Improving a process of cultivation of bifidobacteria in a bioreactor to obtain lyophilized seed culture

The parameters of the cultivation process and the characteristics of the culture growth have been analyzed. The phases of the population growth have been determined. The existence of short stages differing in the physiological state of the cells, their resistance to damaging factors and metabolic activity within the deceleration phase of the growth of bifidobacteria has been experimentally substantiated. To harvest the biomass, the period of the completion of the cultivation process has been chosen. The lyophilized seed culture in which a high percentage of viable cells is preserved for one year has been obtained.     

Bordetella pertussis agglutinogens in cultivation dynamics

Bordetella pertussis growth phases during homogenous batch dynamic cultivation in the liquid medium as well as during the static cultivation on the solid medium were established. The maximal activity of agglutination reaction with antisera to B. pertussis agglutinogens 1, 2, and 3 was detected in bacterial culture at the end of exponential phase of growth. The activity of agglutination reaction decreased when cultures in stationary and death phases were used. During transition from exponential to death phase level of antibodies to agglutinogen 2 decreased by4 - 32 times. 2 - 4-fold decrease of antibodies level was observed when antiserum to agglutinogen 3 was used. Activity of agglutination reaction with antiserum to agglutinogen 1 was high and did not depend from phase of growth. When polyvalent antiserum to B. pertussis was used 4-fold decrease of antibody titers was observed in parallel with change of growth phases. Sera from rabbits immunized with B. pertussis cultures from the middle of exponential growth phase, the end of this phase, and begin of the death phase had high (maximal) level of agglutinating antibodies (6400), which was detected on 101 day after immunization with the former culture and on 31 day after immunization with either of the two latter cultures. To the end of experiment (292 day) titers decreased to 800, 3200, and 1600 respectively. These findings confirm an advisability of use of exponential growth culture for immunization of rabbits in order to obtain highly active diagnostic antisera to B. pertussis.     

Seed Dormaney in Acer: Maturation in Relation to Dormancy in Acer Pseudoplatanus L

Maturation of Acer pseudoplatanus seeds comprises three phases.The first is a growth phase lasting for about 100 d, duringwhich fresh weight and dry weight increase steadily. The endof the growth phase is marked by a temporary cessation of weightincrease and is followed by a phase of reserve accumulationextending for a further 60 d. During this phase levels of extractablelipid, soluble and insoluble carbohydrate, protein, and membrane-boundribosomes show a marked increase. The third phase is a periodof desiccation, lasting at least 30 d. The kind of dormancyexhibited by the immature seed is characteristic of the stageof maturation. Before the desiccation phase the embryo has nocapacity for germination even when subjected to treatments knownto promote germination in the mature seed. In the desiccationphase the seed becomes responsive to chilling, but a wide rangeof hormones and other substances known to promote seed germinationare ineffective. Embryos contain a persistently high level ofacidic inhibitors throughout maturation. The level of neutralinhibitors, initially high, showed a marked drop after 150 dand remained low for the rest of the maturation period.     

Biotechnological aspects of the production of the anticancer drug podophyllotoxin

The natural lignan podophyllotoxin, a dimerized product of two phenylpropanoid moieties which occurs in a few plant species, is a pharmacologically important compound for its anticancer activities. It is used as a precursor for the chemical synthesis of the anticancer drugs etoposide, teniposide and etopophose. The availability of this lignan is becoming increasingly limited because of the scarce occurrence of its natural sources and also because synthetic approaches for its production are still commercially unacceptable. Biotechnological production using cell culture may be considered as an alternative source. Selection of the best performing cell line, its maintenance and stabilization are necessary prerequisites for its production in bioreactors and subsequent scale-up of the cultivation process to the industrial level. Scale-up of growth and product yield depends on a multitude of factors, such as growth medium, physicochemical conditions, seed inoculum, type of reactor and processing conditions. The composition of the growth medium, elicitors and precursors, etc. can markedly influence the production. Optimum levels of parameters that facilitate high growth and product response in cell suspensions of Podophyllum hexandrum have already been determined by statistical design. P. hexandrum cells have successfully been cultivated in a 3-l stirred-tank bioreactor under low shear conditions in batch and fed-batch modes of operation. The batch kinetic data were used to identify the mathematical model which was then used to develop nutrient-feeding strategies for fed-batch cultivation to prolong the productive log phase of cultivation. An improvement in the production of podophyllotoxin to 48.8 mg l^–1 in a cell culture of P. hexandrum was achieved, with a corresponding volumetric productivity of 0.80 mg l^–1 day^–1, when the reactor was operated in continuous cell-retention mode. Efforts are being made to further enhance its production levels by the development of hairy root culture or by varying the channeling of precursors towards the desired biosynthetic pathway by molecular approaches.     

