Successful application of monolithic innovative technology using a carbonyldiimidazole disk to purify supercoiled plasmid DNA suitable for pharmaceutical applications

The growing demand on plasmid DNA (pDNA) manufacture for therapeutic applications requires a final product with higher quality and quantity, spending the least time. Most of the current processes for pDNA production use at least one chromatographic step, which often constitutes a key-step in the purification sequence. Monolithic stationary phases are new alternatives to the conventional matrices, which offer fast separation of pDNA due to their excellent mass transfer properties and their high binding capacity for large molecules, as pDNA. However, the efficient recovery of pure pDNA focuses on a suitable balance of the feedstock, adsorbent and mobile phase properties. To satisfy the increasing demand for pharmaceutical grade plasmids, we developed a novel downstream process which overcomes the bottlenecks of common lab-scale techniques while complying with all regulatory requirements. This work reports an integrative approach using the carbonyldiimidazole monolith to efficiently purify the supercoiled (sc) pDNA active conformation from other plasmid topologies and Escherichia coli impurities present in a clarified lysate. The monolith specificity and selectivity was also assessed by performing experiments with plasmids of several sizes of 2.7, 6.05 and 7.4 kilo base pairs (kbp), verifying the applicability to purify different plasmids. Hence, the process yield of the pDNA purification step using the CDI monolith was 89%, with an extremely reduced level of impurities (endotoxins and gDNA), which was reflected in good transfection experiments of the sc plasmid DNA sample. Overall, the analytical results and transfection studies performed with the pDNA sample purified with this monolithic enabling technology, confirmed the suitability of this pDNA to be used in pharmaceutical applications.     

Purification of supercoiled plasmid DNA from clarified bacterial lysate by arginine‐affinity chromatography: Effects of spacer arms and ligand density

Efficient loading on a chromatographic column is the dilemma of the process development faced by engineers in plasmid DNA purification. In this research, novel arginine‐affinity chromatographic beads were prepared to investigate the effect of spacer arm and ligand density to their chromatographic performance for the purification of plasmid. The result indicated that dynamic binding capacity for plasmid increased with an increasing ligand density and carbon number of spacer arm, and the highest binding capacity for plasmid of 6.32 mg/mL bead was observed in the column of arginine bead with a ligand density of 47 mmol/L and 10‐atom carbon spacer. Furthermore, this arginine bead exhibited better selectivity to supercoiled (sc) plasmid. The evidence of a linear gradient elution suggested further that the binding of plasmid on arginine beads was driven by electrostatic interaction and hydrogen bonding. Hence, sc plasmid could successfully be purified from clarified lysate by two‐stepwise elution of salt concentration. By the refinement of the elution scheme and loading volume of clarified lysate, the column of arginine bead with a ligand density of 47 mmol/L exhibited the highest recovery yield and a much higher productivity among arginine‐affinity columns. Therefore, reshaped arginine beads provided more feasible and practical application in the preparation of sc plasmid from clarified lysate.     

Adsorption Strategy of Plasmid DNA Nanoparticulate: Preparative Purification by a Simple Custom Expanded Bed Column

This paper summarizes the critical examination of the hydrodynamic performance of the NBG expanded bed contactor operated with streamline-DEAE adsorbent under various operating conditions for expanded bed adsorption of plasmid DNA nanoparticles from alkaline lysate. The purification process is not RNase-free. In this study, a rapid and efficient scaleable purification protocol obtaining, plasmid DNA nanoparticles (average size of 40 nm) with a high purity level for use as therapeutic agent in customized NBG expanded bed columns was developed. This technique allows efficient levels of binding to the column media and vector purification without centrifugation or filtration steps. Residence time distribution (RTD) studies were exploited to achieve the optimal condition of plasmid DNA nanoparticle (pDNA) recovery upon anion exchange adsorbent in this contactor. In addition, the purification experiments were carried out in the expanded bed columns with settle bed height of 6.0 ± 0.2 cm. NaCl gradient elution enabled the isolation of supercoiled plasmid from low-Mr RNA, cDNA and plasmid variants. Subsequently dynamic binding capacity of the adsorbent was calculated while these values decreased with increase in flow velocity. Moreover, the effect of pH upon the performance of this recovery process and the feedstock volume upon the expanded bed anion exchange purification was investigated. The results demonstrated that separation of low-Mr RNA from plasmid DNA isoforms in the range of pH between 5.5 and 7.5 is achievable in this column. The yield of recovery of pDNA in optimal condition was higher than 88.51% which was a superior result in one-pass frontal chromatography. The generic application of simple customized NBG expanded bed column and its potential for the purification and recovery of plasmid DNA as a nanoparticulate bioproduct is strongly discussed.     

Large-volume methacrylate monolith for plasmid purification. Process engineering approach to synthesis and application

The extent of exothermicity associated with the construction of large-volume methacrylate monolithic columns has somewhat obstructed the realisation of large-scale rapid biomolecule purification especially for plasmid-based products which have proven to herald future trends in biotechnology. A novel synthesis technique via a heat expulsion mechanism was employed to prepare a 40 mL methacrylate monolith with a homogeneous radial pore structure along its thickness. Radial temperature gradient was recorded to be only 1.8 degrees C. Maximum radial temperature recorded at the centre of the monolith was 62.3 degrees C, which was only 2.3 degrees C higher than the actual polymerisation temperature. Pore characterisation of the monolithic polymer showed unimodal pore size distributions at different radial positions with an identical modal pore size of 400 nm. Chromatographic characterisation of the polymer after functionalisation with amino groups displayed a persistent dynamic binding capacity of 15.5 mg of plasmid DNA/mL. The maximum pressure drop recorded was only 0.12 MPa at a flow rate of 10 mL/min. The polymer demonstrated rapid separation ability by fractionating Escherichia coli DH5alpha-pUC19 clarified lysate in only 3 min after loading. The plasmid sample collected after the fast purification process was tested to be a homogeneous supercoiled plasmid with DNA electrophoresis and restriction analysis.     

