Removal of nitrate from water by foam-immobilizedPhormidium laminosum in batch and continuous-flow bioreactors

Cells of the non-N₂-fixing cyanobacteriumPhormidium laminosum were immobilized in polyurethane (PU) foams either by absorption or by entrapment in the PU prepolymer followed by polymerisation and by adsorption onto polyvinyl (PV) foams. Although entrapment caused toxicity problems which lead to rapid death of the immobilized cells, they were immobilized successfully by adsorption onto PU or PV foams and maintained their photosynthetic electron transport activities (PS I, II, I + II) for at least 7 weeks. Changes in the morphology resulting from immobilization, as revealed by scanning electron microscopy (SEM) and low temperature-SEM, were investigated. Batch cultures and a continuous-flow packed bed photobioreactor were used to study nitrate removal from water. The effects of light intensity and CO₂ concentration on bioreactor performance were studied with respect to the nitrate uptake efficiency of the system. It was concluded thatP. laminosum immobilized on polymer foams is of potential value for biological nitrate removal in a continuous-flow system. author for correspondence     

A New Method For Axenic Mass Cultivation of Paramecium Tetraurelia*

SYNOPSIS A method is described for the axenic mass cultivation of Paramecium tetraurelia strains 51s and 299s. the ciliate is grown in an enriched axenic medium developed by Soldo, Godoy & van Wagtendonk. Under continuous shaking on a rotary shaker, cultures were grown in one-liter Erlenmeyer flasks with 330 ml medium yield cell densities of 32,000 cell/ml and 20,000 cells/ml for strains 299s and 51s respectively. Doubling time is considerably shorter under these conditions than in the conventional static cultures. A 20-liter airlift bioreactor is described in detail which can be used successfully to otain up to 100 g wet weight of Paramecium in a single run; in this reactor the cell density reaches 38,000 cells/ml for strain 299s. and 23,000 cells/ml for 51s. This technic should facilitate the study of minor protein components of the ciliate.     

Design of an efficient fermentation process for the production of Metarhizium acridum blastospores

Using a sequential approach, we described efficient blastospore production in a stirred tank bioreactor (3?L capacity). We used the response surface methodology to optimise the media ingredients and fermentation parameters to obtain the maximum production of blastospores by a locally collected isolate of Metarhizium acridum (Ascomycota: Hypocreales). The results showed that a liquid culture medium supplemented with monopotassium phosphate (15.17?g/L), corn steep liquor (69.25?g/L), and casamino acids (80.68?g/L) in a stirred tank bioreactor under operating conditions constant at 635?rpm, a temperature of 26°C, and pH 3.3 produced 1.25?×?10⁸?blastospores (bls)/ml, with 93% viability after 120?h of fermentation. This bioreactor yield compares favourably with the yields obtained by shake flask production and confirms the suitability of the media and production parameters for the potential scale-up fermentation production of M. acridum.     

Trends in application of gas-phase bioreactors

Gas-phase biological processes areeffective systems for treating air contaminatedwith biodegradable compounds. The greatestamount of experience with gas-phase processesexists with odor control and sulfide oxidation.Organic contaminant concentrations are limitedby oxygen transfer and clogging to values ofapproximately 1000 ppmv and loading rates ofapproximately 20 g/m³·h with empty bed contacttimes and air flux values of approximatelyone-minute and 1 m³/m²·min, respectively.Outlet contaminant concentrations attainableare generally near the non-detect level andnearly always below 50 ppbv. Very fewcontaminant concentration profiles have beenpublished and most performance and processresponse modeling has been based on in/outcontaminant values. Based on limited pilot andlaboratory scale profile data, it appears thatmany systems treating less soluble organics maybe fully or partially mass transport limited.The principal control problem in biofilters ismoisture content. Systems should be designedwith capacity to periodically add moisture tothe bed. In systems treating sulfides orchlorinated organics acid is produced and pHcontrol and corrosion can be problems. Cloggingdue to excess microbial growth results inincreased head loss, channelization, anddecreased performance. Initial head loss isusually less than 10 mm/m but increases as runtimes become extended. Typical of plug flowbiological processes, the highest removal ratesoccur near the inlet. Transient contaminantconcentration pulses tend to result in deeperpenetration into the bed where activity islower.     

