Extraction of plasmid DNA using reactor scale alkaline lysis and selective precipitation for scalable transient transfection

DNA extracted and purified for vaccination, gene therapy or transfection of cultured cells has to meet different criteria. We describe herein, a scalable process for the primary extraction of plasmid DNA suitable for transient expression of recombinant protein. We focus on the scale up of alkaline lysis for the extraction of plasmid DNA from Escherichia coli, and use a simple stirred tank reactor system to achieve this. By adding a series of three precipitations (including a selective precipitation step with ammonium acetate) we enrich very quickly the plasmid DNA content in the extract. The process has been thus far used to extract up to 100 mg of plasmid from 1.5 l of clarified lysate, corresponding to an E.coli bioreactor fermentation of 3 l. This revised version was published online in July 2006 with corrections to the Cover Date.     

A continuous cell alkaline lysis, neutralization, and clarification combination process for production of plasmid pUDK-HGF

Plasmid DNA for biopharmaceutical applications is produced easily in Escherichia coli bacteria. The cell lysis is the most crucial step for purification of plasmid DNA. In this paper, we describe a continuous cell alkaline lysis, neutralization, and clarification combination process for production of plasmid pUDK-HGF using hollow fiber ultrafiltration column as a lysis chamber and compare the plasmid DNA yield and homogeneity with the T-connector and manual processes, respectively. The results show that the plasmid pUDK-HGF yield of the combination process is 13% higher than manual lysis, twice higher than using T-connector. When the proportion of lysed cells and neutralization solution is 3:1, the plasmid pUDK-HGF yield can improve by 70%. This process could be easily scaled up to meet the industrial scale for cell lysis.     

Expression and purification of cGMP grade NY-ESO-1 for clinical trials

NY-ESO-1 is a cancer testis antigen expressed in numerous cancers. Initial tests have shown its efficacy as a cancer vaccine, stimulating the body's own immune response against the invading tumor. To produce enough material for phase I clinical trials, a process using current good manufacturing practices to produce clinical grade material was developed and executed. His-tagged NY-ESO-1 was expressed in C41DE3 Escherichia coli under control of the T-7 promoter. NY-ESO-1 was produced in a 20 L fed-batch fermentation utilizing a pH-stat control scheme. The protein was then purified from inclusion bodies using a three-column process that achieved a yield of over 3.4 g and endotoxin below the detection limit of 0.005 EU/μg protein.     

Enhanced production of exopolysaccharides using industrial grade starch as sole carbon source

Bioprocess and Biosystems Engineering - Industrial grade soluble corn starch was used directly and effectively as the fermentation substrate for microbial exopolysaccharides production. Bacillus...     

饲用复合益生菌粉剂工业化生产技术研究

目的 建立饲用枯草芽孢杆菌-嗜酸乳杆菌-酿酒酵母复合益生菌粉剂工业化生产线.方法 采用液-固态二步发酵法扩增益生菌,采用低温抽湿法干燥益生菌,采用GMP规范控制杂菌污染.结果 确立了饲用复合益生菌粉剂规模化、连续化、标准化生产工艺流程、设备设施和技术参数.结论 本研究为饲用复合益生菌粉剂工业化生产提供了重要的数据、方法、规程和示范.     

碱裂解提取质粒DNA的改进

碱裂解提取质粒DNA是分子生物学实验中常用的方法,但通常方法所提取的质粒往往含有大量的RNA和其他杂质.本文适时加入较高浓度的RNA酶和适当延长冰浴时间,结果得到了几乎没有RNA和其他杂质的高纯质粒DNA,不仅达到了分子生物学实验要求,而且可用作抗原检测抗dsDNA抗体.该法操作简单、经济、实用.     

