Microbial biosensors.

A microbial biosensor consists of a transducer in conjunction with immobilised viable or non-viable microbial cells. Non-viable cells obtained after permeabilisation or whole cells containing periplasmic enzymes have mostly been used as an economical substitute for enzymes. Viable cells make use of the respiratory and metabolic functions of the cell, the analyte to be monitored being either a substrate or an inhibitor of these processes. Bioluminescence-based microbial biosensors have also been developed using genetically engineered microorganisms constructed by fusing the lux gene with an inducible gene promoter for toxicity and bioavailability testing. In this review, some of the recent trends in microbial biosensors with reference to the advantages and limitations are been discussed. Some of the recent applications of microbial biosensors in environmental monitoring and for use in food, fermentation and allied fields have been reviewed. Prospective future microbial biosensor designs have also been identified.     

A fluidised bed vessel for the culture of immobilised plant cells and its application for the continuous production of fine cell suspensions

With the expansion of immobilised plant cell technology the need has arisen for a suitable vessel in which systems can be efficiently manipulated.Described is a vessel which incorporates many of the features of a fluidised bed, together with some of those from airlift technology to enable immobilised plant cells to be cultured at high biomass concentrations while maintaining a high mass transfer and controlled aeration under continuous flow conditions. In the case described, the vessel has been used for the continuous production of fine plant cell suspensions, although it is easily adaptable for use in cell mediated biotransformation or de novo synthesis studies.Abbreviations 2,4D 2.4 dichlorophenoxyacetic acid     

The role of cell immobilization in fermentation technology

The distinction between immobilized cell fermentation and immobilized cell biocatalysis is seldom made, though they are conceptually quite different. Unlike immobilized enzyme systems, immobilized viable cells can be used to carry out conventional fermentations. Microbial cells which would otherwise be freely dispersed (in almost colloidal suspension) within the fermentation environment can be encouraged to become attached in some way to a support (carrier), thus producing a discrete particulate solid phase. Such immobilization offers several potential advantages of a process engineering nature to the fermentation system. These include ease of handling and of cell separation, and lowering of bulk viscosity, as well as the obvious potential benefits of increased cell concentration.     

Comparison of fluidized bed and ultrasonic cell-retention systems for high cell density mammalian cell culture

Economically viable biopharmaceutical production is to a high degree dependent on high product yields and stable fermentation systems that are easy to handle. In the current study we have compared two different fermentation systems for the production of recombinant protein from CHO cells. Both systems are fully scaleable and can be used for industrial high cell density bioprocesses. As a model cell line we have used a recombinant CHO cell line producing the enzyme arylsulfatase B (ASB). CHO cells were cultivated as adherent cell culture attached on Cytoline macroporous microcarrier (Amersham Biosciences, Sweden) using a Cytopilot Mini fluidized bed bioreactor (FBR, Vogelbusch-Amersham Biosciences, Austria) and as suspension culture using a stirred tank bioreactor equipped with a BioSep ultrasonic resonator based cell separation device (Applikon, The Netherlands). Both systems are equally well-suited for stable, long-term high cell density perfusion cell culture and provide industrial scalability and high yields. For products such as the recombinant ASB, high perfusion rates and therefore short product bioreactor residence times may be of additional benefit.     

Bioreactor systems for in vitro production of foreign proteins using plant cell cultures

Plant cells have been demonstrated to be an attractive heterologous expression host (using whole plants and in vitro plant cell cultures) for foreign protein production in the past 20years. In recent years in vitro liquid cultures of plant cells in a fully contained bioreactor have become promising alternatives to traditional microbial fermentation and mammalian cell cultures as a foreign protein expression platform, due to the unique features of plant cells as a production host including product safety, cost-effective biomanufacturing, and the capacity for complex protein post-translational modifications. Heterologous proteins such as therapeutics, antibodies, vaccines and enzymes for pharmaceutical and industrial applications have been successfully expressed in plant cell culture-based bioreactor systems including suspended dedifferentiated plant cells, moss, and hairy roots, etc. In this article, the current status and emerging trends of plant cell culture for in vitro production of foreign proteins will be discussed with emphasis on the technological progress that has been made in plant cell culture bioreactor systems.     

A single cell model system to study hormone signal transduction

The model system presented here is based on immobilised single cells, derived directly from tobacco mesophyll protoplasts. It allows the adequate steering of cell populations towards expansion, cell cycling or cell resting. Using this approach cells always have the same predictable response to auxins and cytokinins whatever their actual physiological status. This model system opens new ways to study cellular parameters governing these hormone responses, some of which have been explored so far; a) the cytokinin response can equally well be induced by endogenous as by exogenous cytokinins; b) at least two intracellular components, microtubuli and the ER, adapt their architecture to the hormone-induced status of the cell; c) addition of NAA to the cells does not induce a change in the cytoplasmic pH.     

