Production of microbial rennin from Mucor miehei in a continuously fed fermenter

In this study, microbial production of rennin, a milk-clotting enzyme, from a commercial strain of Mucor miehei NRRL 3420 has been investigated in a continuously fed fermenter for prolonged times. The spherical film-type growth of the culture has been accomplished in the fermenter and the effects of medium pH, mixing and dilution rates, and feed -glucose concentration on milk-clotting activity have been elaborated. In the fermenter, optimum operational parameters have been determined as 400 rpm, 0.125 day⁻¹, and 7.5 g l⁻¹ for mixing rate, dilution rate, and feed -glucose concentration, respectively. Under these conditions, the fermenter operated 575 h continuously producing 1.24 IU ml⁻¹ maximum milk-clotting activity without concentration. In the fermenter sample at maximum milk clotting activity, the R factor and specific milk-clotting activity were determined as 1.55 × 10⁻³ IU PU⁻¹ and 5.28 IU mg⁻¹ medium protein, respectively, denoting competitive characteristics of a commercial rennet after concentration.     

以麦秸为基质豌豆根瘤菌的压力脉动固态发酵

生物肥料的常规生产方法是经液态发酵后 ,再以固态基质吸附[1 ] 。其工艺繁琐 ,吸附时易引入大量杂菌 ,从而降低生物肥料的施用效果。而由于静止浅盘固态发酵存在着较大的氧气浓度和温度梯度[2 ,3 ] ,及易染菌等因素 ,所以利用固态发酵成功生产生物肥料的研究较少。近年来 ,固态发酵以其优于液态发酵的特点而成为人们研究的热点[4] ,但至今仍未能普遍应用于工业生产。其主要原因是固态发酵反应器在放大过程中传质、传热困难[3 ] 。Ｂａｊｒａｃｈａｒｙａ＆Ｍｕｄｇｅｔｔ[5 ] 指出 ,解决上述弊端的唯一可行的方法是对反应器中的气相进行控…     

High-yield cellulase production by Trichoderma reesei ZU-02 on corn cob residue

Cellulase production using corn cob residue from xylose manufacture as substrate was carried out by Trichoderma reesei ZU-02. It was found that on the same cellulose basis, the cellulase activity and yield produced on corn cob residue were comparable with that on purified cellulose. Under batch process, the optimum concentration of substrate was 40 g/l and the optimum C/N ratio was 8.0. In 500 ml flasks, cellulase activity reached 5.25 IU/ml (213.4 IU/g cellulose) after seven days' cultivation. In a 30 m(3) stirred fermenter for large scale production, cellulase and cellobiase activity were 5.48 IU/ml (222.8 IU/g cellulase) and 0.25 IU/ml (10.2 IU/g cellulose), respectively, after four days' submerged fermentation. The produced cellulase could effectively hydrolyze the corn cob residue, and the yield of enzymatic hydrolysis reached 90.4% on 10% corn cob residue (w/v) when the cellulase dosage was 20 IU/g substrate.     

l-Lysine-2-monooxygenase production by strains of Pseudomonas fluorescens and P. putida

Twelve strains of Pseudomonas fluorescens and P. putida were grown in a synthetic medium that contained l-lysine as the only source of carbon and nitrogen, and screened for l-lysine-2-monooxygenase production. Best production was by P. putida BKM B-1458 at 30 IU/g wet wt biomass when grown in a shake-flask but 25 IU/g in a 250-l fermenter.     

The influence of pressure on the growth of methanotrophic bacteria

The growth rate and the maximum cell concentration of methanotrophic bacteria are limited by the transfer of methane and oxygen to the culture fluid. The operation under moderate pressure results in an increase in driving force for the mass transfer of both nutrients and, therefore, in a large increase in the attainable biomass concentration. Our laboratory pressure fermenter with a volume of 12 litres operates under a system pressure of up to 0.5 MPa. In this reactor a maximum productivity of 6 g biomass/lh is achieved. However, operating under moderate system pressure and exhaust gas recycling has also disadvantages because the concentrations of the gas phase components may inhibit the growth process. From the results of the laboratory fermenter we have developed kinetic models of the influence of dissolved oxygen and carbon dioxide on the specific growth rate of the methanotrophic strain GB 25. These models are the basis for processing under increased system pressure and exhaust gas recycling.     

