A cyclical semicontinuous process for production of human alpha 1-antitrypsin using metabolically induced plant cell suspension cultures

Transgenic rice suspension cultures were utilized to produce a human therapeutic protein, recombinant alpha(1)-antitrypsin (rAAT), in a cyclical, semicontinuous operation. Recombinant protein production was induced by removing the carbon source from the cell culture medium. The transgenic rice cells secreted the rAAT into the medium, and therefore medium exchanges could be performed for consecutive growth and protein expression phases. The process consisted of three cycles over a 25-28 day period, with growth phases lasting 4-6 days each and protein expression phases lasting 2.5-5 days each. Biomass and sugar concentrations, oxygen uptake rate, cell viability, culture pH, total extracellular protein, and active rAAT were measured throughout the cyclical process. The data profiles were reproducible between separate cyclical runs where, following each induction period, cell growth and viability could be reestablished once sucrose was added back to the culture. Volumetric productivities ranged from 3 to 12 mg active rAAT/(L day) for individual cycles with overall volumetric productivities of 4.5 and 7.7 mg active rAAT/(L day).     

Production of human alpha-1-antitrypsin from transgenic rice cell culture in a membrane bioreactor

Transgenic plant cell cultures offer a number of advantages over alternative host expression systems, but so far relatively low product concentrations have been achieved. In this study, transgenic rice cells are used in a two-compartment membrane bioreactor (CELLine 350, Integra Biosciences) for the production of recombinant alpha-1-antitrypsin (rAAT). Expression of rAAT is controlled by the rice alpha-amylase (RAmy3D) promoter, which is induced in the absence of sugar. The extracellular product is retained in the bioreactor's relatively small cell compartment, thereby increasing product concentration. Due to the packed nature of the cell aggregates in the cell compartment, a clarified product solution can be withdrawn from the bioreactor. Active rAAT reached levels of 100-247 mg/L (4-10% of the total extracellular protein) in the cell compartment at 5-6 days postinduction, and multiple inductions of the RAmy3D promoter were demonstrated.     

Improvement of Panax notoginseng cell culture for production of ginseng saponin and polysaccharide by high density cultivation in pneumatically agitated bioreactors

A Panax notoginseng cell culture was successfully scaled up from shake flask to 1.0-L bubble column reactor and concentric-tube airlift reactor. High-density bioreactor batch cultivation was carried out using a modified MS medium. The maximum cell density in batch cultures reached 20.1, 21.0 and 24.1 g/L in the shake flask, bubble column and airlift reactors, respectively, and their corresponding biomass productivity was 950, 1140 and 1350 mg/(L x d) for each. The productivity of ginseng saponin was 70, 96 and 99 mg/(L x d) in the flask, bubble column and airlift reactors, respectively; and the polysaccharide productivity reached 104, 119 and 151 mg/(L x d) for each. Furthermore, a fed-batch cultivation strategy was developed on the basis of specific oxygen uptake rate (SOUR), i.e., sucrose feeding before a sharp decrease of SOUR, and the highest cell density of 29.7 g/L was successfully achieved in the airlift bioreactor on day 17 with a very high biomass productivity of 1520 mg/(L x d). The concentrations of ginseng saponin and polysaccharide reached about 2.1 and 3.0 g/L, respectively, and their productivity was 106 (saponin) and 158 mg/(L x d) (polysaccharide). This work successfully demonstrated the high-density bioreactor cultivation of P. notoginseng cells in pneumatically agitated bioreactors and the reproduction of the shake flask culture results in bioreactors. The cell density, biomass productivity, production titer and productivity of both ginseng saponin and polysaccharide obtained here were the highest that have been reported on a reactor scale for all the ginseng species.     