流式细胞术检测毕赤酵母发酵过程中胞内活性氧水平

以2′,7′-二氢二氯荧光黄双乙酸钠(DCFH-DA)和碘化丙锭(PI)为标记探针,通过DCFH-DA/PI双染色与PI单染色的对照,检测毕赤酵母胞内活性氧(reactive oxygen species,ROS)的水平及其影响。研究发现发酵过程细胞活性下降与胞内ROS积累相关。在甘油生长期,细胞几乎没有ROS积累,细胞活性接近100%。在甲醇诱导初期,部分细胞积累少量的ROS,细胞活性仍然很高,死亡细胞所占比例只有1.5%。在甲醇诱导后期,94.0%的细胞积累了大量的ROS,高含量的ROS造成细胞损伤,引起部分细胞丧失了活性,在总共29.1%的死亡细胞中,高ROS积累的死亡细胞占了25.4%。     

Cell immobilization: Application to alcohol production

The immobilization of whole cells is a technique that can be used in several production processes, among them alcoholic fermentation. By concentrating an active cell biomass in a bioreactor, the efficiency of bioconversion increases, as does the reactor productivity which, in turn, results in the reduction of the reactor size for a given production rate. Immobilization can be carried out in different ways; adsorption and entrapment in gelatinous matrices are the methods most commonly used. These techniques can be applied to practically all of the viable and non-viable whole cells systems of interest. Several reactor configurations are used sucessfully; many more have been proposed. Fermentor design imposes limitations on immobilization processes, requiring study of such aspects as mass-transfer, growth of cells in the reactor, aeration and backmixing.     

Responsive systems for cell sheet detachment

Cell sheet engineering has been progressing rapidly during the past few years and has emerged as a novel approach for cell based therapy. Cell sheet harvest technology enables fabrication of viable, transplantable cell sheets for various tissue engineering applications. Currently, the majority of cell sheet studies use thermo-responsive systems for cell sheet detachment. However, other responsive systems began showing their potentials for cell sheet harvest. This review provides an overview of current techniques in creating cell sheets using different types of responsive systems including thermo-responsive, electro-responsive, photo-responsive, pH-responsive and magnetic systems. Their mechanism, approach, as well as applications for cell detachment have been introduced. Further development of these responsive systems will allow efficient cell sheet harvesting and patterning of cells to reconstruct complex tissue for broad clinical applications.     

Malolactic fermentation in chardonnay wine by immobilised Lactobacillus casei cells

The kinetics of malolactic fermentation in Chardonnay wine by immobilised Lactobacillus casei cells has been studied. Calcium pectate gel and chemically modified chitosan beads were used as supports for immobilisation. Repeated batch fermentations were carried out with different wine samples, some of which were treated with sulfur dioxide (free 19–25 mg/litre and total 80–88 mg/litre), in shake flask at 36, 25 and 20°C without any loss of activity. The degradation of malic acid obtained using immobilised cells was twice as high as that obtained with free cells. At an initial pH 3·2, decrease of malic acid of about 30% was observed at 25°C in one hour using L. casei cells immobilised either in pectate gel or on chitosan. Among the physico-chemical parameters studied, temperature was the main factor affecting metabolism of the organic acids as well as the rate of the malolactic fermentation. Operational stability of calcium pectate gel beads and chemically modified chitosan beads was 6 months after eight fermentations and 2 months after five fermentations, respectively, which proved the possibility of industrial application of the chosen supports in wine making.     

Characterisation of the shrinkage of calcium alginate gel membrane with immobilised Lactobacillus rhamnosus

To quantify the shrinkage of calcium alginate gel membrane as a support matrix for immobilising cells during the fermentation of Lactobacillus rhamnosus, factors including time, pH, membrane thickness, and the concentrations of immobilised cells, lactic acid, glucose, and calcium chloride were examined by statistical experimental design. A Plackett-Burman design was used for the first screening experiment to identify the important factors which caused the divergent effects. Uniform Design, a powerful modelling design technique, was thus chosen to design the modelling experiments. Through a non-linear step-wise regression analysis, the predictive mathematical model of the shrinkage in membrane thickness was established and the significant main effects and two-factor interactions were identified. However, no significant model equations could be obtained for the shrinkage in area and volume of gel membranes. The methodology developed can be extrapolated to the quantitative characterisation of shrinkage in other immobilised gel matrices, which will be very useful in mathematical modelling, design, operation and scale-up of gel immobilised cell systems. Received: 8 November 1999 / Revision received: 17 January 2000 / Accepted: 23 January 2000     

Kinetic model for nitrogen-limited wine fermentations.