Processes of spore formation and gramicidin C formation by Bacillus brevis var. G.B.]

Correlation between gramidicin C biosynthesis and sporulation in the process of Bac. brevis var. G.B. cultivation under various aeration conditions was studied. It was shown that biosynthesis of gramicidin C was characteristic of the young cells and its level was the highest during the culture active growth. The time of the sporulating forms appearance depended on the aeration rate which defined the quantitative composition of the population during the phase of the culture active growth and the stationary phase. Under the optimal aeration conditions the spore formation started during the phase of the culture active growth after some decrease in the maximum level of the cell productivity with respect to the antibiotic. When the aeration rate was increased the spore formation was shifted to later periods of the culture development, i.e. the stationary phase and the phase of the cell autolysis, the gap between the highest levels of gramicidin C buosynthesis and the beginning of sporulation being increased. Under certain aeration conditions the spore formation was not observed, while gramicidin C was synthesized. A conclusion has been made that there is no correlation between gramacidine C biosynthesis and sporualtion in Bacillus brevis var. G.B.     

Perfusion seed cultures improve biopharmaceutical fed‐batch production capacity and product quality

Volumetric productivity and product quality are two key performance indicators for any biopharmaceutical cell culture process. In this work, we showed proof‐of‐concept for improving both through the use of alternating tangential flow perfusion seed cultures coupled with high‐seed fed‐batch production cultures. First, we optimized the perfusion N‐1 stage, the seed train bioreactor stage immediately prior to the production bioreactor stage, to minimize the consumption of perfusion media for one CHO cell line and then successfully applied the optimized perfusion process to a different CHO cell line. Exponential growth was observed throughout the N‐1 duration, reaching >40 × 10⁶ vc/mL at the end of the perfusion N‐1 stage. The cultures were subsequently split into high‐seed (10 × 10⁶ vc/mL) fed‐batch production cultures. This strategy significantly shortened the culture duration. The high‐seed fed‐batch production processes for cell lines A and B reached 5 g/L titer in 12 days, while their respective low‐seed processes reached the same titer in 17 days. The shortened production culture duration potentially generates a 30% increase in manufacturing capacity while yielding comparable product quality. When perfusion N‐1 and high‐seed fed‐batch production were applied to cell line C, higher levels of the active protein were obtained, compared to the low‐seed process. This, combined with correspondingly lower levels of the inactive species, can enhance the overall process yield for the active species. Using three different CHO cell lines, we showed that perfusion seed cultures can optimize capacity utilization and improve process efficiency by increasing volumetric productivity while maintaining or improving product quality. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:616–625, 2014     

Physiology of the growth and supersynthesis of DNA-polymerase in Escherichia coli during 2-stage continuous cultivation

The physiology of growth under the conditions of batch and continuous cultivation was studied with the recombinant strain of Escherichia coli CM 5199 capable of DNA polymerase I superproduction. The specific growth rate of the strain is 0.8 h-1 under the conditions of continuous cultivation which is almost 2.5 times greater than that in the exponential phase of batch cultivation. When the strain was cultivated at a flow rate above 0.3 h-1, the biomass concentration in the fermenter decreased and the culture was no more limited by the carbon source in the absence of other growth limiting components of the medium. Apparently, the metabolic product ceased to inhibit high growth rates of the culture under the conditions of continuous cultivation. The rate of DNA polymerase synthesis correlated with the specific growth rate and the respiration activity of the culture when the lambda pol A prophage was induced in the cells. The authors discuss the effectiveness of ribosome operation in the cells at a growth rate of 0.05 to 0.3 h-1 and the content of ribosomes at a higher growth rate in relation to DNA polymerase I synthesis.     

