system has been described. The results of this investigation show that the rotifer productivity in the continuous culture system is considerably higher than in any of the conventional culture systems described to date for aquacultural purposes.This research was financed by the Kuwait Foundation for the Advancement of Sciences (KFAS), Kuwait, under a contract research project code 86-04-02.     

Lysis by interleukin 2-stimulated tumor-infiltrating lymphocytes of autologous and allogeneic tumor target cells

Summary Stepwise counterflow centrifugal elutriation of leukapheresed human mononuclear cells (MNC) in a Beckman JE-6B rotor and J6-M/E centrifuge yielded a population highly enriched in natural killer (NK) cells (70–75% large granular lymphocytes with 10–13 times greater NK activity) at a flow rate of 38–44 ml/min using a fixed rotor speed of 3000 rpm at 27° C. However, the mean cell recovery was <1%. To obtain sufficient numbers of purified NK cells for adoptive immunotherapy, a strategy combining counterflow centrifugal elutriation with adherence of recombinant interleukin-2(rIL-2)-activated NK cells to plastic was developed. First, MNC were elutriated to give a twofold enrichment in NK cells, containing 22% Leu19⁺ cells, 18% large granular lymphocytes and 51 lytic units of activity against K562 targets as opposed to the unfractionated MNC containing 10% Leu19⁺ cells, 7% large granular lymphocytes and 26 lytic units of activity. The mean recovery was 80±15% (n=10). Further enrichment was obtained by isolation of the elutriated cells that adhered to plastic after culture for 24 h in the presence of 1000 U/ml rIL-2. The initial adherent lymphokine-activated killer (A-LAK) cells represented 1–4% of total MNC, but their subsequent expansion was at least 10–22-fold during 8–14 days in culture with 1000 U/ml rIL-2. Using this strategy, 2 × 10⁹ normal MNC, obtained by leukapheresis, yielded 5 × 10⁸ A-LAK cells with a total of 5.7 × 10⁵ lytic units of cytotoxicity against K562 and a total of 3.3 × 10⁵ lytic units against Daudi targets. This enrichment method has yielded sufficient numbers of A-LAK cells to form the basis for a phase I clinical trial of adoptive immunotherapy in patients with advanced cancer.     

Analysis of the methane production in thermophilic anaerobic reactors: use of autofluorescence microscopy

Methanogenic activity in thermophilic, anaerobic reactors was determined by comparing the amount of methane generated in single- and two-stage systems with the size of the methanogenic population, as determined by microscopy. The methanogenic activities were 2.71 × 10^–9 ml methane cell^–1 d^–1 and 1.10 × 10^–9 ml methane cell^–1 d^–1 for 10 and 4 days of the hydraulic retention time (HRT), in the single-stage system. In the two-stage system, 7.49 × 10^–9 ml methane cell^–1 d^–1 in the acidogenic reactor and 1.56 × 10^–9 ml methane cell^–1 d^–1 in the methanogenic reactor for 4 days of the HRT. A high correlation was evident between the methane production and methanogenic population [0.1354 ln(x) – 2.1375](R ² 0.8619).     

Batch and continuous ribonuclease production by immobilized Aspergillus clavatus cells in a bubble-collumn bioreactor

Summary Ribonuclease production using immobilized cells (IC) of Aspergillus clavatus has been studied under batch, repeated-batch and continuous fermentation conditions in a bubble-column bioreactor and compared with production by free cells, Immobilization was achieved by the method of cryostructurization in polyvinyl alcohol beads. The effect of various aeration rates in a column bioreactor has been investigated. Enzyme production by IC [42 000 units (U)·l^–1] during batch fermentations was comparable to that of a free-cell system. The specific productivity of IC was 8.5 times higher than that of free cells. In repeated batch fermentation at various aeration rates, successful reuse of IC was obtained, with comparable levels of enzyme production. Continuous ribonuclease production was achieved for 44 days at 1 vvm aeration and a dilution rate of 0.0 h^–1 with volumetric productivity (450 U·1^–1) and yield.     

