Enhanced shikonin production from Lithospermum erythrorhizon by in situ extraction and calcium alginate immobilization

Plant cell cultures of Lithospermum erythrorhizon were carried out to produce shikonin by in situ extraction and cell immobilization in calcium alginate bead in shake flask cultures. In situ product extraction and cell immobilization enhanced shikonin production and facilitated product recovery. In situ extraction by n-hexadecane and cell immobilization by calcium alginate gave higher specific shikonin productivities of 7.4 and 2.5 times, respectively, than those from the cultures of free cells without extraction. Simultaneous use of both techniques increased specific and volumetric productivities of shikonin 25- and 15-fold, respectively. In calcium alginate immobilized cell cultures, n-hexadecane addition at an early stage (before 15 days) was effective for shikonin production, and solvent addition after 15 days of the culture significantly reduced shikonin production. Higher numbers of plant cell immobilized bead inoculation did not increase shikonin production and sucrose consumption. Most of the produced shikonin was dissolved in the solvent layer.     

Production of anthraquinones by immobilized Frangula alnus Mill. plant cells in a four-phase air-lift bioreactor

 The production of anthraquinones by Frangula alnus Mill. plant cells was used as a model system to evaluate the performance of a liquid-liquid extractive product-recovery process. The shake flask experiments have shown higher production of anthraquinones in cell suspension and flask cultures of calcium-alginate-immobilized cells when silicone oil was incorporated into the medium, compared to a control without silicone oil. An external-loop air-lift bioreactor, developed and designed for the production and simultaneous extraction of extracellular plant cell products, was regarded as a four-phase system, with dispersed gas, non-aqueous solvent and calcium-alginate-immobilized plant cells in Murashige and Skoog medium. Continuous extraction of anthraquinones by silicone oil and n-hexadecane inside the bioreactor resulted in 10–30 times higher cell productivity, compared to that of immobilized cells in a flask. Based on the mixing pattern, immobilized biocatalyst extraparticle and intraparticle diffusional constraints and the kinetics of growth, substrate consumption and product formation, a mathematical model was developed to describe the time course of a batch plant cell culture. The model showed satisfactory agreement with four sets of shake flask experiments and three bioreactor production cycles. Received: 18 March 1994/Received revision: 20 September 1994/Accepted: 28 September 1994     

A novel alginate hollow fiber bioreactor process for cellular therapy applications

Gel‐matrix culture environments provide tissue engineering scaffolds and cues that guide cell differentiation. For many cellular therapy applications such as for the production of islet‐like clusters to treat Type 1 diabetes, the need for large‐scale production can be anticipated. The throughput of the commonly used nozzle‐based devices for cell encapsulation is limited by the rate of droplet formation to ～0.5 L/h. This work describes a novel process for larger‐scale batch immobilization of mammalian cells in alginate‐filled hollow fiber bioreactors (AHFBRs). A methodology was developed whereby (1) alginate obstruction of the intra‐capillary space medium flow was negligible, (2) extra‐capillary alginate gelling was complete and (3) 83 ± 4% of the cells seeded and immobilized were recovered from the bioreactor. Chinese hamster ovary (CHO) cells were used as a model aggregate‐forming cell line that grew from mostly single cells to pancreatic islet‐sized spheroids in 8 days of AHFBR culture. CHO cell growth and metabolic rates in the AHFBR were comparable to small‐scale alginate slab controls. Then, the process was applied successfully to the culture of primary neonatal pancreatic porcine cells, without significant differences in cell viability compared with slab controls. As expected, alginate‐immobilized culture in the AHFBR increased the insulin content of these cells compared with suspension culture. The AHFBR process could be refined by adding matrix components or adapted to other reversible gels and cell types, providing a practical means for gel‐matrix assisted cultures for cellular therapy. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