Bioprocess development for kefiran production by Lactobacillus kefiranofaciens in semi industrial scale bioreactor

Lactobacillus kefiranofaciens is non-pathogenic gram positive bacteria isolated from kefir grains and able to produce extracellular exopolysaccharides named kefiran. This polysaccharide contains approximately equal amounts of glucose and galactose. Kefiran has wide applications in pharmaceutical industries. Therefore, an approach has been extensively studied to increase kefiran production for pharmaceutical application in industrial scale. The present work aims to maximize kefiran production through the optimization of medium composition and production in semi industrial scale bioreactor. The composition of the optimal medium for kefiran production contained sucrose, yeast extract and K₂HPO₄ at 20.0, 6.0, 0.25 g L⁻¹, respectively. The optimized medium significantly increased both cell growth and kefiran production by about 170.56% and 58.02%, respectively, in comparison with the unoptimized medium. Furthermore, the kinetics of cell growth and kefiran production in batch culture of L. kefiranofaciens was investigated under un-controlled pH conditions in 16-L scale bioreactor. The maximal cell mass in bioreactor culture reached 2.76 g L⁻¹ concomitant with kefiran production of 1.91 g L⁻¹.     

An improved alkaline lysis method for minipreparation of plasmid DNA

This study is to improve the digestion pattern of miniprepped plasmid analyzed on gel. Frequently, some ambiguous DNA bands, which are suspected to be denatured DNA molecules, appear during electrophoresis of enzyme digested miniprepped plasmids. By employing Southern hybridization of two identical gels, one had been treated with denaturation-neutralization step and another without such treatment, we confirmed that many of these ambiguous DNA bands were single-stranded (SS) DNA molecules. The presence of SS DNA was due to the use of excess amount of NaOH during plasmid DNA purification with the conventional alkaline lysis method. We, therefore, modified the procedure and recommend that a half amount of NaOH (0.1N instead of 0.2N) should be used when isolating small quantity of plasmid DNA with the method.     

Proposal for a better integration of bacterial lysis into the production of plasmid DNA at large scale

The paper addresses the question of how to achieve bacterial lysis in large-scale plasmid DNA production processes, where conventional alkaline lysis may become awkward to handle. Bacteria were grown in shaker flasks and a bioreactor. Suboptimal growth conditions were found advantageous for stable plasmid production at high copy numbers (up to 25mg/L could be achieved). Cells were harvested by filtration in the presence of a filter aid. A linear relationship between the biomass and the optimal filter aid concentration in terms of back pressure could be established. Bacteria-containing filter cakes were washed with isotonic buffer and lysis was achieved in situ by a two-step protocol calling for fragilisation of the cells followed by heat lysis in a suitable buffer. RNA and other soluble cell components where washed out of the cake during this step, while the plasmid DNA was retained. Afterwards a clear lysate containing relatively pure plasmid DNA could be eluted from the cake mostly as the desired supercoiled topoisomer, while cell debris and genomic DNA were retained. Lysis is, thus, integrated not only with cell capture but also with a significant degree of isolation/purification, as most impurities were considerably reduced during the procedure.     

Continuous ethanol production by zymomonas mobilis on an industrial scale

The specific growth rate of the ethanol producing bacterium Zymomonas mobilis was lower in the presence of oxygen than under anaerobic conditions. Aerobically, considerable amounts of acetaldehyde and acetic acid were formed in addition to the normal fermentation products, ethanol and carbon dioxide. This bacterium contains considerable amounts of pentacyclic triterpenoids, mainly 1, 2, 3, 4-tetrahydroxypentane-29-hopane. It seems that stability and permeability of the cytoplasmic membrane of this rather ethanol tolerant organism is achieved by the hopanoid content. A continuous culture of Zymomonas mobilis produced 60 g/l ethanol over a test period of 39 days. This strain was used for ethanol production from an enzymatically hydrolyzed wheat starch fraction on an industrial scale of 100 m³.     