Influence of tetracycline on the submerge Pleurotus saca cultivation

Summary The influence of various tetracycline hydrochlorides (TC HC concentrations: 3,6,8 and 12 × 10^–3g 1^–1), on growth and protection against bacterial infections in submerged Pleurotus saca cultivation was studied. 8 × 10^–g 1^–1 of TC HC added before the inoculation showed a reasonable protection effect, simultaneously promoting the growth of fungus. In the presence of tetracycline the lag phase was prolonged, and the final biomass production increased by 200 % on average. If the infection occurred during the cultivation process, even 12–16 × 10^–3g 1^–1 of added TC HC, could not prevent bacterial infection.     

A preliminary carbon budget for a part of the Ems estuary: The Dollard

During 1975, measurements were made to quantify all sources of input of organic matter in the Dollard. This made a comparison possible between in situ primary production, import from natural sources and organic waste discharges in terms of organic carbon. In order to make a carbon budget, mineralization and the amount of organic matter buried in the sediment was also measured. Input of organic carbon was mainly based on primary production on the tidal flats (measured in situ as O₂ production, 9.3×10⁶ kg C · year^–1), accumulation of suspended matter originating from the North Sea and the River Ems (maximal 37.1×10⁶ kg C · year^–1) and discharge of heavily polluted water (33.0×10⁶ kg C · year^–1). Input from primary production in the water phase was negligibly low (0.7×10⁶ kg C · year^–1). Loss of organic carbon was due to mineralization in the sediment (measured in situ as oxygen consumption, 18.2×10⁶ kg C · year^–1), mineralization in the water phase (using the BOD technique, 7.2×10⁶ kg C · year^–1) and burying of organic matter in the sediment (9.9·10⁶ kg C · year^–1). The loss of dissolved organic matter to the adjacent Waddensea was not measured but must be considerable. Allochthonous detritus was the main source of energy for the food-webs in the Dollard. The role of bacteria as an important source of food for higher organisms in the Dollard is discussed.     

Growth ofCatharanthus roseus cell suspensions in bioreactors: On-line analysis of oxygen and carbon dioxide levels in inlet and outlet gas streams

Summary Catharanthus roseus cells (C87N) grown in a 30 litre airlift vessel achieved a growth rate of 0.366 day^–1. The maximum biomass yield (9.13 gl^–1) was recorded after 168 hours (7 days). On-line analysis of the composition of inlet and outlet gas streams during the growth cycle allowed calculation of the metabolic activity of the cultures. Oxygen uptake on a dry weight basis reached a maximum of 4.5×10^–4 Moles O₂ g dry weight^–1 h^–1 after 96 hours (during the mid-logarithmic phase of growth) and a maximum of 2.7×10^–3 Moles O₂ l^–1 h^–1 on a volume basis (towards the end of the logarithmic phase). Carbon dioxide production ran in parallel with oxygen use with maxima at 4.2×10^–4 Moles CO₂ g dry weight^–1 h^–1 and 3.4×10^–3 Moles g l^–1 h^–1 respectively.     

Soy-based medium for ethanol production byEscherichia coli KO11

An optimized soy-based medium was developed for ethanol production byEscherichia coli KO11. The medium consists of mineral salts, vitamins, crude enzymatic hydrolysate of soy and fermentable sugar. Ethanol produced after 24 h was used as an endpoint in bioassays to optimize hydrolysate preparation. Although longer fermentation times were required with soy medium than with LB medium, similar final ethanol concentrations were achieved (44–45 g ethanol L^–1 from 100 g glucose L^–1). The cost of materials for soy medium (excluding sugar) was estimated to be $0.003 L^–1 broth, $0.006 L^–1 ethanol.     

