Plasmid adsorption to anion-exchange matrices: comments on plasmid recovery

A number of anion-exchange adsorbents were constructed, employing nonporous silica fibers, and examined with the aim of describing factors that influence desorption and recovery of plasmid DNA (pDNA). The fibers were provided with ligands via adsorption of the polymeric amines poly(ethyleneimine) or chitosan, or via graft-polymerization of primary, tertiary, or quaternary amine monomers to vinyl-silanized fibers. Several adsorbents showed an almost irreversible plasmid binding. It was suggested that important factors affecting the DNA releasing ability are (i) type of amine ligand used (primary amines bind plasmids the strongest), (ii) the structure of the nucleic acid (supercoiled pDNA may bind stronger than linear genomic DNA), (iii) shift of ligand pK(a) (due to the proximity of highly charged pDNA), and (iv) the solid support itself (steric factors may lead to kinetically stable complexes). The last factor was derived from several comparisons between support-bound ligand and free soluble ligand. It was thus observed that polyelectrolyte complexes associated with a surface were much more difficult to dissociate than the equivalent soluble complexes.     

Design of expanded bed supports for the recovery of plasmid DNA by anion exchange adsorption

In this study we detail the rational design of new chromatographic adsorbents tailored for the capture of plasmid DNA. Features present on current chromatographic supports that can significantly enhance plasmid binding capacity have been identified in packed bed chromatography experiments and blueprints for improved expanded bed adsorbents have been put forward. The characterisation and testing of small (20-40 m) high density (>3.7 g cm^–3) pellicular expanded bed materials functionalised with various anion exchange structures is presented. In studies with calf thymus DNA, dynamic binding capacities of 1.2 and 3.4 mg ml^–1 were recorded for prototype diethylaminoethyl-and polyethylene imine-linked adsorbents which were respectively 25 and 70 fold higher than those of equivalently derivatised commercial expanded bed materials. The prototype polyethylene imine-coupled material exhibited severe sensitivity to inter-particle bridging by nucleic acid polymers, gave low DNA recoveries (<37%) and proved difficult to regenerate. In contrast, few operational difficulties were experienced with the diethylaminoethyl-linked prototype adsorbent and successful high capacity (>0.8 mg ml^–1) capture of plasmid DNA from crude neutralised E. coli lysate was demonstrated.     

阴离子交换晶胶层析分离质粒DNA

质粒DNA(pDNA)作为重要的基因治疗药物载体,其广泛应用受纯度和产量的限制。为了获得高纯度的pDNA,首先制备超大孔连续床晶胶基质,接枝二乙氨基乙基葡聚糖得到阴离子交换型晶胶介质;然后以pUC19质粒为例,将目标质粒转化至大肠杆菌,培养收集,碱液裂解和离心;最后用阴离子交换型晶胶介质从离心上清液中一步法层析分离pDNA。通过优化层析过程的pH值和洗脱条件,最终在pH值为6.6时,用0.5 mol/L的NaCl溶液洗脱,得到较高纯度的pDNA。整个分离过程中不使用动物源性酶,也不需常规分离中的高毒试剂,使获得pDNA的过程和产物更加安全。     

Affinity adsorption of plasmid DNA

The development of a protein-mediated dual functional affinity adsorption of plasmid DNA is described in this work. The affinity ligand for the plasmid DNA comprises a fusion protein with glutathione-S-transferase (GST) as the fusion partner with a zinc finger protein. The protein ligand is first bound to the adsorbent by affinity interaction between the GST moeity and gluthathione that is covalently immobilized to the base matrix. The plasmid binding is then enabled via the zinc finger protein and a specific nucleotide sequence inserted into the DNA. At lower loadings, the binding of the DNA onto the Fractogel, Sepharose, and Streamline matrices was 0.0078 +/- 0.0013, 0.0095 +/- 0.0016, and 0.0080 +/- 0.0006 mg, respectively, to 50 microL of adsorbent. At a higher DNA challenge, the corresponding amounts were 0.0179 +/- 0.0043, 0.0219 +/- 0.0035, and 0.0190 +/- 0.0041 mg, respectively. The relatively constant amounts bound to the three adsorbents indicated that the large DNA molecule was unable to utilize the available zinc finger sites that were located in the internal pores and binding was largely a surface adsorption phenomenon. Utilization of the zinc finger binding sites was shown to be highest for the Fractogel adsorbent. The adsorbed material was eluted with reduced glutathione, and the eluted efficiency for the DNA was between 23% and 27%. The protein elution profile appeared to match the adsorption profiles with significantly higher recoveries of bound GST-zinc finger protein.     