Fed-batch cultivation of transgenic rice cells for the production of hCTLA4Ig using concentrated amino acids

RAmy3D promoter is capable of expressing high levels of recombinant proteins in response to the depletion of sugar in transgenic rice cell suspension cultures. For this reason, it is necessary to change the growth medium into sugar-free production medium to produce the target protein, human cytotoxic T-lymphocyte antigen 4-immunoglobulin (hCTLA4Ig), using the inducible RAmy3D promoter. Since the two-stage culture is a complex process to perform in large-scale, a fed-batch method was evaluated with the addition of concentrated amino acids before the depletion of sugar to induce hCTLA4Ig production. This fed-batch culture was found to be effective and the production of hCTLA4Ig was enhanced up to 1.2-fold compared to that of two-stage cultures with medium exchange. In addition, when this fed-batch culture was performed in a 15-l stirred-tank bioreactor, maximum hCTLA4Ig level was 76.5 mg l⁻¹ at day 10.     

Effects of sugar concentration on recombinant human alpha(1)-antitrypsin production by genetically engineered rice cell

Productivity of recombinant human alpha(1)-antitrypsin (rAAT) with a genetically engineered rice cell using an inducible promoter has been studied by batch-wise and continuous production. A simple model explained the effect of proteases released from the disrupted cells on the rAAT degradation. Glucose concentration in the medium significantly affected the rAAT productivity in the continuous production, because the rAAT was induced by sugar depletion. When the fresh medium containing 5mM glucose was supplied to the continuous bioreactor, induction time was long and the productivity was low, indicating that the glucose concentration in the cells was high enough as to repress the promoter. When the glucose concentration in the fresh medium was reduced to 0.5mM, total amount of rAAT produced in 70h cultivation reached 6.7-7.6mg/g-dry cell, which was two times larger than the control medium without glucose.     

Large-scale (20 l) culture of surface-immobilized Catharanthus roseus cells.

Surface-immobilized C. roseus cell cultures were grown in a 20-l modified airlift bioreactor operated at 0.51 vvm (kLa approximately 8 h-1) under various gassing regimes [air, 2% (v/v) and 5% CO2]. Extracellular ammonium, phosphate, and nitrate ions as well as carbohydrate uptake and pH value of the medium were monitored together with on-line dissolved oxygen concentration, conductivity of the medium, and carbon dioxide production rate (CPR) of the cultures. Cultures supplemented with 2% CO2 showed higher nitrate (5.0-7.0 mM d-1) and carbohydrate (3.3 g l-1 d-1) uptake rates and biomass production (mu approximately 0.24 d-1, yield approximately 0.33 g dw g CHO-1 and 7.4 g dw L-1) as compared to air (3.6 mM d-1, 2.1 g l-1 d-1; 0.20 d-1, 0.25 g dw g CHO-1 and 5 g dw l-1) and 5% CO2 (2.0-3.6 mM d-1, 2.0 g l-1 d-1; 0.11 d-1, 0.20 g dw g CHO-1 and 5 g dw l-1) cultures and as reported previously for suspension cultures. In addition, air and 5% CO2 cultures displayed incomplete carbohydrate uptake and, more important, phosphate and ammonium ion release into the medium at the end, which was ascribed to loss of viability. This was not observed for 2% CO2 immobilized bioreactor as well as shake flask control suspension cultures, which suggests that sparged C. roseus surface-immobilized cell cultures require 2% CO2 supplementation of the gas phase for both maximum growth and retained viability. The maximum CPRs of all cultures were in the same range (2.1-2.8 mM CO2 l-1 h-1). However, the estimated maximum specific CO2 production rates of 2% CO2 and 5% CO2 immobilized cultures (0.6 mM g dw-1 h-1) were lower than those found for air-sparged immobilized cultures (1.0-1.3 mM g dw-1 h-1). These rates are significantly higher than those reported in the literature for C. roseus cell suspension cultures performed in bioreactors gassed with air (approximately 0.2-0.55 mM g dw-1 h-1).     