Influence of temperature rise on kinetic parameters during batch propagation of Kluyveromyces fragilis in cheese whey under ambient conditions

Three 5 l working volume fermenters were used to investigate the growth of the yeast Kluyveromyces fragilis in acid cheese whey under ambient temperature in order to assess the specific growth rate and yield, the lactose and oxygen uptake rates during the various phases of batch culture, the effect of increasing temperature on the various kinetic parameters, and the need for a cooling unit for single cell production batch systems. The initial dissolved oxygen in the medium was 5.5 mg l^–1 and the pH was maintained at 4.5. The observed lag phase, specific growth rate and maximum cell number were 4 h, 0.2 h^–1 and 8.4 × 10⁸ cells ml^–1, respectively. About 99% of the lactose in cheese whey was utilized within 20 h, 85% during the exponential growth phase. The specific lactose utilization rates by K. fragilis were 0.20 × 10^–12, 1.457 × 10^–12, 0.286 × 10^–12 and 0.00 g lactose cell^–1 h^–1, for the lag, exponential, stationary and death phases, respectively. The dissolved oxygen concentration in the medium decreased as the cell number increased. The lowest oxygen concentration of 1.2 mg l^–1 was observed during the stationary phase. The volumetric oxygen transfer coefficient was 0.41 h^–1 and the specific oxygen uptake rates were 0.32 × 10^–12, 2.14 × 10^–12, 0.51 × 10^–12 and 0.003 × 10^–12 mg O₂ cell^–1 h^–1, for the lag, exponential, stationary and death phases, respectively. The maximum temperature recorded for the medium was 33 °C, indicating that a cooling unit for batch production of single cell protein at ambient temperature is not needed for this type of bioreactor. The increase in medium temperature affected the cell growth and the lactose and oxygen uptake rates.     

Viriobenthos Production and Virioplankton Sorptive Scavenging by Suspended Sediment Particles in Coastal and Pelagic Waters

Virus production in oxic surface sediments and virioplankton sorption to suspended particles was estimated across three stations in the Southern California region (33.4°N, 118.6°W). Viriobenthos production was estimated using a sterile sediment and filtered porewater dilution technique that targeted production from both attached bacteria and bacteria living free in the porewater, and attached bacteria alone. Potential virus production rates by bacteria free in the porewater ranged from 1.7 to 4.6 × 10⁸ VLP cm^–3 h^–1, while attached bacteria had slower potential production rates of between 0.4 and 1.1 × 10⁸ VLP cm^–3 h^–1, suggesting turnover rates of viruses in sediments (1–5 h) which are significantly higher than those of virioplankton (~24–48 h). Virioplankton adsorbed to small (<150 µm) suspended sediments at stations with high ambient suspended solid concentrations. Virioplankton scavenging rates combined with published sedimentation rates demonstrate that this mechanism of virus arrival could only account for 0.01% of daily benthic virus production. Calculated mortality rates of benthic bacteria (4–14% h^–1) suggest viruses may play an important role in sediment carbon cycling.     

Biomass,production and activity of bacteria in the Black Sea,with special reference to chemosynthesis and the sulfur cycle

Abundance, morphological composition, vertical distribution, production and activity of total bacterioplankton and its specific groups in the Black Sea were investigated in August–September 1989. The total bacterioplankton was highest in the upper mixed layer (0.7–1 × 10⁶ cells ml^–1), corresponding to that in mesotrophic basins. In the N-E shallow part of the sea it attained 3 × 10⁶. Below the thermocline (50–100 m) the total number of bacteria decreased to 0.2–0.4 × 10⁶ ml^–1. In the redox gradient zone (zone of O₂-H₂S interface), it increased again. In deep anoxic waters the bacterioplankton, numbering 0.15–0.2 × 10⁶ ml^–1, was functionally inactive. Its biomass was 12–40 mg C m^–3 in the upper mixed layer, 5–10 mg C m^–3 in the intermediate cold layer (40–100 m depth), and 10–20 mg C^–3 in the redox zone. Maximum production rates occurred in the upper mixed layer (8–20 mg C^–3 d^–1) and in the redox-zone, 80–90% of it was due to chemosynthesis of thiobacilli. Below 200 m, microbial production decreased to about zero in the anoxic zone. Maximum activity of heterotrophic bacteria was recorded in the upper mixed layer, while thiobacilli and methaneoxidezing bacteria were most active in the redox-zone. Here, the maximum rates of H₂S and of thiosulfate oxidation, as well as maximum sulfate reduction were recorded. Chemical oxidation of H₂S was dominant. These results are discussed with respect to the present ecological situation of the Black Sea.     