Production of leucine amino peptidase in lab scale bioreactors using Streptomyces gedanensis

Studies were conducted on the production of leucine amino peptidase (LAP) by Streptomyces gedanensis to ascertain the performance of the process in shake flask, parallel fermenter and 5-L fermenter utilizing soy bean meal as the carbon source. Experiments were conducted to analyze the effects of aeration and agitation rate on cell growth and LAP production. The results unveiled that an agitation rate of 300 rpm, 50% dissolved oxygen (DO) upholding and 0.15 vvm strategies were the optimal for the enzyme production, yielding 22.72 ± 0.11 IU/mL LAP in parallel fermenter which was comparable to flask level (24.65 ± 0.12 IU/mL LAP) fermentation. Further scale-up, in 5-L fermenter showed 50% DO and 1 vvm aeration rate was the best, producing optimum and the production was 20.09 ± 0.06 IU/mL LAP. The information obtained could be useful to design a strategy to improve a large-scale bioreactor cultivation of cells and production of LAP.     

High level expression of a recombinant xylanase by Pichia pastoris NC38 in a 5 L fermenter and its efficiency in biobleaching of bagasse pulp

A genetically modified XynA gene from Thermomyces lanuginosus was expressed in Pichia pastoris under the control of GAP promoter. P. pastoris expressed greater levels of xylanase (160 IU ml(-1)) on BMGY medium without zeocin after 56 h. The xylanase production by recombinant P. pastoris was scaled up in a 5L fermenter containing 1% glycerol and the highest xylanase production of 139 IU ml(-1) was observed after 72 h. Further studies carried out in fermenter under controlled pH (5.5) yielded a maximum xylanase production of 177 IU ml(-1) after 72 h. The biobleaching efficacy of crude xylanase was also evaluated on bagasse pulp and a brightness of 47.4% was observed with 50 IU of crude xylanase used per gram of pulp, which was 2.1 points higher in brightness than the untreated samples. Reducing sugars (24.8 mg g(-1)) and UV absorbing lignin-derived compounds values were considerably higher with xylanase treated samples.     

Growth of Rhizobium leguminosarum in a periodic pressure oscillating, solid-state fermentation of wheat straw

Wheat straw impregnated with a nutrient solution was used to culture Rhizobium leguminosarum. The fermentation was carried out in a periodic pressure, oscillating, solid-state fermenter. At 30 °C and 3 atm, Rhizobium leguminosarum grew to 5.3×10¹⁰ c.f.u. g^–1 substrate dry matter in about 36 h, while only 1.8×10¹⁰ c.f.u. g^–1 substrate dry matter was obtained in a conventional static tray fermenter.     

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.     

Pulsatile pulmonary microvascular pressure measured with vascular occlusion techniques

The periodic variations of the pulmonary microvascular pressure during pulsatile perfusion were studied in isolated left lower lobes of canine lungs by the arterial occlusion (AO) and double occlusion (DO) techniques. Sixteen AO and eight DO maneuvers evenly distributed within the pump cycle were performed for each of four frequencies: 36, 54, 72, and 90 beats/min. Nearly identical microvascular pressure contours were reconstructed from the AO and DO maneuvers by relocating the measured occlusion pressures in time. These contours lagged behind the pulmonary arterial pressure waveform. Their amplitude decreased from 25 to 14% of the arterial pulse pressure as the pump frequency was increased from 36 to 90 beats/min. The modulus of the pressure transfer function at the site of arterial occlusion decreased as the frequency increased. The phase was negative for all frequencies and it approached -90 degrees for the higher frequencies. Vasoconstriction induced by serotonin resulted in an increase of the magnitude of the AO pressure contour that was nearly proportional to the increase of the pulmonary arterial pulse pressure. In contrast, elevation of the lobar venous pressure to 10 mmHg increased the amplitude of the AO pressure contour, whereas it slightly decreased the pulmonary arterial pulse pressure. These experiments demonstrate that the AO and DO pressures fluctuate markedly during pulsatile perfusion. Their oscillations would be indicative of the pulsatility in the pulmonary microvascular bed.     

增大罐压提高脱氮假单胞菌发酵生产维生素B12的产量

【目的】提高发酵罐的罐压,增加维生素B12的产率。【方法】利用常规代谢通量分析(MFA)方法,对脱氮假单胞菌生产维生素B12的发酵过程进行研究。【结果】发现随着VB12合成速率的加快,磷酸烯醇式丙酮酸(PEP)羧化生成草酰乙酸(OAA)的通量明显加大,以满足维生素B12合成对前体的需求。根据该分析结果,对发酵工艺进行了改进,即在脱氮假单胞菌进入合成维生素B12阶段时,提高发酵罐的罐压,增加发酵液中二氧化碳的溶解度,从而强化了羧化回补途径。维生素B12的产率明显增加,发酵160 h的产物浓度为176 mg/L,比对照批次终浓度147 mg/L高出了19.7%。【结论】通过增大罐压提高了脱氮假单胞菌进入合成维生素B12的产量。     

A Shortcut to the Optimization of Cellulase Production Using the Mutant Trichoderma reesei YC-108

Trichoderma reesei YC-108, a strain isolated by a kind of newly invented plate was found to over produce cellulase and it was then used as a cellulase producer. To get the maximum amount of cellulase, the combination of the medium ingredients, which has a profound influence on metabolic pathway was optimized using response surface methodology. The optimum composition was found to be 24.63 g/L wheat bran, 30.78 g/L avicel, and 19.16 g/L soya-bean cake powder. By using the optimized medium, the filter paper activity (FPA) increased nearly five times to 15.82 IU/mL in a 30 L stirred fermenter, carboxymethyl cellulase activity (CMCase) was increased from 83.02 to 628.05 IU/mL and the CMCase/FPA ratio was nearly doubled compared with the parent strain at initial medium.     