Semicontinuous bioreactor production of a recombinant human therapeutic protein using a chemically inducible viral amplicon expression system in transgenic plant cell suspension cultures

Plant cell culture is an alternative for the production of recombinant human therapeutic proteins because of improved product safety, lower production cost, and capability for eukaryotic post‐translational modification. In this study, bioreactor production of recombinant human alpha‐1‐antitrypsin (rAAT) glycoprotein using a chemically inducible Cucumber mosaic virus (CMV) viral amplicon expression system in transgenic Nicotiana benthamiana cell culture is presented. Optimization of a chemically inducible plant cell culture requires evaluation of effects of timing of induction (TOI) and concentration of inducer (COI) on protein productivity and protein quality (biological functionality). To determine the optimal TOI, the oxygen uptake rate (OUR) of the plant cell culture was chosen as a physiological indicator for inducing maximum rAAT expression. Effects of COI on rAAT production were investigated using a semicontinuous culture, which enables the distinction between effects of growth rate and effects of inducer concentration. An optimized semicontinuous bioreactor operation was further proposed to maximize the recombinant protein production. The results demonstrated that the transgenic plant cells, transformed with the inducible viral amplicon expression system, maintain higher OUR and exhibit lower extracellular protease activity and lower total phenolics concentration in the optimized semicontinuous bioreactor process than in a traditional batch bioreactor operation, resulting in a 25‐fold increase in extracellular functional rAAT (603 µg/L) and a higher ratio of functional rAAT to total rAAT (85–90%). Surprisingly, sustained rAAT production and steady state, long‐term bioreactor operation is possible following chemical induction and establishment of the viral amplicons. Biotechnol. Bioeng. 2010; 106: 408–421. © 2010 Wiley Periodicals, Inc.     

Effects of immobilization by entrapment in alginate and scale-up on paclitaxel and baccatin III production in cell suspension cultures of Taxus baccata

Paclitaxel and baccatin III-producing cells of Taxus baccata were immobilized within Ca(2+)-alginate beads. Under established optimum conditions for the biosynthesis of both taxanes, the yields of paclitaxel and baccatin III in shake-flask cultures of free cells increased by factors of up to 3 and 2, respectively, in the corresponding cultures of immobilized cells. Although the scale-up from shake-flask to bioreactor culture usually results in reduced productivities when both free and immobilized cells were grown in the same optimum conditions in three different bioreactor types (Stirred, Airlift, and Wave) running for 24 days in a batch mode and with the system optimized in each case, there was a considerable increase in the yields of paclitaxel and baccatin III. Among the reactors, the Stirred bioreactor was the most efficient in promoting immobilized cell production of paclitaxel, giving a content of 43.43 mg.L(-1) at 16 days of culture, equivalent to a rate of 2.71 mg.L(-1).day(-1). To our knowledge, the paclitaxel productivity obtained in this study is one of the highest reported so far by academic laboratories for Taxus species cultures in bioreactors.     

Bioreactor culture of heterotrophic sandalwood (Santalum album L.) cell suspensions utilizing a cell-lift impeller

Summary Growth and phenolic production by two heterotrophic suspension cultures (SW-1 and SW-2) of sandalwood cultivated in a 2.5 L bioreactor were investigated. Cultures of SW-1 cell suspensions resulted in a maximum phenolic content of 32.5 mg L^–1 compared to 12.5 mg L^–1 produced by SW-2 cell suspensions. Fresh weight doubling time (Td) was 5.8 days and the specific growth rate () was 0.12 d^–1 during exponential growth for both cell lines. The pH of the culture medium decreased from 5.5 to 3.5 during the exponential growth phase of SW-1 and SW-2 cell suspensions. The dissolved oxygen content also dropped steadily during culture and remained at 40% throughout exponential growth phase. These results should provide a basis for developing sandalwood cell cultures for bioproduction of useful compounds.Abbreviations 2,4-D: 2–4 dichlorophenoxyacetic acid - BA N⁶-benzyladenine - Eh Medium oxidation-reduction potential - K_La Oxygen transfer coefficient - MS Murashige and Skoog (1962) basal medium - SW-1 and SW-2 Sandalwood suspension lines     

Bioreactor strategies for improving production yield and functionality of a recombinant human protein in transgenic tobacco cell cultures