Effect of high concentration of nutrients onBacillus thuringiensis cultures

Summary Bacterial insecticide production using a strain ofBacillus thuringiensis var. kurstaki was studied in batch culture considering the influence of increasing concentration of components of a glucose — yeast extract — mineral salts medium.It was found that spore counts were increased from 1.08×10¹² spores. 1^–1 to 7.36×10¹² spores. 1^–1 and toxin level from 1.05 mg.ml^–1 to 6.85 mg.ml^–1, when the concentration of glucose was increased from 8 to 56 (g 1^–1), with the corresponding increase in the rest of medium components. Higher concentration of nutrients inhibit either spore count or toxin production.Preliminary experiments of fed-batch cultures which allows the use of high amounts of nutrients were also carried out. In this case spore counts of 1.2×10¹³ spores.1^–1 were achieved.     

Dynamics of bacterioplankton in a mesotrophic French reservoir (Pareloup)

Bacterioplankton abundance, biomass and production were studied at a central station (35 m depth) from April 1987 to September 1988 in a mesotrophic reservoir. Bacterial production was calculated by the (³H) thymidine method.For the water column, integrated estimates of bacterioplankton abundance ranged from 2.3 10⁹ to 4.6 10⁹ cells l^–1, and carbon biomass from 0.037 to 0.068 mg C l^–1; the thymidine incorporation rates ranged from 0.8 to 17.2 picomoles l^–1 h^–1, leading to net bacterial production estimates of less than 0.7 µg C l^–1 d^–1 in winter to 18 µg C l^–1 d^–1 in summer. About 55% of the production occurred in the euphotic layers.Over the year, the bacterial carbon requirement represented 90% of the autotrophic production for the whole lake. It was five times lower than autotrophic production in spring, but twice as high in summer. This important temporal lack of balance suggests that not all the spring primary production products are consumed immediately and/or that other carbon sources probably support bacterial growth in summer.     

Enhancement of production of cloned α-amylase by lactic acid feeding from recombinant Saccharomyces cerevisiae using a SUC2 promoter

-Amylase production was higher (13 units ml^–1) when a recombinant Saccharomyces cerevisiae containing a SUC2 promoter was grown with 10 g lactic acid l^–1 than without addition (8 units ml^–1). With continuous lactic acid feeding in the inducing phase, -amylase increased to 79 units ml^–1 in a 1-l jar fermenter.     

Inhibition of yeast by lactic acid bacteria in continuous culture: nutrient depletion and/or acid toxicity?

Lactic acid was added to batch very high gravity (VHG) fermentations and to continuous VHG fermentations equilibrated to steady state with Saccharomyces cerevisiae. A 53% reduction in colony-forming units (CFU) ml^–1 of S. cerevisiae was observed in continuous fermentation at an undissociated lactic acid concentration of 3.44% w/v; and greater than 99.9% reduction was evident at 5.35% w/v lactic acid. The differences in yeast cell number in these fermentations were not due to pH, since batch fermentations over a pH range of 2.5–5.0 did not lead to changes in growth rate. Similar fermentations performed in batch showed that growth inhibition with added lactic acid was nearly identical. This indicates that the apparent high resistance of S. cerevisiae to lactic acid in continuous VHG fermentations is not a function of culture mode. Although the total amount of ethanol decreased from 48.7 g l^–1 to 14.5 g l^–1 when 4.74% w/v undissociated lactic acid was added, the specific ethanol productivity increased ca. 3.2-fold (from 7.42×10^–7 g to 24.0×10^–7 g ethanol CFU^–1 h^–1), which indicated that lactic acid stress improved the ethanol production of each surviving cell. In multistage continuous fermentations, lactic acid was not responsible for the 83% (CFU ml^–1) reduction in viable S. cerevisiae yeasts when Lactobacillus paracasei was introduced to the system at a controlled pH of 6.0. The competition for trace nutrients in those fermentations and not lactic acid produced by L. paracasei likely caused the yeast inhibition.     