Use of frozen bagged seed inoculum for secondary metabolite and bioconversion processes at the pilot scale

Frozen bagged seed inoculum was prepared, thawed and tested for seven cultures. Thawing techniques were developed and other key influences on thawing rate were quantified; seed bag thawing without a water bath rarely required more than 4 to 5 h and was as short as 0.5 to 1 h for lower fill volume bags. Testing included growth of bagged seed as a function of bag fill volume (0.5, 1.0, 2.0, and 3.5 L), comparison of culture age at time of bagging, growth of bagged versus laboratory-prepared seed, productivity of production cultures derived from bagged versus laboratory-prepared seed, growth of bagged seed as a function of volume percent glycerol added at time of bagging, and growth of bagged seed as a function of frozen storage time and temperature. For each culture tested, conditions were developed such that seed tanks inoculated with bagged seed showed only minimal delay in attaining the target oxygen uptake rate (OUR) relative to seed tanks inoculated with laboratory-prepared inoculum. Although the bag fill volume did influence culture growth in some cases, bag fill volumes required were reasonable (typically 2.0 to 3.5 L) compared with laboratory seed inoculum volumes of 2.0 L. In the most remarkable example, frozen bagged seed was prepared from a second-stage seed-tank cultivation of Glarca lozoyensis, then thawed and inoculated into first-stage seed medium. It grew to the desired OUR in a similar timeframe as laboratory-prepared inoculum inoculated into first-stage seed medium. Thus, the frozen bagged seed replaced an existing laboratory inoculum preparation period of 7 days without an appreciable delay in either of the two subsequent seed-tank growth stages. Furthermore, productivities were found to be comparable for bagged-seed-derived and laboratory-seed-derived production cultivations for four different fermentation processes.     

影响杏黄兜兰种子萌发的因素

通过在不同条件下杏黄兜兰 (Paphiopedilumarmeniacum)种子萌发的观察 ,对影响其萌发的诸因子报道如下 :1)果实的生长期与种子的萌发率有关。实验表明种子采自生长期为 6 0d的果实 ,发芽率为 3 5 % ,采自 12 0d的果实 ,发芽率为 4 0 % ,采自 180d的果实 ,发芽率为 18 3%。 2 )培养基也会影响到种子的萌发 ,种子在 1 5MS内培养 ,萌发率明显高于培养于MS ,RE和改良HyponexNo 1内的种子。 3)培养基 (1 5MS)掺入添加物也会影响到种子的萌发率 ,如掺入 10 %椰子水会促使种子的萌发率达到很高的水平 ,掺入马铃薯泥 (5 0g L)或胰化胨 (2g L) ,种子的萌发率会达到较高的水平 ,而掺入香蕉泥则会对种子的萌发率产生负面影响 ,掺入活性炭 (2g L)会促使种子萌发和幼苗发育。 4 )与固态培养基相比 ,种子在液体悬浮培养基内的萌发速度更快 ,幼苗更为整齐划一。     

Role of elongation and secondary pathways in S6 amyloid fibril growth

The concerted action of a large number of individual molecular level events in the formation and growth of fibrillar protein structures creates a significant challenge for differentiating between the relative contributions of different self-assembly steps to the overall kinetics of this process. The characterization of the individual steps is, however, an important requirement for achieving a quantitative understanding of this general phenomenon which underlies many crucial functional and pathological pathways in living systems. In this study, we have applied a kinetic modeling approach to interpret experimental data obtained for the aggregation of a selection of site-directed mutants of the protein S6 from Thermus thermophilus. By studying a range of concentrations of both the seed structures, used to initiate the reaction, and of the soluble monomer, which is consumed during the growth reaction, we are able to separate unambiguously secondary pathways from primary nucleation and fibril elongation. In particular, our results show that the characteristic autocatalytic nature of the growth process originates from secondary processes rather than primary nucleation events, and enables us to derive a scaling law which relates the initial seed concentration to the onset of the growth phase.     