Plant cell culture production of recombinant products offers a number of advantages over traditional eukaryotic expression systems, particularly if the product can be targeted to and purified from the cell culture broth. However, one of the main obstacles is product degradation by proteases that are produced during cell culture, and/or the loss of biological activity of secreted (extracellular) products as a result of alteration in the protein conformation. Because proteolysis activity and target protein stability can be significantly influenced by culture conditions, it is important to evaluate bioprocess conditions that minimize these effects. In this study, a bioreactor strategy using a protocol involving pH adjustment and medium exchange during plant cell culture is proposed for improving the production of functional recombinant alpha(1)-antitrypsin (rAAT), a human blood protein, produced using several alternative expression systems, including a Cauliflower mosaic virus (CaMV) 35S constitutive promoter expression system, a chemically inducible, estrogen receptor-based promoter (XVE) expression system, and a novel Cucumber mosaic virus (CMV) inducible viral amplicon (CMViva) expression system developed by our group. We have demonstrated that higher medium pH help reduce protease activity derived from cell cultures and improve the inherent stability of human AAT protein as well. This strategy resulted in a fourfold increase in the productivity of extracellular functional rAAT (100 microg/L) and a twofold increase in the ratio of functional rAAT to total rAAT (48%) in transgenic N. benthamiana cell cultures using a chemically inducible viral amplicon expression system.     

A high-rate perfusion bioreactor for plant cells

A perfusion bioreactor allowing continuous extraction of secondary metabolites was designed and challenged for Eschscholtzia californica plant cell suspensions. Four sedimentation columns mounted inside a 2.5-L bioreactor separated single cells and cell aggregates from the culture medium. Cells were elicited with chitin at day 4 and the liquid medium free of cells and debris was then continuously pumped to the extraction columns containing fluidized XAD-7 resins, and then recirculated back to the cell suspension. A medium upward velocity corresponding to cell sedimentation velocity maintained a stable cell/medium separation front in the columns for sedimented cell volume (SCV) of 90% (70% packed cell volume, PCV). Two perfusion bioreactor cultures of 10 and 14 days were performed. A maximum dilution rate of 20.4/day was reached from day 4 to day 6, and was then reduced to 5/day at day 9 for 55% SCV. Control cultures were performed without and with free extraction resins into the cell suspension. Perfusion cultures showed similar specific growth rates of 0.24 +/- 0.04/day before and after elicitation. However, production level in the perfusion cultures was similar to that from the culture without resins with a maximum of 2.06 micromole/gDW total alkaloids, with 1.54 micromole/gDW in the resins. Cultures with free resins resulted in 30.94 micromole/gDW with 28.4 +/- 8.8 micromole/gDW in the resins. Difference in the cells nutritional state from elicitation was identified as a major cause in the production reduction. However, pathway to chelilutine was favored in the continuous extraction culture.     

Growth kinetics of vitis vinifera cell suspension cultures: I. Shake flask cultures

Vitis vinifera cell suspension cultures carried out in shake flasks were closely examined for biomass growth and cell division in relation to carbohydrate, NH(4), NO(3)PO(4), and dissolved oxygen (DO)consumption. After inoculation, the oxygen uptake rate of the cultures measured on-tine was observed to increase continuously to a maximum value of 3.8 mmol O(2)L(-1)h(-1) at day 7 when cell division ceased and dissolved oxygen reached its lowest level of 17% air saturation. During this first phase of growth, the specific oxygen uptake rate remained constant at approximately 0.6 mmol 02 O(2) g(-1) dw h(-1)or approximately 2.2 mumol O(2), (10(6) cells)(-1) h(-1) whereas dry biomass concentration increased exponentially from 1.5 to 6.0 g dw L(-1). Thereafter, dry biomass concentration increased linearly to approximately 14 g dw L(-1) at day 14 following nitrate and carbohydrate uptake. During this second phase of growth, the biomass wet-to-dry weight ratio was found to increase in an inverse relationship with the estimated osmotic pressure of the culture medium. This corresponded to inflection points in the dry and wet biomass concentration and packed cell volume curves. Furthermore, growth and nutrient uptake results suggest that extracellular ammonium or phosphate ion availability may limit cell division. These findings indicate that cell division and biomass production of plant cell cultures may not always be completely associated, which suggests important new avenues to improve their productivity. (c) 1995 John Wiley & Sons, Inc.     