A comparison of gel filtration chromatographic supports for plasmid purification

Two gel filtration chromatographic supports, Superose 6 and Sephacryl S1000 SF, were used to purify supercoiled plasmids using a 4.8 kb plasmid as a model. Both supports purified the plasmid from RNA and other small molecular weight contaminants, as shown by agarose electrophoresis and ion exchange HPLC, with an overall yield of 70%. Sephacryl S1000 SF was the better support as it resolved supercoiled, relaxed, linear and concatamer plasmid forms, and chromosomal DNA.     

Purification of plasmid DNA by chromatographic methods

Chromatographic methods have been used to purify the DNA of plasmid RP1. DNA was purified in two stages. DNA was precipitated by ethanol and separated from RNA and proteins in Sepharose 4B column after lysis of plasmid containing cells by alkaline solution of sodium dodecylsulphate. Separation of the total DNA preparation and isolation of plasmid DNA was achieved at the second stage by chromatography on the hydroxyapatite column. The resulting purified plasmid DNA was free of RNA, protein and linear fragments of chromosomal DNA. The plasmid DNA kept intact native structure and possessed the transforming activity. The DNA of RP1 yield after purification by the described technique presented 70-80 micrograms per g of wet biomass.     

Large-scale purification of plasmid DNA by anion-exchange high-performance liquid chromatography.

Numerous methods have previously been reported for the final steps in the large-scale purification of plasmid DNA. Although gel permeation and reverse-phase high-performance liquid chromatography have been utilized for this procedure in the past, the limited capacity of these systems often necessitated multiple rounds of chromatography, especially with the high copy number plasmids commonly in use today. In this paper, the use of the high-capacity, high-resolution Protein-Pak DEAE 8HR column is presented for the large-scale isolation of highly purified plasmid DNA from crude E. coli cell lysates. Up to 5 mg of plasmid DNA have been purified in a single 50-minute chromatography run. The purified DNA demonstrated excellent biological activity as demonstrated by restriction endonuclease digestion, E. coli transformation and DNA-mediated gene transfection of eukaryotic cells.     

Potential application of hydrogel-based strong anion-exchange membrane for plasmid DNA purification

The potential application of a hydrogel-based strong anion-exchange (Q) membrane to purify plasmid DNAs was evaluated. The maximum binding capacity of plasmid DNA was estimated to be 12.4 mg/ml of membrane volume with a plasmid recovery yield of ～90%. The effect of the inherent properties of plasmid DNA, membrane adsorbent, and the ionic environment on membrane performance was systematically investigated. Plasmid DNAs with smaller tertiary structure tended to have a better recovery than those with larger tertiary structure. Environmental Scanning Electron Microscopy (ESEM) revealed that the hydrogel structure is more porous on one side of membrane than the other. Membrane pre-treatment significantly improved pore distribution and increased membrane porosity resulting in a better adsorption, recovery, and higher flux. The selection of proper operating pH led to further improvement. The relative contribution of these factors to improve membrane chromatography of plasmid DNAs was analyzed using statistical modeling. It was found that the adsorption of plasmid DNA was mainly affected by the available adsorptive area associated with membrane porosity, whereas the recovery of plasmid DNAs was mainly affected by the environmental pH.     

Purification of supercoiled plasmid DNA using chromatographic processes

The interest in purifying injectable-grade plasmid DNA has increased with the development of gene therapy and DNA vaccination technologies. In this paper we develop a method for purifying a 4.8 kb plasmid based on chromatographic processes. An NaCl gradient was optimized on a Q Sepharose column and plasmid was eluted at 800-820 mM NaCl in a broad peak. Supercoiled plasmid was isolated after a final Sepharcryl S1000 SF gel filtration step. Final plasmid preparation was depleted of proteins and RNA, as revealed by the BCA assay and 1% agarose gel electrophoresis.     

Purification of pharmaceutical-grade plasmid DNA by anion-exchange chromatography in an RNase-free process

Anion-exchange is the most popular chromatography technique in plasmid DNA purification. However, poor resolution of plasmid DNA from RNA often results in the addition of bovine-derived ribonuclease (RNase) A to degrade RNA impurities which raises regulatory concerns for the production of pharmaceutical-grade plasmid DNA. Low capacity for plasmid of most commercial media is another issue affecting the suitability of anion-exchange chromatography for large-scale processing. This study reports the use of anion-exchange chromatography to remove RNA in an RNase-free plasmid purification process. Resolution was achieved through careful selection of adsorbent and operating conditions as well as RNA reduction steps before chromatography. Dynamic capacity for plasmid was significantly increased (to 3.0mg/ml) so that it is now possible to envisage the large-scale manufacturing of therapeutic-grade plasmid DNA in the absence of added RNase using anion-exchange chromatography as a polishing step.     