重组巴氏毕赤酵母高密度发酵表达rHSA

对基因工程菌Pichiapastoris的摇瓶发酵条件进行了试验 ,并根据摇瓶发酵的优化结果进行了补料分批高密度发酵。在摇瓶发酵时 ,甲醇诱导基因工程菌P .pastoris表达重组人血清白蛋白的发酵周期为 96h ;甲醇的最佳诱导浓度为 1 0g L ;发酵pH范围为 5 72～ 6 5 9;在摇瓶培养时 ,随着接种量的增加 ,虽然目的蛋白表达量缓慢增加 ,但单位细胞光密度的蛋白产率却明显下降 ,符合y =1 2 941x- 0 50 59方程 (线性相关系数r=0 9789) ,其限制性因子很可能为溶氧。在分批发酵 ,接种量为 1 0 %且种子细胞光密度 (OD60 0 )为 2 0左右时 ,细胞生长的延迟期为 2 1 1h左右 ,细胞生长光密度与培养时间的关系模型为 :y =0 7841e0 .2 3 19t(线性相关系数r=0 .993 6 ) ;在补料发酵时细胞干重浓度可达到 1 1 5g L— 1 6 0g L ,在 1 2 0h重组人血清白蛋白表达量最大达到 3 6g L。     

In vitro amino acid requirements of Bacillus anthracis cells

In the process of batch cultivation in a synthetic medium B. anthracis cells actively consume free amino acids. The maximum amino acid consumption per unit of biomass occurs at the exponential phase of growth, but the consumption of serine is maintained at a high level also during the stationary phase. At the same time the consumption of proline by both vaccine and virulent strains is insignificant at the stationary phase of growth. In contrast to B. anthracis virulent strains, vaccine strains have been shown to consume no lysine, histidine, arginine and tryptophan.     

Formation of ethyl acetate by Kluyveromyces marxianus on whey: Influence of aeration and inhibition of yeast growth by ethyl acetate

The ability of the yeast Kluyveromyces marxianus to convert lactose into ethyl acetate offers good opportunities for the economical reuse of whey. The formation of ethyl acetate as a bulk product depends on aerobic conditions. Aeration of the bioreactor results in discharge of the volatile ester with the exhaust gas that allows its process‐integrated recovery. The influence of aeration (varied from 10 to 50 L/h) was investigated during batch cultivation of K. marxianus DSM 5422 in 0.6 L whey‐borne medium using a stirred reactor. With lower aeration rates, the ester accumulated in the bioreactor and reached higher concentrations in the culture medium and the off gas. A high ester concentration in the gas phase is considered beneficial for ester recovery from the gas, while a high ester concentration in the medium inhibited yeast growth and slowed down the process. To further investigate this effect, the inhibition of growth by ethyl acetate was studied in a sealed cultivation system. Here, increasing ester concentrations caused a nearly linear decrease of the growth rate with complete inhibition at concentrations greater than 17 g/L ethyl acetate. Both the cultivation process and the growth rate depending on ethyl acetate were described by mathematical models. The simulated processes agreed well with the measured data.     

The potential of flow cytometric analysis for the characterization of hybridoma cells in suspension cultures

Flow cytometric (FC) analysis was applied to determine changes at cellular level during the cultivation of hybridoma cell line MN12 in a suspension batch culture. The relative cell size, cytoplasmic and membrane IgG content and the viability were monitored. Besides, the specificity of the cytoplasmic and membrane IgG was ascertained by means of a synthetic peptide containing the antigenic epitope recognized by the antibody. Cell size was found to increase during the exponential growth phase. The viability as determined by FC follows a similar pattern with the viability data obtained by the conventional trypan blue exclusion test. The relative cytoplasmic and membrane IgG contents were high during the exponential growth and low during stationary phase. Measurement of cell cycle distribution and the antibody content in the culture fluid, indicated that the major part of the cytoplasmic IgG is secreted by cells in the G1-phase. It is concluded that flow cytometry is a useful tool to characterize hybridoma cell lines in a suspension batch culture.     