Trichloroethylene mineralization in a fixed-film bioreactor using a pure culture expressing constitutively toluene ortho -monooxygenase

An aerobic, single-pass, fixed-film bioreactor was designed for the continuous degradation and mineralization of gas-phase trichloroethylene (TCE). A pure culture of Burkholderia cepacia PR1(23)(TOM(23C)), a Tn5transposon mutant of B. cepacia G4 that constitutively expresses the TCE-degrading enzyme, toluene ortho-monooxygenase (TOM), was immobilized on sintered glass (SIRANtrade mark carriers) and activated carbon. The inert open-pore structures of the sintered glass and the strongly, TCE-absorbing activated carbon provide a large surface area for biofilm development (2-8 mg total cellular protein/mL carrier with glucose minimal medium that lacks chloride ions). At gas-phase TCE concentrations ranging from 0.04 to 2.42 mg/L of air and 0.1 L/min of air flow, initial maximum TCE degradation rates of 0.007-0.715 nmol/(min mg protein) (equivalent to 8.6-392.3 mg TCE/L of reactor/day) were obtained. Using chloride ion generation as the indicator of TCE mineralization, the bioreactor with activated carbon mineralized an average of 6.9-10.3 mg TCE/L of reactor/day at 0.242 mg/L TCE concentration with 0.1 L/min of air flow for 38-40 days. Although these rates of TCE degradation and mineralization are two- to 200-fold higher than reported values, TOM was inactivated in the sintered-glass bioreactor at a rate that increased with increasing TCE concentration (e.g., in approximately 2 days at 0.242 mg/L and <1 day at 2.42 mg/L), although the biofilter could be operated for longer periods at lower TCE concentrations. Using an oxygen probe and phenol as the substrate, the activity of TOM in the effluent cells of the bioreactor was monitored; the loss of TOM activity of the effluent cells corroborated the decrease in the TCE degradation and mineralization rates in the bioreactor. Repeated starving of the cells was found to restore TOM activity in the bioreactor with activated carbon and extended TCE mineralization by approximately 34%. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 674-685, 1997.     

Effects of oxygen on recombinant protein production by suspension cultures of Spodoptera frugiperda (Sf-9) insect cells.

Spodoptera frugiperda (Sf-9) insect cells have been grown in serum-free medium in 250-ml spinner flasks. The maximum cell density obtained in these cultures was dependent on the aeration rate of the culture. Similar yields of uninfected cells were obtained when cultures were stirred in spinner flasks at 80 rev min-1 and in a 4-1 stirred-tank bioreactor and the dissolved oxygen in the bioreactor was controlled at 20% of air saturation. Cells were infected with a recombinant baculovirus at different multiplicities of infection: the timing and maximum level of expression of the recombinant protein were dependent on the multiplicity of infection, the cell density at infection, and on the aeration rate of the culture. Oxygen-limited growth resulted in undetectable levels of recombinant protein (< 6 ng recombinant protein 10(-7) cells). Compared with the maximum yields observed in spinner flask cultures, higher levels of recombinant protein were produced when cells were grown and infected in the bioreactor. The level of dissolved oxygen in the bioreactor was controlled at 50% of air saturation.     