Activity and stability of immobilised soybean lipoxygenase-1 in aqueous and supercritical carbon dioxide media

The activity of immobilised soybean lipoxygenase-1 (LOX-1) was studied in aqueous and supercritical carbon dioxide (SCCO₂) media for the production of 13S-hydroperoxyoctadecadenoic acid (13S-HPODE). In SCCO₂, it was optimal at 33 °C and 25 MPa. A higher space-time yield of 5.7×10^–3 Ms^–1 mg^–1 LOX-1 for 13S-HPODE was obtained in SCCO₂ compared to only 5×10^–5 Ms^–1 mg^–1 LOX-1 in aqueous medium. The stability of immobilised LOX-1 was only significantly affected by the pressurisation and depressurisation steps during reactions in SCCO₂.     

Bacterial productivity in ponds used for culture of penaeid prawns

The quantitative role of bacteria in the carbon cycle of ponds used for culture of penaeid prawns has been studied. Bacterial biomass was measured using epifluorescence microscopy and muramic acid determinations. Bacterial growth rates were estimated from the rate of tritiated thymidine incorporation into DNA. In the water column, bacterial numbers ranged from 8.3×10⁹ 1^–1 to 2.57×10¹⁰ 1^–1 and production ranged from 0.43 to 2.10 mg Cl^–1 d^–1. In the 0–10 mm zone in sediments, bacterial biomass was 1.4 to 5.8 g C m^–2 and production was 250 to 500 mg C m^–2 d^–1. The results suggested that most organic matter being supplied to the ponds as feed for the prawns was actually being utilized by the bacteria. When the density of meiofauna increased after chicken manure was added, bacterial biomass decreased and growth rates increased.     

Pullulanases of alkaline and broad pH range from a newly isolated alkalophilicBacillus sp. S-1 and aMicrococcus sp. Y-1

Summary Two highly alkalophilic bacteria, and potent producers of alkaline pullulanase, were isolated from Korean soils. The two isolates, identified asBacillus sp. S-1 andMicrococcus sp. Y-1, grow on starch under alkaline conditions and effectively secrete extracellular pullulanases. The two isolates were extremely alkalophilic since bacterial growth and enzyme production occurred at pH values ranging from pH 6.0 to 12.0 forMicrococcus sp. Y-1 and pH 6.0 to 10.0 forBacillus sp. S-1. Both strains secrete enzymes that possess amylolytic and pullulanolytic acitivities. Extracellular crude enzymes of both isolates gave maltotriose as the major product formed from soluble starch and pullulan hydrolysis. Compared to other alkalophilic microbes such asMicrococcus sp. (0.57 units ml^–1),Bacillus sp. KSM-1876 (0.56 units ml^–1) andBacillus No. 202-1 (1.89 units ml^–1) these isolates secreted extremely high concentrations (7.0 units ml^–1 forBacillus sp. S-1 and 7.6 units ml^–1 forMicrococcus sp. Y-1) of pullulanases in batch culture. The pullulanase activities from both strains were mostly found in the culture medium (85–90%). The extracellular enzymes of both bacteria were alkalophilic and moderately thermoactive; optimal activity was detected at pH 8.0–10.0 and between 50 and 60°C. Even at pH 12.0, 65% of original Y-1 pullulanase activity and 10% of S-1 pullulanase activity remained. The two newly isolated strains had broad pH ranges and moderate thermostability for their enzyme activities. These result strongly indicate that these new bacterial isolates have potential as producers of pullulanases for use in the starch industry.     

Extracellular amylase activities ofRhizomucor pusillus andHumicola lanuginosa at initial stages of growth

Among thermophilic fungi,Rhizomucor Pusillus andHumicola lanuginosa have been reported to be among the most prolific producers of amylase, an apparently heat stable enzyme vital to the incorporation of carbon from macromolecular sources such as starch. Yet the highest levels of extracellular amylase in starch-yeast cultures of these fungi were measured after most of the growth had occurred; pre-growth levels appeared to be very small. Since these low levels are the significant ones for growth, a procedure was devised to measure them: 1.162×10^–2 units (mg maltose/ml/min) were measured after two days of growth ofR. pusillus and 6.230×10^–3 units measured after four days of the slower-growingH. lanuginosa. Re-assays of these after dialysis to remove most of the reducing sugars gave 1.689 × 10^–2 units and 1.234 × 10^–2 units, respectively, with all correlation coefficients 0.96 or better.