LacO-LacI interaction in affinity adsorption of plasmid DNA

Current approaches for purifying plasmids from bacterial production systems exploit the physiochemical properties of nucleic acids in non-specific capture systems. In this study, an affinity system for plasmid DNA (pDNA) purification has been developed utilizing the interaction between the lac operon (lacO) sequence contained in the pDNA and a 64mer synthetic peptide representing the DNA-binding domain of the lac repressor protein, LacI. Two plasmids were evaluated, the native pUC19 and pUC19 with dual lacO3/lacOs operators (pUC19(lacO3/lacOs)), where the lacOs operator is perfectly symmetrical. The DNA-protein affinity interaction was evaluated by surface plasmon resonance using a Biacore system. The affinity capture of DNA in a chromatography system was evaluated using LacI peptide that had been immobilized to Streamline adsorbent. The KD-values for double stranded DNA (dsDNA) fragments containing lacO1 and lacO3 and lacOS and lacO3 were 5.7 +/- 0.3 x 10(-11) M and 4.1 +/- 0.2 x 10(-11) M respectively, which compare favorably with literature reports of 5 x 10(-10)-1 x 10(-9) M for native lacO1 and 1-1.2 x 10(-10) M for lacO1 in a saline buffer. Densitometric analysis of the gel bands from the affinity chromatography run clearly showed a significant preference for capture of the supercoiled fraction from the feed pDNA sample. The results indicate the feasibility of the affinity approach for pDNA capture and purification using native protein-DNA interaction.     

Purification of plasmid DNA using tangential flow filtration and tandem anion-exchange membrane chromatography

A new bioprocess using mainly membrane operations to obtain purified plasmid DNA from Escherechia coli ferments was developed. The intermediate recovery and purification of the plasmid DNA in cell lysate was conducted using hollow-fiber tangential filtration and tandem anion-exchange membrane chromatography. The purity of the solutions of plasmid DNA obtained during each process stage was investigated. The results show that more than 97% of RNA in the lysate was removed during the process operations and that the plasmid DNA solution purity increased 28-fold. One of the main characteristics of the developed process is to avoid the use of large quantities of precipitating agents such as salts or alcohols. A better understanding of membrane-based technology for the purification of plasmid DNA from clarified E. coli lysate was developed in this research. The convenience of anion-exchange membranes, configured in ready-to-use devices can further simplify large-scale plasmid purification strategies.     

N-乙酰神经氨酸在离子交换树脂AD-1上的吸附热/动力学

主要研究了N-乙酰神经氨酸(Neu5Ac)在AD-1离子交换树脂上的吸附行为。通过静态摇瓶的方法,利用Langmuir模型对热力学平衡数据进行拟合,测得树脂的最大Neu5Ac吸附量为0.39 g/g,且不受温度影响。依次用大孔扩散模型、大孔微孔扩散模型对不同Neu5Ac初始质量浓度的动力学数据进行拟合,结果表明,在较低浓度和较高浓度下,Neu5Ac在AD-1树脂上的离子交换过程的限速步骤依次为大孔扩散和大孔微孔扩散,其中大孔扩散系数Dp为1.453×10-8m2/min,微孔扩散系数Dc为9.153×10-15m2/min。最后利用大孔微孔扩散模型研究了树脂颗粒度大小对Neu5Ac在AD-1树脂上的离子交换动力学的影响,发现选取较小颗粒度的树脂有利于提高离子交换速率,且模型与实验数据吻合较好,从而验证了模型的准确性。AD-1树脂对Neu5Ac有较大的吸附容量和较快的吸附速率。     

Purification of plasmid DNA from Escherichia coli ferments using anion-exchange membrane and hydrophobic chromatography

A novel downstream bioprocess was developed to obtain purified plasmid DNA (pDNA) from Escherichia coli ferments. The intermediate recovery and purification of the pDNA in cell lysate was conducted using hollow-fiber tangential filtration and frontal anion-exchange membrane and elution hydrophobic chromatographies. The purity of the solutions of pDNA obtained during each process stage was investigated. The results show that the pDNA solution purity increased 30-fold and more than 99% of RNA in the lysate was removed during the process operations. The combination of membrane operations and hydrophobic interaction chromatography resulted in an efficient way to recover pDNA from cell lysates. A better understanding of membrane-based technology for the purification of pDNA from clarified E. coli lysate was developed in this research.     

Separation of topological forms of plasmid DNA by anion-exchange HPLC: shifts in elution order of linear DNA

We sought to establish a single anion-exchange HPLC method for the separation of linear, open circular and supercoiled plasmid topoisomers using purified topoisomeric forms of three plasmids (3.0, 5.5 and 7.6 kb). However, finding one condition proved elusive as the topoisomer elution order was determined to depend on salt gradient slope. The observed change in selectivity increased with plasmid size and was most pronounced for the linear form. Indeed, the elution order of the linear 7.6 kb plasmid was reversed relative to the supercoiled form. This observation may have implications for methods used in quality control of plasmid DNA.     