High Yield of Human Monoclonal Antibody Produced by Stably Transfected Drosophila Schneider 2 Cells in Perfusion Culture Using Wave Bioreactor

Since it was first introduced in late 1990s Wave bioreactor has been used for protein production by mammalian and insect cell lines. However, using Wave bioreactor to produce human monoclonal antibody by stable Drosophila Schneider 2 (S2) cell transfectants has not been reported before. In this study, S2 cells were co-transfected with an inducible vector expressing human monoclonal antibody heavy and light chains, respectively, specific for hemagglutinin (HA) of H5N1 influenza virus. Stable S2 transfectant clone was selected by limiting dilution assay. Stable S2 transfectant clone that produce the highest amount of human monoclonal antibody was inoculated into two 2-l disposable cellbags, where cell growth and antibody production were compared between batch and perfusion cultures using Wave bioreactor. Here, we report that maximum viable cell density reached 1.06?×?10(7) cells/ml in batch culture; whereas 1.04?×?10(8)?cells/ml was achieved in perfusion culture. The maximum volumetric antibody productivity in batch culture was 52?mg/l/day; while perfusion culture yielded 1,437?mg/l/day. As a result, the total antibody production was 201?mg in batch culture and 8,212?mg in perfusion culture. The antibody produced by both cultures displays full neutralizing activity. Thus, our results provide strong support for using Wave bioreactor in perfusion culture for a large-scale production of human monoclonal antibody by stable S2 cell transfectants.     

补料培养与溶氧控制联合应用对红豆杉细胞培养的影响

为进一步提高红豆杉 (Taxuschinensis (Pilg.)Rehd .)细胞培养过程中紫杉醇的产量 ,采用细胞悬浮培养方法研究了补料培养与溶氧控制联合应用对紫杉醇产量的影响。 5L反应器中补料培养研究表明 ,培养过程中第 16天添加含 2 0g/L蔗糖的补料培养液有利于细胞的生长及紫杉醇的合成。 2 0L反应器中补料培养的研究结果表明 :2 0 %饱和度培养时紫杉醇含量最高 (0 .98mg/gDW) ,但 4 0 %～ 6 0 %溶氧饱和度能提高紫杉醇的产量。进一步研究表明 ,细胞在 6 0 %溶氧饱和度培养 2 0d后转入 2 0 %溶氧饱和度继续培养 12d ,能显著提高紫杉醇产量。补料培养与溶氧控制联合应用时 ,2 0L反应器中红豆杉细胞培养紫杉醇产量可达 18.7mg/L。     

Ultrahigh diterpenoid tanshinone production through repeated osmotic stress and elicitor stimulation in fed-batch culture of <Emphasis Type="Italic">Salvia miltiorrhiza</Emphasis> hairy roots

Hyperosmotic stress (OS, created with 50 g/L sorbitol) and a yeast elicitor (YE, polysaccharide fraction of yeast extract) applied to Salvia miltiorrhiza hairy root cultures had a synergistic effect on the diterpenoid tanshinone production. With a single OS+YE treatment and nutrient feeding, the total tanshinone content of roots was increased by sevenfold (from 0.2 to 1.6 mg/g dry weight (dw)) and the volumetric yield by 13-fold (from 1.95 to 27.4 mg/L) compared to the batch control culture. With repeated feeding of OS and nutrient medium in an extended fed-batch culture process (i.e., 10 mL fresh medium with 50 g/L sorbitol 25 mg/L YE, every 5 days from day 21 to day 60), the total tanshinone content of roots was increased to 18.1 mg/g dw (or 1.8 wt.%) and the volumetric tanshinone yield to 145 mg/L, which were about 100-fold and 70-fold of those, respectively, in the batch control. Another interesting finding was the presence of root fragments (fine particles) with extremely high tanshinone content in the OS+YE treated cultures. It was also possible to reuse the sorbitol medium for the hairy root growth and tanshinone production to reduce the medium expenses.     