犬肾细胞MDCK无血清贴壁及单细胞悬浮培养

旨在挖掘用于鉴定金黄色葡萄球菌的高特异性靶点及其PCR检测引物。采用C++语言编程,以金黄色葡萄球菌Staphylococcus aureus MRSA 252基因组编码序列为对象,对2 656个可编码区进行分析,获得特异性靶点序列,并设计PCR扩增引物。对包括葡萄球菌属11个种及其他细菌属在内的共计137株细菌验证引物特异性,筛选获得9个DNA序列,并设计了4对引物。经验证2对引物的特异性较好,其中引物SA3的基因组DNA检测限为13.7 fg/μL,菌体检测限为9.25×102 CFU/mL。结果验证     

类弹性蛋白多肽的从头设计、非色谱纯化及盐效应

近年来,因病毒侵害人类每年都要蒙受巨大的经济损失和社会损失。犬肾细胞MDCK以其具有的培养容易、增殖快、流感病毒感染效率高等特点,成为适用于流感病毒疫苗生产的重要细胞系之一。以MDCK细胞为研究对象,在自制无血清培养基中成功实现了MDCK细胞从有血清培养到无血清培养的驯化;并通过单细胞悬浮培养驯化过程实现了MDCK细胞的无血清单细胞悬浮培养,获得了适于无血清单细胞悬浮生长的ssf-MDCK细胞株,无血清单细胞悬浮批培养最大活细胞密度可达3.81×106 cells/mL,最大比生长速率可达0.056 h?     

Production of molecular hydrogen with immobilized cells ofRhodospirillum rubrum

Summary Cells ofRhodospirillum rubrum have been immobilized in various gels and tested for photobiological hydrogen production. Agar proved to be the best immobilizing agent with respect to production rates as well as stability. Agar immobilized cells were also superior compared to liquid suspension cultures. Growth conditions of the cells prior to immobilization, e.g. cell age, light intensity or nutrient composition, were of primary importance for the activity in the later immobilized state. A reactor with agar immobilized cells has been operated successfully over 3000 h with a loss of the activity of about 60%. Mean rates for hydrogen production for immobilized cells in this work during the first 60 to 70 hours after immobilization were in the range of 18 to 34 μl H₂ mg⁻¹ d.w. h⁻¹ and thus by a factor of up to 2 higher than liquid cultures under the same conditions. Maximal rates of hydrogen production (57 μl H₂ ml⁻¹ immobilized cell suspension) were reached in agar gel beads with cells immobilized after 70 h growth in liquid culture in the light and a cell density of 1.0 mg ml⁻¹, 70 h after immobilization.     

Efficient production of celery embryos and plantlets released in culture of immobilized gel beads

Celery embryos and plantlets were found to be selectively released in a culture of immobilized Ca-alginate gel beads in which celery callus was entrapped under regeneration conditions. We studied the feasibility of use of this process for celery embryogenesis in an artificial seed system. The cells released from the gel beads were larger than those obtained in suspension culture. The optimal concentration of alginate gel for embryo and plantlet production was 2% for the immobilized cell culture. Considering the maintenance of the gel bead structure and detrimental effect of CaCl₂ on plantlet development, 5 mM CaCl₂ supplementation gave the best result in terms of the number of heart and torpedo embryos and plantlets. The ratio of the number of heart embryos, torpedo embryos and plantlets to total number of cells in the immobilized cell culture was higher than that in the suspension culture. Repeated batch culture with 5 mM CaCl₂ provided long-term (more than 154 d) embryo and plantlet production without gel beads disruption. Productivity of plantlets in the immobilized cell culture with 5 mM CaCl₂ was 2.2-fold as high as that in the suspension culture.     

The production of monoclonal antibody in growth-arrested hybridomas cultivated in suspension and immobilized modes.