Production and separation of dipeptidyl peptidase IV from Lactococcus lactis: scale up for industrial production

Lactococcus lactis spp. lactis and Lactococcus lactis spp. cremoris are widely used in the manufacture of fermented milk. These strains were compared for production of Dipeptidyl Peptidase IV (DPP IV) enzyme in terms of enzyme activity, specific growth rates and productivity. Lactococcus lactis spp. lactis was produced in 3?L bioreactor and scaled up to 30 and 150?L stirred tank bioreactors, and the enzyme activities were found as 110, 110 and 122?mU?mL(-1), respectively. After 8?h of production, separation steps were performed. While purification fold was 127 and yield was 2.69?%, the molecular weight of the enzyme was estimated as 68?kDa. Partially purified enzyme was enteric coated with capsules and a 95.5?% of DPP IV enzyme passed into the artificial intestine. Results show that production of DPP IV enzyme by Lactococcus lactis spp. lactis strain in submerged culture is comparable with the productions by commercial strains, mostly Aspergillus, in solid state fermentations based on productivity.     

Synthetic biology advances for pharmaceutical production

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Environmental evaluation and comparison of selected industrial scale biomethane production facilities across Europe

Purpose

The two main reasons for producing biomethane as renewable fuel are reduction of climate impacts and depletion of fossil resources. Biomethane is expected to be sustainable, but how sustainable is it actually? This article contributes to the clarification. Therefore, the environmental impacts of several biomethane facilities all over Europe were assessed. A special focus is put on the differences between the facilities as they follow different production routes.

Methods

The method used for evaluation is life cycle assessment (LCA) applied in a well-to-wheel approach. This enables to show the overall performance in terms of global warming potential (GWP), acidification potential (AP), eutrophication potential (EP), photochemical ozone creation potential (POCP) and PE fossil. The system boundary includes the entire chain from biogas production to upgrading, distribution and use. For evaluating the different production routes several years of measuring data, calculating and improving the LCA models in close cooperation with the plant operators were carried out.

Results and discussion

The evaluation of the production routes shows a high reduction potential compared to fossil fuels. Regarding the depletion of fossil resources, the amounts vary between the sites, but the reduction is at least 50 % and reaches almost 100 % reductions at some sites. The reduction of GWP is at least 65 %, because waste flows free of environmental burdens are used almost exclusively as substrate. Other dominant factors are power and heat demand, methane losses to the environment and the use of by-products, e.g. fertilizer.

Conclusions

Despite this caveat, the evaluated systems demonstrate the possible positive results of renewable fuel production if done properly.     

Automated production support for the bioprocess industry

This paper describes the application of Artificial Intelligence and Multivariate Statistical Techniques to two industrial fermentation systems. In the first example, an Expert System is shown to provide tighter control of an important process parameter. This is shown to lead to improved consistency of operation. In the second application, Principal Component Analysis is applied to a final stage fermentation production facility. The results presented indicate that the algorithm can provide concise indicators of process faults that can be presented to the operators to assist them in taking suitable corrective actions.     

Reverse micellar extraction systems for the purification of pharmaceutical grade plasmid DNA

Plasmid DNA as an active pharmaceutical ingredient (API) is gaining more and more importance. For the production of multigram quantities of this substance robust and scalable processes comprising several purification steps have to be designed. One main challenge is the initial separation of plasmid DNA and RNA in such a purification scheme. In this study we investigated the distribution of plasmid DNA and RNA in reverse micellar two-phase systems which is considered to be the basis for the development of an extractive purification step that can easily be integrated into common processes. For this purpose the distribution of the 4.6kb plasmid pUT649 and Escherichia coli RNA in systems comprising isooctane, ethylhexanol, and the surfactant methyltrioctylammoniumchloride (TOMAC) under the influence of different salts was studied. Anion concentrations at which the partitioning behaviour for nucleic acids inverted (inversion point) were identified. Systems capable of separating RNA from plasmid DNA were further analysed and applied to extract RNA from plasmid DNA out of a preconditioned cleared lysate. The capability of reverse micellar systems for plasmid form separation was also shown by capillary and agarose gel electrophoresis.     