Production of functional human α1-antitrypsin by plant cell culture

Recombinant human α₁-antitrypsin (rAAT) was expressed and secreted from transgenic rice cell suspension cultures in its biologically active form. This was accomplished by transforming rice callus tissues with an expression vector, p3D-AAT, containing the cDNA for mature human AAT protein. Regulated expression and secretion of rAAT from this vector was achieved using the promoter, signal peptide, and terminator from a rice α-amylase gene Amy3D. The Amy3D gene of rice is tightly controlled by simple sugars such as sucrose. It was possible, therefore, to induce the expression of the rAAT by removing sucrose from the cultured media or by allowing the rice suspension cells to deplete sucrose catabolically. Although transgenic rice cell produced a heterogeneous population of the rAAT molecules, they had the same N-terminal amino acids as those found in serum-derived (native) AAT from humans. This result indicates that the rice signal peptidase recognizes and cleaves the novel sequence between the Amy3D signal peptide and the first amino acid of the mature human AAT. The highest molecular weight band seen on Western blots (AAT top band) was found to have the correct C-terminal amino acid sequence and normal elastase binding activity. Staining with biotin-concanavalin A and avidin horseradish peroxidase confirmed the glycosylation of the rAAT, albeit to a lesser extent than that observed with native AAT. The rAAT, purified by immunoaffinity chromatography, had the same association rate constant for porcine pancreatic elastase as the native AAT. Thermostability studies revealed that the rAAT and native AAT decayed at the same rate, suggesting that the rAAT is correctly folded. The productivity of rice suspension cells expressing rAAT was 4.6–5.7 mg/g dry cell. Taken together, these results support the use of rice cell culture as a promising new expression system for production of biologically active recombinant proteins. Received: 18 January 1999 / Received revision: 26 April 1999 / Accepted: 1 May 1999     

Scale‐up of Oldenlandia affinis suspension cultures in photobioreactors for cyclotide production

Cyclotides are a family of backbone‐cyclized cystine‐knot‐containing macrocyclic peptides from plants that possess extremely interesting biological activities. Suspension cultures of Oldenlandia affinis, a model plant containing cyclotides, were scaled‐up from shake flask to photobioreactor operation in order to produce these plant peptides under controlled conditions. Cell growth was highly dependent on inoculation culture; cell density as well as culture age had an effect on the growth rates and thus affected the kalata B1 productivity of the bioprocess. In a 25 l scale bioreactor the maximum doubling time was about 1.12 days compared to 2.24 days in shake flasks. The accumulation of kalata B1 of 0.09 mg g^?1 DW and 0.07–0.10 mg g^?1 DW respectively, however, was on a similar level during the corresponding stationary growth phases in both bioreactor and flask processes. An adjustment of cell culture growth via culture preparation and inoculum density to high cyclotide accumulation results in an estimated output during the most productive retardation phase of about 21 mg kalata B1 per day in the 25 l system. This makes the biotechnological cyclotide synthesis under GMP conditions a competitive production tool compared to field cultivation, chemical, and recombinant synthesis in drug discovery for structure analysis and bioactivity assays.     

Photolithotrophic cultivation of Laminaria saccharina gametophyte cells in a stirred-tank bioreactor

Filamentous cell cultures derived from female gametophytes of the temperate brown macroalga Laminaria saccharina were photolithotrophically cultivated in artificial seawater medium within an illuminated 1.3-L stirred-tank bioreactor at 13 degrees C using CO(2) in air as the carbon source. A Monod model adequately described light-saturated growth. The apparent half-saturation constant (K(o)) was 23 muE/m(2)-s, and maximum specific growth rate was 0.15 day(-1). At a constant inoculation cell density of 50 mg DCW/L, biomass productivity after 26 days of cultivation increased from 630 mg DCW/L at 18 muE/m(2)-s to 890 mg DCW/L at 228 muE/m(2)-s. At 98 muE/m(2)-s, 1.1 vvm aeration rate, and 250 rpm impeller speed, the CO(2) transfer rates (CO(2) TRs) and CO(2) consumption rates (r(co(2) )) were determined over the cultivation period. At peak CO(2) demand, the maximum CO(2) TR was 0.19 mmol CO(2)/L-h, but r(co(2) ) was only 0.15 mmol CO(2)/L-h, implying that the culture was not CO(2) transport limited. This is the first reported bioreactor cultivation study of cell cultures derived from a macrophytic marine alga. (c) 1995 John Wiley & Sons, Inc.