A physical and mathematical model for wine fermentation kinetics has been developed to predict sugar utilization curves based on experimental data from wine fermentations with various initial nitrogen and sugar concentrations in the juice. The model is based on: (1) yeast cell growth limited by nitrogen; (2) sugar utilization rates and ethanol production rates proportional solely to the number of viable cells; and (3) a death rate for cells proportional to alcohol content. All but one parameter in the model can be estimated from existing data. However, experiments to find this final parameter, a constant describing cell death, indicate that cell death may not be the critical factor in determining fermentation kinetics as cell viability remains significant until sugar utilization has ceased. The model, nevertheless, predicts a transition from normal to sluggish to stuck fermentations as initial nitrogen levels decrease. It also predicts that fermentations with high initial Brix levels may go to completion when supplemented with nitrogen in the form of ammonia. Therefore, we hypothesize that the model is valid but that ethanol causes the yeast cells to become inactive while remaining viable. Experimental verification of the model has been performed using flask-scale experiments. The model has also been used to evaluate the possibility of using nitrogen or viable cell additions to avoid or correct problem (i.e., sluggish or stuck) fermentations.     

Improving immobilized biocatalysts by gel phase polymerization

A new method is presented for the treatment of gel-type supports, used for immobilizing microbial cells and enzymes, to obtain high mechanical strength. It is particularly useful for ethanol fermentation over gel beads containing immobilized viable cells, where the beads can be ruptured by gas production and the growth of cells within the gels. This method consists of treating agar or carrageenan gel with polyacrylamide to form a rigid support which retains the high catalytic activity characteristic of the untreated biocatalysts. The size and shape of the biocatalyst is unaffected by this treatment. The method involves the diffusion of acrylamide, N,N'-methylenebisacrylamide and beta-dimethylaminopropionitrile (or N,N,N',N'-tetramethyl-ethylenediamine) into the performed biocatalyst beads followed by the addition of an initiator to cause polymerization within the beads. Treated gels have been used for the continuous fermentation of glucose to ethanol in a packed column for over two months. During this operation, the gel beads maintained their rigidity, and the maximum productivity was as high as 50 g h(-1) L(-1) gel. There was no appreciable decay of cell activity.     

Increasing batch-to-batch reproducibility of CHO cultures by robust open-loop control

In order to guarantee the quality of recombinant therapeutic proteins produced in mammalian cell systems, the straightforward approach in industry is to run the processes as reproducible as possible. It is first shown that considerable distortions in the currently operated processes appear when the initial cell density deviates from its nominal value. Small deviations in the initial cell mass may lead to severe deviations from the desired biomass trajectory. Next, it is shown how to design a fed-batch production process in such a way that it is robust with respect to variations in the viable cell density. A simple open loop strategy is proposed for that purpose. Here we show for the first time at animal cell cultures (CHO cells) that by means of an appropriate glutamine feed rate profile F(t), which keeps the specific growth rate of the cells on a predefined value below its maximal value while maintaining the viabilities on a high level, the diverging viable cell count profiles change over into a robust converging set of profiles. The CHO cells used to validate the procedure could be focused to any specific growth rates below μ_max.     

Inclined sedimentation for selective retention of viable hybridomas in a continuous suspension bioreactor.

The continuous separation of nonviable hybridoma cells from viable hybridoma cells by using a narrow rectangular channel that is inclined from the vertical has been investigated experimentally. The effectiveness of the settler in selectively retaining viable hybridomas in the bioreactor while permitting the removal of nonviable hybridomas has been shown to depend on the flow rate through the settler. Intermediate flow rates through the settler have been found to provide the highest removal of nonviable hybridomas relative to viable hybridoma retention. At high dilution rates through the chemostat, over 95% of the viable cells could be partitioned to the bottom of the settler while over 50% of the nonviable cells are removed through the top of the settler. This successful separation is due to the significantly larger size of the viable hybridomas than the nonviable ones. A continuous perfusion experiment was performed in which an external inclined settler was used to retain virtually all of the viable hybridomas in the culture, while selectively removing from the culture approximately 20% of the nonviable cells that entered the settler. A stable viable cell concentration of 1.0 x 10(7) cells/mL was achieved, as was an antibody productivity of over 50 micrograms/(mL.day). These represent 3- and 6-fold increases, respectively, over the values obtained from a chemostat culture without cell retention.     