The effects of the microenvironment and the nature of the limiting nutrient on culture viability and overall MAb productivity were explored using a hybridoma cell line which characteristically produces MAb in the stationary phase. A direct comparison was made of the changes in the metabolic profiles of suspension and PEG-alginate immobilized (0.8 mm beads) batch cultures upon entry into the stationary phase. The shifts in glucose, glutamine, and amino acid metabolism upon entry into the stationary phase were similar for both microenvironments. While the utilization of most nutrients in the stationary phase decreased to below 20% of that in the growth phase, antibody production was not dramatically affected. The immobilized culture did exhibit a 1.5-fold increase in the specific antibody rate over the suspension culture in both the growth and stationary phases. The role of limiting nutrient on MAb production and cell viability was assessed by artificially depleting a specific nutrient to 1% of its control concentration. An exponentially growing population of HB121 cells exposed to these various depletions responded with dramatically different viability profiles and MAb production kinetics. All depletions resulted in growth-arrested cultures and nongrowth-associated MAb production. Depletions in energy sources (glucose, glutamine) or essential amino acids (isoleucine) resulted in either poor viability or low antibody productivity. A phosphate or serum depletion maintained antibody production over at least a six day period with each resulting in a 3-fold higher antibody production rate than in growing batch cultures. These results were translated to a high-density perfusion culture of immobilized cells in the growth-arrested state with continued MAb expression for 20 days at a specific rate equal to that observed in the phosphate- and serum-depleted batch cultures.     

In situ extraction strategy affects benzophenanthridine alkaloid production fluxes in suspension cultures of Eschscholtzia californica

The effect of contact between cells and extractive phase on secondary metabolite production was investigated in two-phase suspension cultures of Eschscholtzia californica. A system was designed to extract benzophenanthridine alkaloids from the cell culture, without contact between XAD-7 resins and the cells: only medium was recirculated through a column packed with the extractive phase. This strategy was compared to the classic method of addition of resins directly into the cell suspension. Removal of the product directly from the medium enabled important increases in production of alkaloids, namely a 20-fold increase in sanguinarine production and a 10-fold increase in chelerythrine, with high recovery in the resin. The recirculation strategy greatly simplified the production process since the resins are easily recovered from the cell culture and enable harvest of product without termination of culture. However, due to limited flow rate, the recirculation strategy was slightly less effective than direct addition of resins into the cell suspension. In addition to enabling increased production, removal of secondary metabolites from the medium changed metabolic flux distribution, testifying to a complex control mechanism of production.     

Enhanced taxol production and release in Taxus chinensis cell suspension cultures with selected organic solvents and sucrose feeding

Suspension culture of Taxus chinensis cells was carried out in aqueous-organic two-phase systems for the production and in situ solvent extraction of taxol (paclitaxel). Three organic solvents, hexadecane, decanol, and dibutylphthalate, were tested at 5-20% (v/v) in the culture liquid. All of these solvents stimulated taxol release and the yield per cell, though decanol and higher concentrations of the other two solvents depressed biomass growth significantly. Ten percent dibutylphthalate was the optimal solvent for improving taxol production and release with minimal cell growth inhibition. The time of solvent addition to the culture also affected taxol production, with the addition during the late-log growth phase being most favorable. By feeding sucrose to the culture near the stationary growth phase, the cell growth and taxol production period was extended from 27 to 42 days. The combining of the two-phase culture and sucrose feeding increased the taxol yield by about 6-fold compared with the single-phase batch culture, to 36.0 +/- 3.5 mg/L, with up to 63% taxol released. This study shows that in situ solvent extraction combined with nutrient feeding is an effective process strategy for production and recovery of secondary metabolites in plant cell suspension culture.     

High density culture of hybridoma cells in a dual hollow fiber bioreactor

Summary Hybridoma cells were cultured for two months in the dual hollow fiber bioreactor (DHFBR) which had been successfully used for high cell density cultures of various microbial cells. In batch suspension culture the concentration of monoclonal antibody (Mab) against human Chorionic Gonadotropin (hCG) and the cell density of Alps 25-3 hybridoma cells were obtained in 30 μg/mL and 2.35×10⁶ cells/mL, respectively. The continuous culture with DHFBR produced Mab of 100–130 μg/mL for 30 days and the estimated cell density in the extracapillary space of DHFBR was 1.87×10⁸ cells/mL based on the antibody production rate. The productivity of Mab was 205 mg/day per litre of the total reactor volume while that of the batch suspension culture was only 10 mg/L day.     