Effect of the producer type on the nature of antibiotic fermentation

Fermentation processes in production of bacitracin, a polypeptide antibiotic by Bacillus licheniformis, and oleandomycin, a macrolide antibiotic by Streptomyces antibioticus, were studied comparatively. It was shown that the antibiotic-producing actinomycete was characterized by a prolonged phase of growth retardation. The highest efficiency of the control actions was observed at the beginning of the fermentation. They were aimed at intensifying the substrate usage during the growth phase and activation of cell metabolism. Controlled cultivation of the Bacillus representative was based on its capacity of achieving the maximum growth rate possible under the certain conditions. Therefore, an increase in the quantity of the synthesized antibiotic was due, under such conditions, to inhibition of the culture growth by various means including lower mass exchange intensity.     

“Organized stress” for robust scale-up of intensified production process with fed-batch seed bioreactor

Process intensification has been widely used for many years in the mammalian biomanufacturing industry to increase productivity, agility and flexibility while reducing production costs. The most commonly used intensified processes are operated using a perfusion or fed-batch seed bioreactor enabling a higher than usual seeding density in the fed-batch production bioreactor. Hence, as part of the growth phase is shifted to the seed bioreactor, there is a lower split ratio, which increases the criticality of the seed bioreactor and could impact production performance. Therefore, such intensified processes should be designed and characterized for robust process scale-up. This research work is focused on intensified processes with high seeding density inoculated from seed bioreactor in fed-batch mode. The impact of the feeding strategy and specific power input (P/V) in the seed bioreactor and on the production step with two different cell lines (CL1 and CL2) producing two different monoclonal antibodies was investigated. Cell culture performance in the production bioreactor has been improved due to more stressful conditions for the cells in the seed bioreactor and the impact of the production bioreactor P/V on the production performance was limited. This is the first reported study highlighting a positive impact of cellular stress in seed bioreactors on intensified production bioreactor with the introduction of the “organized stress” concept.     

Cultivation of Neisseria meningitidis serogroups A, B and C in a synthetic nutrient broth

The processes of the cultivation of N. meningitidis, serogroups A, B and C, in a liquid synthetic culture medium have been studied. Strictly group-specific biomass has been obtained. The maximum productivity at all stages of the batch cultivation of N. meningitidis strains 125 and 133 in this medium does not differ from that at similar stages of cultivation in modified Cohen-Wheller semisynthetic medium. In the serotype antigen preparations obtained from N. meningitidis strain 125 grown in the above-mentioned liquid synthetic culture medium basic polypeptides with a molecular weight of 33000, 36000 and 41000 D have been detected. Their presence in N. meningitidis cells is linked with the growth phase of the population.     

溶氧水平对红豆杉细胞悬浮培养的影响研究

紫杉醇 (Ｔａｘｏｌ)是源自红豆杉提取物的一种高度衍生化的二萜类化合物 ,临床实验结果表明紫杉醇对于卵巢癌、乳腺癌、胃肠道癌等具有明显的抗肿瘤活性[1] ,因而受到世界各国的广泛关注 ,并已被美国食品与药品管理局 (ＦＤＡ)批准用于卵巢癌与乳腺癌的治疗[2 ] 。到目前为止紫杉醇仍然主要从树皮中提取 ,但由于红豆杉生长缓慢 ,天然资源非常有限 ,加快其替代来源的研究势在必行。利用植物细胞悬浮培养生产紫杉醇作为一种可行的选择 ,近年来取得了较大的进展[3 ,4 ] 。本文研究了摇瓶及 2 0 Ｌ反应器培养过程的溶氧水平对细胞生长及紫杉醇…     

Use of the luciferin-luciferase assay of ATP for measuring the bacterial growth: Application to Escherichia coli

The relative constancy of ATP content per unit of dry biomass in different microorganisms enables to use the specific, sensitive and quick luciferin-luciferase method for ATP assay for indirect quantitation of microbial biomass by measuring the ATP content in biomass samples.The aim of this work was to investigate the feasibility of using the ATP concentration for the monitoring of the growth of Escherichia coli K 12 W 3350 in different cultivation conditions. Statistically significant high correlation coefficients (r > 0.9) between the ATP content (ATP/ml) and the other growth characteristics examined showed that the ATP content of the culture is as suitable characteristic as the optical density of the culture, total cell number per ml or total cell volume per ml for the monitoring of the growth of E.coliin batch culture in mineral medium with glucose at different growth temperatures (27–42 °C) as well as in fed-batch culture.