Volumetric productivity improvement for endoglucanase of Trichoderma pseudokoingii S-38

AIMS: The objective of this study was to design an economically feasible process for endoglucanase (EG) production. METHODS AND RESULTS: Trichoderma pseudokoingii S-38 EG synthesis was studied. Initially, either glucose at 2.5, 5 or 10 g l-1, or cellulose powder (CF11) at 5 g l-1 was used as the sole carbon source. The results showed that enzyme synthesis and biomass formation were closely correlated, and both were affected by the carbon source. To improve EG volumetric product efficiency, a new technique was developed. Glucose and CF11 (2.5 and 5 g l-1, respectively) were used as initial carbon source, and glucose was added at 2.5 g l-1 day-1. EG activity, volumetric and specific EG productivities were 6.17 IU l-1, 53 IU l-1 h-1 and 114.3 IU (g cell protein)-1 h-1, respectively. Batch production in a 2-l laboratory fermenter confirmed the advantage of the technique. The product contained 10.86 IU ml-1 EG activity in 88 h. The volumetric and specific EG productivities were 123.4 IU l-1 h-1 and 177.8 IU (g cell protein)-1 h-1, respectively. CONCLUSIONS: These results suggest that optimization of the ratio of glucose to CF11 for balancing the induction and growth rate in the production of EG may lead to technical and economical benefits. SIGNIFICANCE AND IMPACT OF THE STUDY: A new technique was developed for the production of EG which improves both the volumetric product efficiency and the specific activity.     

Pectin lyase production by Penicillium griseoroseum grown in sugar cane juice in repeated batch cultures

Penicillium griseoroseum cultured in the presence of sucrose and yeast extract produces pectin lyase (EC 4.2.2.10) (PL) in the absence of its natural inducer pectin. This fungus was cultured in a fermenter at an aeration rate of 0.5 l/min for the first 25 h and 1.0 l/min for the remainder of the culture period, and at a stirring rate of 200 rev/min for the entire culture period. Fungal spores were inoculated directly into the fermenter at a final concentration of 5 × 10⁴ spores/ml. The fungus was cultured in minimal medium supplemented with powdered dehydrated sugar cane juice, producing PL without added yeast extract. Maximum PL activity (0.067 IU/ml) was obtained after 65 h in batch culture. Pellet morphology of the mycelia made it possible to carry out three cycles of repeated batch culture. The same medium was used for renewal as for the single batch culture. The initial cycle was 53 h, after which approximately 0.103 IU/ml of PL was obtained. After this period, the medium was renewed and fermentation continued for two more cycles, which lasted approximately 20 h. Activity of PL obtained in the second cycle was approximately 0.118 IU/ml and in the third, approximately 0.109 IU/ml.     

Periodic hemodynamics in skeletal muscle during local arterial pressure reduction.

The time-dependent features of red blood cell flow were evaluated with laser-Doppler flowmetry (LDF) in the left gastrocnemius muscle of 31 anesthetized New Zealand White rabbits during stepwise arterial occlusion. During the control period with a median femoral pressure of 72 mmHg, 29 animals showed minor irregular fluctuations in LDF blood flow, and only two animals displayed periodic variations of blood flow. Lowering femoral arterial pressure induced maximal periodic blood flow variations at a median pressure of 35 mmHg in all animals with a median frequency of 1.5 cycles/min (termed "slow-wave flow motion"). The median amplitude was 48% of the corresponding average flow. These slow waves disappeared at a median femoral pressure of 20 mmHg. The median LDF flow value was 4.00 arbitrary units (AU) at control pressure and 2.05 AU at maximum slow-wave flow motion. When slow-wave flow motion was seen at several pressure levels, their frequency was identical, which supports the local pacemaker concept. This study promotes a novel concept for the role and physiological significance of periodic hemodynamics in that it is a condition not characteristic for normal control situations but is activated below a specific local arterial blood pressure and flow threshold, which is known to be the lower end of autoregulation in the microcirculation of rabbit skeletal muscle. This also suggests that slow-wave flow motion is primarily under local control mechanisms.     

Estimation of alveolar pressure during forced oscillation of the respiratory system.