Artificial, non-antibody binding proteins for pharmaceutical and industrial applications

Using combinatorial chemistry to generate novel binding molecules based on protein frameworks ('scaffolds') is a concept that has been strongly promoted during the past five years in both academia and industry. Non-antibody recognition proteins derive from different structural families and mimic the binding principle of immunoglobulins to varying degrees. In addition to the specific binding of a pre-defined target, these proteins provide favourable characteristics such as robustness, ease of modification and cost-efficient production. The broad spectrum of potential applications, including research tools, separomics, diagnostics and therapy, has led to the commercial exploitation of this technology by various small- and medium-sized companies. It is predicted that scaffold-based affinity reagents will broaden and complement applications that are presently covered by natural or recombinant antibodies. Here, we provide an overview on current approaches in the biotech industry, considering both scientific and commercial aspects.     

Novel applications for glycosylphosphatidylinositol-anchored proteins in pharmaceutical and industrial biotechnology

Glycosylphosphatidylinositol (GPI)-anchored proteins have been regarded as typical cell surface proteins found in most eukaryotic cells from yeast to man. They are embedded in the outer plasma membrane leaflet via a carboxy-terminally linked complex glycolipid GPI structure. The amphiphilic nature of the GPI anchor, its compatibility with the function of the attached protein moiety and the capability of GPI-anchored proteins for spontaneous insertion into and transfer between artificial and cellular membranes initially suggested their potential for biotechnological applications. However, these expectations have been hardly fulfilled so far. Recent developments fuel novel hopes with regard to: (i) Automated online expression, extraction and purification of therapeutic proteins as GPI-anchored proteins based on their preferred accumulation in plasma membrane lipid rafts, (ii) multiplex custom-made protein chips based on GPI-anchored cell wall proteins in yeast, (iii) biomaterials and biosensors with films consisting of sets of distinct GPI-anchored binding-proteins or enzymes for sequential or combinatorial catalysis, and (iv) transport of therapeutic proteins across or into relevant tissue cells, e.g., enterocytes or adipocytes. Latter expectations are based on the demonstrated translocation of GPI-anchored proteins from plasma membrane lipid rafts to cytoplasmic lipid droplets and eventually further into microvesicles which upon release from donor cells transfer their GPI-anchored proteins to acceptor cells. The value of these technologies, which are all based on the interaction of GPI-anchored proteins with membranes and surfaces, for the engineering, production and targeted delivery of biomolecules for a huge variety of therapeutic and biotechnological purposes should become apparent in the near future.     

Aspergillus terreus as an industrial filamentous fungus for pharmaceutical biotechnology

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A novel cleaning process for industrial production of xylose in pilot scale from corncob by using screw-steam-explosive extruder

Steam explosion is the most promising technology to replace conventional acid hydrolysis of lignocellulose for biomass pretreatment. In this paper, a new screw-steam-explosive extruder was designed and explored for xylose production and lignocellulose biorefinery at the pilot scale. We investigated the effect of different chemicals on xylose yield in the screw-steam-explosive extrusion process, and the xylose production process was optimized as followings: After pre-impregnation with sulfuric acid at 80 °C for 3 h, corncob was treated at 1.55 MPa with 9 mg sulfuric acid/g dry corncob (DC) for 5.5 min, followed by countercurrent extraction (3 recycles), decoloration (activated carbon dosage 0.07 g/g sugar, 75 °C for 40 min), and ion exchange (2 batches). Using this process, 3.575 kg of crystal xylose was produced from 22 kg corncob, almost 90 % of hemicellulose was released as monomeric sugar, and only a small amount of by-products was released (formic acid, acetic acid, fural, 5-hydroxymethylfurfural, and phenolic compounds were 0.17, 1.14, 0.53, 0.19, and 1.75 g/100 g DC, respectively). All results indicated that the screw-steam-explosive extrusion provides a more effective way to convert hemicellulose into xylose and could be an alternative method to traditional sulfuric acid hydrolysis process for lignocellulose biorefinery.