Influence of surface characteristics of cellulose carriers on ethanol production by immobilized yeast cells

Ethanol production was carried out by growing yeast cells immobilized on porous cellulose carriers. The effects of the chemical modification of cellulose carriers on cell immobilization and ethanol production were examined with respect to ion-exchange capacity and chemical structure. The ion-exchange capacity of 0·1 meq/g-carriers had no effect on immobilization but affected ethanol production by repeated batch cultures using immobilized yeast cells. Diethylaminoethyl was a suitable function group for immobilization and ethanol production. Ethanol productivity of the 10th batch cycle with diethylaminoethyl cellulose carriers was 23% greater than that of the first batch cycle.     

In situ pH maintenance for mammalian cell cultures in shake flasks and tissue culture flasks

pH in animal cell cultures decreases due to production of metabolites like lactate. pH control via measurement and base addition is not easily possible in small‐scale culture formats like tissue‐culture flasks and shake flasks. A hydrogel‐based system is reported for in situ pH maintenance without pH measurement in such formats, and is demonstrated to maintain pH between 6.8 and 7.2 for a suspension CHO cell line in CD CHO medium and between 7.3 and 7.5 for adherent A549 cells in DMEM:F12 containing 10% FBS. This system for pH maintenance, along with our previous report of hydrogels for controlled nutrient delivery in shake flasks can allow shake flasks to better mimic bioreactor‐based fed batch operation for initial screening during cell line and process development for recombinant protein production in mammalian cells. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 2012     

Immobilization of Rubia tinctorum L. suspension cultures and its effects on alizarin and purpurin accumulation and biomass production

The present study is investigating the immobilization of Rubia tinctorum L. suspension cultures. The effects of three inoculation volumes and three immobilization materials (loofa, sisal and jute) on fresh and dry weights of biomass as well as on alizarin and purpurin production were determined in this study. Two grams of four-week old callus tissue were transferred to liquid medium to establish suspension cultures. After four weeks, suspension cultures of R. tinctorum at concentration of 8?×?10⁵?living cells/ml were immobilized with lignocellulosic materials and the cells were attached to all immobilization materials at the end of the first week and started to form aggregates on them. At the fourth week of these batch systems, biomass was measured approximately three times higher than the starting suspension cultures. The highest fresh weight was obtained (339.40?g/l) from sisal with ? inoculation ratio. Immobilization materials and inoculation volumes had an effect on dry weights, and accordingly, the most effective combinations were jute with ? (J3) and ? (J1) inoculation volumes with 7.86 and 7.82?g/l dry weights, respectively. Alizarin and purpurin contents of immobilized cells, analyzed with U-HPLC method, were 6.05 and 22.91 times higher than inoculated cells. All immobilization materials used in this study had no negative effect on to cells and biomass accumulation was enhanced. Concomitantly with rapid biomass increase, alizarin and purpurin production was ascended.     

Plant cell bioreactor for the production of protoberberine alkaloids from immobilized Thalictrum rugosum cultures

Cultured Thalictrum rugosum cells were immobilized using a glass fiber substratum previously shown to provide optimum immobilization efficiency based on spontaneous adhesion mechanisms. When cultivated in shake flasks, immobilized cells exhibited decreased growth and protoberberine alkaloid production rates in comparison to freely suspended cells. Since alkaloid production is growth associated in T. rugosum, the decreased specific production rate was a function of the slower growth rate. Cells immobilized on glass fiber mats appear to be amenable for extended culture periods. Maximum biomass and protoberberine alkaloid levels were maintained for at least 14 days in immobilized cultures. In contrast, fresh weight, dry weight, and total alkaloid content decreased in suspension cultures following the linear growth phase.Glass fiber mats were incorporated in to a 4.5-L plant cell bioreactor as horizontal disks supported on a central rod. Mixing in the reactor was provided by the combined actions of a magnetic impeller and a cylindrical sparging colum. fThe magnetic impeller and a cylindrical sparging column. The entire inoculum biomass of T. rougosum, introduced as suspension, was spontaneously immobilized with in 8h. During liner phase, the growth rate of bioreactor cultivated immobilized cells (mu = 0.06 day(-1)) was 50% that immobilized cell viability in both systems was determined to be similar. The increase in specific production of protoberberine alklodis was initially similar in bioreactor-and culture period. The increase in specific production of protoberberine alkaloids was initially similar in bioreactor-and shake-flask-cultivated immobilized cells. However, the maximum specific production of bioreactor grown cultures was lower. The scale up potential of an immobilization strategy based on the spontaneous adhesion of immobilization strategy based on the spontaneous adhesion of cultured plant cells to glass fiber is demonstrated.     