Anion exchange purification of plasmid DNA using expanded bed adsorption

Recent developments in gene therapy with non-viral vectors and DNA vaccination have increased the demand for large amounts of pharmaceutical-grade plasmid DNA. The high viscosity of process streams is of major concern in the purification of plasmids, since it can cause high back pressures in column operations, thus limiting the throughput. In order to avoid these high back pressures, expanded bed anion exchange chromatography was evaluated as an alternative to fixed bed chromatography. A Streamline 25 column filled with 100 ml of Streamline QXL media, was equilibrated with 0.5 M NaCl in TE (10 mM Tris, 1 mM EDTA, pH=8.0) buffer at an upward flow of 300 cmh^-1, E. coli lysates (obtained from up to 3 liters of fermentation broth) were injected in the column. After washing out the unbound material, the media was allowed to sediment and the plasmid was eluted with 1 M NaCl in TE buffer at a downward flow of 120 cmh^-1. Purification factors of 36±1 fold, 26±0.4 plasmid purity, and close to 100% yields were obtained when less than one settled column volume of plasmid feed was injected. However, both recovery yield and purity abruptly decreased when larger amounts were processed–values of 35±2 and 5±0.7 were obtained for the recovery yield and purity, respectively, when 250 ml of feedstock were processed. In these cases, gel clogging and expansion collapse were observed. The processing of larger volumes, thus larger plasmid quantities, was only possible by performing an isopropanol precipitation step prior to the chromatographic step. This step led to an enhancement of the purification step.     

Milligram scale parallel purification of plasmid DNA using anion-exchange membrane capsules and a multi-channel peristaltic pump

A parallel chromatographic procedure for the purification of milligram amounts of plasmid DNA was developed. Initial studies showed that ion-exchange membrane capsules displayed high capacity for plasmid DNA. Interestingly, a weak anion exchanger (DEAE) proved to be superior to the strong quarternary ammonium group with respect to elution and regeneration properties and the 75 cm(2) Sartobind D membrane capsule (MA75D, Sartorius) was selected for further studies. A method for reducing endotoxin levels by using CTAB as a precipitant was optimised. By introducing this step into the protocol, endotoxin levels could be reduced approximately 100-fold to 相似文献   

Studies on aerosol delivery of plasmid DNA using a mesh nebulizer

Aerosol delivery of plasmid DNA therapeutic solutions is promising for the treatment of respiratory diseases. However, it poses challenges, most significantly the need to protect the delicate supercoiled (sc) structure of plasmid during aerosolization. Nebulizers for liquid aerosolization using meshes appear a better method for delivery than conventional jet and ultrasonic nebulizers. This paper explores their application to the delivery of plasmid DNA. A computational fluid dynamics model of the dynamics of fluid flow through the nozzle of the MicroAIR mesh nebulizer indicated high strain rates (>10(5) s(-1)) near the nozzle exit capable of causing damage to the shear-sensitive plasmid DNA. Knowledge of the strain rates predicted using CFD and molecule size determined using atomic force microscopy (AFM) enabled estimation of the hydrodynamic force and whether damage of shear-sensitive therapeutics was likely. Plasmids of size 5.7 and 20 kb were aerosolized in the mesh nebulizer. The sc structure of the 5.7-kb plasmid was successfully delivered without damage, while aerosolization of the 20-kb plasmid led to disintegration of the pDNA sc structure as observed in AFM. Subsequent formulation of the sc 20-kb plasmid with PEI resulted in successful aerosol delivery. The maximum hydrodynamic forces computed for the aerosolization of structures of the size of 5.7-kb and PEI formulated 20-kb plasmids were less than the forces reported to damage the structure of double-stranded DNA. A combination of CFD analysis and structure analysis may be used to predict successful aerosol delivery in such a mesh nebulizer.     

Supercoiled plasmid DNA: selective purification by thiophilic/aromatic adsorption

Separation of the different plasmid isoforms is a major challenge in purifying plasmid DNA. We describe a new type of biochemical interaction that occurs in the presence of high concentrations of lyotropic salt and results in the selective adsorption of supercoiled plasmid DNA to aromatic thioether ligands. Under well-defined conditions, these ligands are capable of separating supercoiled plasmid DNA (ccc) from its isoform, i.e. open circular (oc) form. Integrated in a process, preceded by group separation and followed by anion-exchange chromatography, this new purification method may facilitate the production of highly purified supercoiled plasmid DNA for use in gene therapy and DNA vaccine applications.