Dielectrophoretic forces can be safely used to retain viable cells in perfusion cultures of animal cells

Dielectrophoresis is a well established and effective means for the manipulation of viable cells. However, its effectiveness greatly depends upon the utilization of very low electrical conductivity media. High conductivity media, as in the case of cell culture media, result only in the induction of weaker repulsive forces (negative dielectrophoresis) and excessive medium heating. A dielectrophoresis-based cell separation device (DEP-filter) has been recently developed for perfusion cultures that successfully overcomes these obstacles and provides a very high degree of viable cell separation while most of the nonviable cells are removed from the bioreactor by the effluent stream. The latter results in high viabilities throughout the culture period and minimization of lysed cell proteases in the bioreactor. However, an important question that remains to be answered is whether we have any adverse effects by exposing the cultured cells to high frequency electric fields for extended periods of time. A special chamber was constructed to quantitate the effect under several operational conditions. Cell growth, glucose uptake, lactate and monoclonal antibody production data suggest that there is no appreciable effect and hence, operation over long periods of time of the DEP-filter should not have any adverse effect on the cultured cells. This revised version was published online in July 2006 with corrections to the Cover Date.     

Production of ethanol by alginate-entrapped Saccharomyces cerevisiae strain "14-12"

Cells of S. cerevisiae strain "14-12" of different ages were immobilized in sodium alginate and used for conversion of glucose to ethanol. Immobilized cells of 48 hr old were the most potential. Employment of high counts of alginate-entrapped cells shortened the period required for production of the maximal alcohol yield. However, the percentage surviving cells decreased with increasing initial cell counts. Maximal accumulation of ethanol (4.18 g/100 ml) was obtained after 4 days of static fermentation with 1.8 X 10(8) immobilized yeast cells. The residual viable cell count was found to represent 3-fold the surviving percentage in a control experiment using an inoculum of the free yeast cells. Immobilized yeast cells could convert about 85% of the available sugars to ethanol over 28 days of the repeated-batch fermentation. The immobilized cells retained 50% of their viability for 16 days. After 48 days of repeated fermentation only 6% of the yeast cells were viable, and on the 52nd day no viable cells could be detected.     

Immobilized yeast cell systems for continuous fermentation applications

In several yeast-related industries, continuous fermentation systems offer important economical advantages in comparison with traditional systems. Fermentation rates are significantly improved, especially when continuous fermentation is combined with cell immobilization techniques to increase the yeast concentration in the fermentor. Hence the technique holds a great promise for the efficient production of fermented beverages, such as beer, wine and cider as well as bio-ethanol. However, there are some important pitfalls, and few industrial-scale continuous systems have been implemented. Here, we first review the various cell immobilization techniques and reactor setups. Then, the impact of immobilization on cell physiology and fermentation performance is discussed. In a last part, we focus on the practical use of continuous fermentation and cell immobilization systems for beer production.     

Use of a micro-expanded bed containing immobilised lysozyme for cell disruption in flow injection analysis

A method for cell disruption in Flow Injection Analysis (FIA) systems has been developed. The principle involves on-line cell disruption by means of immobilised lysozyme followed by an ultrasonic treatment. In order to avoid flow problems in the analytical system, the lysozyme was immobilised to Streamline^reg that was used in an expanded bed in the flow system. Samples of suspensions of Micrococcus lysodeikticus were treated and the success of the treatment was evaluated in terms of released protein and as a decrease in the optical density at 450 nm. The new technology offers a powerful tool in flow injection analyses for quantification of intracellular compounds. The concept of integration, i.e. combining cell disruption with handling of cell debris and assay procedure in one continuous flow process facilitates its use and increases the probability of reaching reproducible and reliable results.     

适于无血清贴壁培养的抗凋亡宿主细胞系CHO-IVB2的构建

应用无血清培养基培养CHO细胞时,由于没有血清提供各种贴壁因子,细胞以悬浮的方式生长。在实际的大规模细胞培养中,CHO细胞往往以贴壁方式培养,要么贴壁于悬浮的微载体中,要么贴壁于固定的聚酯盘状介质或中空纤维中,而很少直接悬浮于培养基中。在无血清培养基中,Vitronectin单一组分可以促使CHO细胞的贴壁和扩增。通过双表达lgf-1和Bcl-2基因,已经构建了可以在无蛋白培养基IMEM中抗凋亡生长的细胞株CHO-IB3。在此基础上,构建了可以同时表达Igf-1、Vitronectin和Bcl-2三个蛋白的三顺反子表达载体pCI—NII—IVB。将该载体转染于CHO—dhfr^-细胞中,构建了一个细胞株CHO—IVB2。该细胞株可以在无蛋白培养基中抗凋亡生长,适于以贴壁的方式大规模培养,用于大量生产外源目的蛋白。