Stimulation of ajmalicine production and excretion from Catharanthus roseus: effects of adsorption in situ,elicitors and alginate immobilization

Summary More efficient bioreactors for the production and recovery of secondary metabolites from plant cell cultures are needed. Three factors that have the potential to increase productivity are adsorption in situ, elicitors, and cell immobilization. The effects of these factors on ajmalicine production from Catharanthus roseus are reported in this paper. Elicitation using autoclaved cultures of the mold, Phytophthora cactorum, stimulates a 60% increase in ajmalicine production. The response time to elicitor addition was under 11 h. Adsorption of ajmalicine from the extracellular medium with the neutral resin, Amberlite XAD-7, greatly enhanced the release of ajmalicine (less than 10% extracellular to 40%) with a 40% increase in total productivity. Immobilization in Caalginate beads resulted in a significant increase in the accumulation of ajmalicine in the medium. The effects of elicitation, adsorption and immobilization were synergistic. For a 23-day culture period the amount of ajmalicine in the medium for cells subjected to all three treatments was 90 mg/L compared to 2 mg/L for suspension cultures cultured under otherwise identical conditions. These results suggest that immobilized cell bioreactors may be feasible for continuous production of products normally stored intracellularly in vacuoles in plant cells.     

Safety and economic aspects of continuous mammalian cell culture.

Mammalian cell cultures are the most appropriate host cells for recombinant DNA derived products if complex protein structures have to be synthesized in their native form. Due to their physiological behaviour they grow either adherent or in suspension. For the attachment of adherent cells, microcarriers or wire springs can be applied to increase the internal surface of the bioreactor. Both systems provide a simplified media exchange but, however, show some limitations in scale up. In contrast, suspension culture systems as homogeneous systems independent of any carrier have not shown any limitation in scale up. Because most cell lines which are of commercial interest grow in suspension, this technology is best advanced and used in batch and continuous mode. Although mammalian cell cultures are sensitive to hydrodynamic shear forces, technologies for deep tank production are developed which allow stirrer tip speed of up to 1.5 m s-1 sufficient for oxygen uptake, suspension of cells and homogeneous supply with nutrients. For long term bioprocesses without selection pressure it has to be considered that transformed cell lines might show genetic instability due to their variations of chromosomes. In addition, sterile technology becomes an important factor in long term bioprocesses. The decision as to which cell culture system should be chosen, whether batch or continuous processes should be applied essentially is based on the capital investment, the amount of material to be produced, genetic stability of the production cell line, reliability of sterile technology and the flexibility required in the production plant. Under the assumption that 20 kg of a protein have to be produced per year and the same product concentrations in the harvest fluid are reached in the batch process and for instance in the chemostat, it can be considered that the capital investment for one 10,000 l batch process and a 2 x 2,000 l continuous process, necessary to produce the amount of material, is comparable. Risk of microbial contamination or technical failure can be considered to be fairly low in the batch process. The economic risk for long term bioprocess in the chemostat can be expected to be medium and high in the perfusion system which is in the large scale not technically fully satisfactory. In addition, due to the longer down time period after contaminations and the start up of the continuous process, the annual yield of the batch process can be considered to be higher.(ABSTRACT TRUNCATED AT 400 WORDS)     