Scalable production of adeno-associated virus type 2 vectors via suspension transfection

Vectors derived from adeno-associated virus type 2 (AAV2) are promising gene delivery vehicles, but it is still challenging to get the large number of recombinant adeno-associated virus (rAAV) particles required for large animal and clinical studies. Current transfection technology requires adherent cultures of HEK 293 cells that can only be expanded by preparing multiple culture plates. A single large-scale suspension culture could replace these multiple culture preparations, but there is currently no effective co-transfection scheme for generating rAAV from cells in suspension culture. Here, we weaned HEK 293 cells to suspension culture using hydrogel-coated six-well culture plates and established an efficient transfection strategy suitable for these cells. Then the cultures were gradually scaled up. We used linear polyethylenimine (PEI) to mediate transfection and obtained high transfection efficiencies ranging from 54% to 99%, thereby allowing efficient generation of rAAV vectors. Up to 10(13) rAAV particles and, more importantly, up to 10(11) infectious particles were generated from a 2-L bioreactor culture. The suspension-transfection strategy of this study facilitates the homogeneous preparation of rAAV at a large scale, and holds further potential as the basis for establishing a manufacturing process in a larger bioreactor.     

提高动物乳腺生物反应器表达水平的策略

在转基因动物乳腺生物反应器研究中,组织特异性表达水平、表达率和表达定位性是决定性的指标。因此,高效表达乳腺生物反应器的制备是许多研究者要实现的目标,也是走向产业化的基本要求。本文从基因构件、动物基因转移方面叙述了如何提高乳腺生物反应器表达水平、增强表达特异性及表达率,着重探讨如何提高动物乳腺生物反应器表达水平。     

β-TCP支架体外构建组织工程骨及其流体力学研究

骨髓基质干细胞在β-tricalciumphosphate(β-TCP)支架上分别进行了1、2和4周的三维动态培养,对支架上不同时间和部位的细胞面积/微孔面积及支架动态培养的流体环境进行了研究.研究表明,第1周细胞在支架大部分孔道内粘附生长并出现一定区域的单细胞层和多细胞层,第2周部分区域的部分孔道已填满了细胞并出现多细胞层,第4周大部分孔道几乎填满了细胞,主管道内壁出现了较多的细胞生长.同时发现,支架上各个区域细胞粘附面积不等,部分区域无细胞存在,有的部位2周后细胞逐渐减少.为了研究支架各个位置细胞増殖与流速、剪切应力的关系,建立了支架随机孔道结构的流体分析模型,通过支架上流速和剪切应力分布探讨实验中细胞分布现象的机理.结合计算和实验发现,流体能流到的部位几乎都有细胞生长,细胞生长较快的部位速度大多集中在0.24～0.53mm/s,剪切力大多在0.0050～0.023Pa,主管道底部及靠近进口的部位可能存在由于过大的剪切力影响细胞生长的区域.上述结果在一定程度上反映了细胞-支架-流体三者在成骨转化过程中的作用,对指导体外灌注培养的流量确定、灌注工艺及骨转化动力学研究有重要的意义.     

基因打靶方法制备乳腺生物反应器

基因打靶技术制备乳腺生物反应器,克服了显微注射法的众多缺陷,并随着第一例基因打靶家畜的诞生而成为这一研究领域的热点。本文从制备乳腺生物反应器过程中基因打靶策略、打靶细胞到打靶位点的选择等各个方面,详细分析了其中的技术难点、解决问题的对策、国内外研究进展以及应用前景。     

Sulfide oxidation at halo-alkaline conditions in a fed-batch bioreactor

A biotechnological process is described to remove hydrogen sulfide (H(2)S) from high-pressure natural gas and sour gases produced in the petrochemical industry. The process operates at halo-alkaline conditions and combines an aerobic sulfide-oxidizing reactor with an anaerobic sulfate (SO(4) (2-)) and thiosulfate (S(2)O(3) (2-)) reducing reactor. The feasibility of biological H(2)S oxidation at pH around 10 and total sodium concentration of 2 mol L(-1) was studied in gas-lift bioreactors, using halo-alkaliphilic sulfur-oxidizing bacteria (HA-SOB). Reactor operation at different oxygen to sulfide (O(2):H(2)S) supply ratios resulted in a stable low redox potential that was directly related with the polysulfide (S(x) (2-)) and total sulfide concentration in the bioreactor. Selectivity for SO(4) (2-) formation decreased with increasing S(x) (2-) and total sulfide concentrations. At total sulfide concentrations above 0.25 mmol L(-1), selectivity for SO(4) (2-) formation approached zero and the end products of H(2)S oxidation were elemental sulfur (S(0)) and S(2)O(3) (2-). Maximum selectivity for S(0) formation (83.3+/-0.7%) during stable reactor operation was obtained at a molar O(2):H(2)S supply ratio of 0.65. Under these conditions, intermediary S(x) (2-) plays a major role in the process. Instead of dissolved sulfide (HS(-)), S(x) (2-) seemed to be the most important electron donor for HA-SOB under S(0) producing conditions. In addition, abiotic oxidation of S(x) (2-) was the main cause of undesirable formation of S(2)O(3) (2-). The observed biomass growth yield under SO(4) (2-) producing conditions was 0.86 g N mol(-1) H(2)S. When selectivity for SO(4) (2-) formation was below 5%, almost no biomass growth was observed.