A method for obtaining a continuous estimate of alveolar pressure (PAlv) during periodic flow is described; it was developed to improve the precision of measurements of airway and respiratory tissue impedance using the improved resolution of relatively high-frequency (approximately 5 Hz) singlas. The respiratory system was modulated with a piston pump, and lung volume and the volume change due to compression and expansion of alveolar gas were measured plethysmorgraphically; these signals and an analog divider were used to obtain a continuous solution of Boyle's law during flow. The plethysmorgraph was of the "flow" type; with it volume changes at frequencies up to 10 Hz and with rates of change up to 6 l/s were measured without amplitude or phase distortion. The method permits control of frequency and flow amplitude during PAlv measurement and calibration of PAlv in the absence of an active chest wall. However, it is technically complex.     

Intrauterine pressure wave-form characteristics of spontaneous first stage labor.

Intrauterine pressure wave-form parameters were measured in 827 contractions obtained from 26 patients in spontaneous labor. The coefficients of correlation between the maximal and minimal rates of pressure change and the maximal pressure amplitude were 0.78 and 0.63, respectively, and greater than or equal to 0.70 in 22/26 patients. Contractions partitioned into decile statistical groups of the pressure amplitude and both maximal and minimal rates. A linear relationship between these parameters has therefore been established. Contractions of greater amplitude tend to be longer, but the relationship between duration and amplitude is nonlinear with a limiting maximum contraction time. The duration of the midportion of the pressure wave appears invariate with respect to wave amplitude and only start-up and termination times increase with increasing amplitude. Mean values and standard deviations of the maximal amplitude (40.4 +/- 16.9mmHg). the maximal (2.4 +/- 0.9 mmHg/s) and minimal (-2.1+/- 0.9 mmHg/s)rates of pressure change, and the total duration of contractions (68.6 +/- 17.8s) were determined.     

Tower fermentation of sugar cane juice

Summary Sugar cane juice, of feed fermentables concentration of 100–180g/l, was simply and rapidly fermented to ethanol in a tower fermenter, using a naturally flocculant yeast. Stable cell densities of 65–80g dry wt/l were obtained. Conversion and ethanol productivity data are given as a function of throughput and initial feed concentration. The limitation to fermenter performance with this yeast was imposed by carryover of non-fermented sugars, principally fructose, rather than washout of the yeast flocs under high hydraulic loadings (residence times of less than 1.5 hours). Further improvement of the fermenter performance may be achieved by strain selection.     

Application of factorial designs for optimization of cyclodextrin glycosyltransferase production from Klebsiella pneumoniae pneumoniae AS-22.

Production of cyclodextrin glycosyltransferase (CGTase) from Klebsiella pneumoniae pneumoniae AS-22 was optimized in shake flasks using a statistical experimental design approach. Effect of various components in the basal medium, like carbon, nitrogen, phosphorus, and mineral sources as well as initial pH and temperature, were tested on enzyme production. The optimum concentrations of the selected media components were determined using statistical experimental designs. Two level fractional factorial designs in five variables, namely, dextrin, peptone, yeast extract, ammonium dihydrogen orthophosphate, and magnesium sulphate concentrations were constructed. The optimum medium composition thus found consisted of 49.3 g/L dextrin, 20.6 g/L peptone, 18.3 g/L yeast extract, 6.7 g/L ammonium dihydrogen orthophosphate, and 0.5 g/L magnesium sulphate. The maximum CGTase activity obtained was 21.4 U/mL in 28 h of incubation. The cell growth and CGTase production profiles were studied with the optimized medium in shake flasks and in 1-L fermenters. It was observed that the enzyme production was growth associated both in shake flask and in fermenter, although it was slower in shake flask. The maximum CGTase activity obtained in the fermenter was 32.5 U/mL in 16 h. The optimized medium resulted in about 9-fold increase in the enzyme activity as compared to that obtained in the basal medium in shake flask as well as in fermenter.     

Hormones and blood pressure: clues from chronobiology

Results relating to the study of several hormones homeostatically related to blood pressure (renin-angiotensins, mineralocorticoids, glucocorticoids, atrial natriuretic factor) are reviewed. Most experimental data and clinical observations concerning 'hypertension' are specified neither as to circadian stage nor do they assess rhythm parameters. Such homeostatic data suggest that several groupings of hormones play a major role in coordinating blood pressure. The majority of hormones involved have multiple actions and the diversity of effects is often unexplained in homeostatic terms. In chronobiology, opposite effects are seen in response to the same stimulus depending upon the stage of the organism's multifrequency rhythms and their intermodulation. The periodic pattern exhibited by some of the hormones coordinating blood pressure in health and the capability of these hormones to modify temporal structure, either inducing a change in timing (circadian blood pressure ecphasia) or in amplitude (amplitude-hypertension) or in mean level of the values (MESOR-hypertension) are reviewed as well.