Immobilization of animal cells using photo-crosslinkable resin

A photo-crosslinkable resin, BIX12, was selected from among various photo-crosslinkable resins for the immobilization of animal cells. BIX12 had no cytotoxic effect on the growth of hybridoma cells and the production of monoclonal antibody, although other photo-crosslinkable resins had significant inhibitory effects. Using BIX12-alginate hybrid gel particles, hybridoma cells could grow in the resins and produce monoclonal antibody. For the continuous production of monoclonal antibody, perfusion culture using a fluidized-bed bioreactor with direct air bubbling was carried out. By this cultivation, monoclonal antibody could be produced stably for more than 50 d. A high viable cell density of more than 10⁷ cells/ml-gel was attained, and the antibody productivity was improved 8.5-fold compared with conventional suspension culture using a spinner flask. Anchorage-dependent cells were also immobilized in the resin particles by three immobilization procedures. Among these procedures, porous BIX12 formed by adding gelatin powder provided good support strength and allowed the cells to grow on the surface inside of the support.     

制备可溶性肿瘤坏死因子受体II－脂联素球部融合蛋白的两种细胞培养工艺比较

利用7.5 L生物反应器篮式贴壁培养和全悬浮批式培养CHO工程细胞株表达可溶性肿瘤坏死因子受体Ⅱ-脂联素球部(sTNFRⅡ-gAD)融合蛋白,比较这两种培养方法的产率,以便优化高效表达sTNFRⅡ-gAD融合蛋白的制备工艺.篮式贴壁培养首先小规模培养CHO工程细胞株,待细胞增殖到一定密度后以3× 105～4× 105 cells/mL密度接种生物反应器贴壁培养3d,调换成不含血清的LK021培养基继续培养4d.而全悬浮无血清批式培养则以3×105～4×105 cells/mL密度的CHO工程细胞株接种于生物反应器,连续培养7d.培养过程实时监测培养条件,维持pH和DO的稳定.分别收集细胞上清,离心去细胞后用Pellicon切相流超滤系统对蛋白进行浓缩,并通过DEAE离子交换柱进行纯化.结果显示,篮式贴壁培养和全悬浮批式培养均成功表达了sTNFRⅡ-gAD融合蛋白,产量分别为8.0 mg/L和7.5 mg/L、纯度分别为95％和98％,从而为sTNFRⅡ-gAD融合蛋白的中试工艺研究提供了一定的基础.     

Low-glutamine fed-batch cultures of 293-HEK serum-free suspension cells for adenovirus production

Recent developments in gene therapy using adenoviral (Ad) vectors have fueled renewed interest in the 293 human embryonic kidney cell line traditionally used to produce these vectors. Low-glutamine fed-batch cultures of serum-free, suspension cells in a 5-L bioreactor were conducted. Our aim was to tighten the control on glutamine metabolism and hence reduce ammonia and lactate accumulation. Online direct measurement of glutamine was effected via a continuous cell-exclusion system that allows for aseptic, cell-free sampling of the culture broth. A feedback control algorithm was used to maintain the glutamine concentration at a level as low as 0.1 mM with a concentrated glucose-free feed medium. This was tested in two media: a commercial formulation (SFM II) and a chemically defined DMEM/F12 formulation. The fed-batch and batch cultures were started at the same glucose concentration, and it was not controlled at any point in the fed-batch cultures. In all cases, fed-batch cultures with double the cell density and extended viable culture time compared to the batch cultures were achieved. An infection study on the high density fed-batch culture using adenovirus-green fluorescent protein (Ad-GFP) construct was also done to ascertain the production capacity of the culture. Virus titers from the infected fed-batch culture showed that there is an approximately 10-fold improvement over a batch infection culture. The results have shown that the control of glutamine at low levels in cultures is sufficient to yield significant improvements in both cell densities and viral production. The applicability of this fed-batch system to cultures in different media and also infected cultures suggests its potential for application to generic mammalian cell cultures.