Hydrophobic interaction membrane chromatography for plasmid DNA purification: Design and optimization

Chromatography is one of the key operations in the downstream processing of plasmid DNA (pDNA). However, the increased demand for highly purified pDNA experienced in recent years has made clear the need for alternative processes capable of retaining the advantages of conventional chromatography, such as selectivity, while providing increased throughput at a lower cost. The work presented in this article outlines the development and optimization of an alternative hydrophobic interaction membrane chromatography process for the purification of pDNA. The studies included the modification of functionalized membrane supports with a linear alkyl chain ligand and the testing of chromatographic performance of these membranes. Three modification procedures were tested and the membranes were screened for their capacity and selectivity. The modified membranes could separate the model plasmid pVAX1‐LacZ (6050 bp) from impurities in clarified Escherichia coli cell lysates (specifically RNA), with good resolution. Subsequent optimization of elution profiles with the best‐performing modified membrane, resulted in a high purification factor of 4.7, competitive with its bead process counterpart, and a plasmid yield of 73%.     

Separation of plasmid DNA isoforms by highly converging flow through small membrane pores

Plasmid DNA isoforms can be separated by both agarose gel electrophoresis and a variety of chromatographic methods, but both of these approaches have significant shortcomings in terms of scalability, throughput, and/or resolution. This study provides the first demonstration that the supercoiled, linear, and open-circular isoforms of plasmid DNA can be effectively separated based on differences in their elongational flexibility in the highly converging flow field that is established during membrane ultrafiltration. Data were obtained with plasmids from 3 to 17 kbp in size using commercially available cellulose ultrafiltration membranes with pores an order of magnitude smaller than the DNA root-mean-square radius of gyration. High-resolution separations were achieved by controlling the filtrate flux between the critical flux values required for transmission of the individual isoforms. The separation behavior in ultrafiltration was very different than that observed in size exclusion chromatography or agarose gel electrophoresis due to differences in the underlying separation mechanisms. The simplicity of the ultrafiltration process makes this approach attractive for a wide range of applications, including large-scale purification of plasmid DNA for gene therapy.     

Recognition based separation of HIV-Tat protein using avidin–biotin interaction in modified microfiltration membranes

Recognition based separation using modified microfiltration membranes provides an efficient and cost-effective alternative to conventional column chromatography for the separation and purification of a specific protein from mixture of proteins. In this study, Tat protein, which has been proposed as the specific target for AIDS vaccine, was separated and purified from a complex mixture of proteins, known as bacterial lysate (BL) using avidin–biotin interaction in 4-stack microfiltration membranes system. It was established by SDS-PAGE and Western Blot analysis that membrane based process recovered more pure form of Tat compared to conventional packed-bead column chromatography. The critical factors involved in the process, mainly, the accessibility of the covalently immobilized avidin sites by the biotinylated protein and the associated fouling of the membranes due to the permeation of proteins, were also studied. The accessibility of immobilized avidin sites in membrane was quantified by biotinylated solutions of different types and compositions. It was observed that permeation of proteins caused substantial fouling on the membrane matrix. The resistance offered by the protein layer and the approximate thickness of the protein layer were also quantified.     

DNA removal on different chromatography supports used for EPO purification by spike studies

Chromatographic techniques are used in the purification step of human recombinant erythropoietin production process to obtain a reliable product with high purity. Anion-exchange chromatography supports have proved high efficient in removing contaminants such as DNA. For that reason, the DNA removal was determined by spike studies, on three anion-exchange chromatographic supports: gel, membrane, and monolithic column, which is used in intermediate purification stage. This study showed that membrane and monolith columns have very good results in the removal of contaminants at this step. Log removal values (LRV) greater than 3.5 were obtained from DNA spike clearance studies. Monolithic column was determined as the best technological proposal, with more than 4 LRV, 7.72?mg DNA per milliliter of adsorbent and 85% protein recovery in nonspike run. The results of this study may be used as a guide in the selection of commercially available chromatography supports for intermediate purification steps in recombinant protein production.     

Performance of a non-grafted monolithic support for purification of supercoiled plasmid DNA

The use of therapeutics based on plasmid DNA (pDNA) relies on procedures that efficiently produce and purify the supercoiled (sc) plasmid isoform. Several chromatographic methods have been applied for the sc plasmid purification, but with most of them it is not possible to obtain the required purity degree and the majority of the supports used present low capacity to bind the plasmid molecules. However, the chromatographic monolithic supports are an interesting alternative to conventional supports due to their excellent mass transfer properties and their high binding capacity for pDNA. The separation of pDNA isoforms, using short non-grafted monolithic column with CarbonylDiImidazole (CDI) functional groups, is described in the current work. The effect of different flow rates on plasmid isoforms separation was also verified. Several breakthrough experiments were designed to study the effect of different parameters such as pDNA topology and concentration as well as flow rate on the monolithic support binding capacity. One of the most striking results is related to the specific recognition of the sc isoform by this CDI monolith, without flow rate dependence. Additionally, the binding capacity has been found to be significantly higher for sc plasmid, probably because of its compact structure, being also improved when using feedstock with increased plasmid concentrations and decreased linear velocity. In fact, this new monolithic support arises as a powerful instrument on the sc pDNA purification for further clinical applications.     

巯基吡啶配基液相色谱固定相的制备及其对质粒的快速纯化

在基因治疗中,质粒是一种常用的非病毒型载体。由于目前市场上对质粒的需求量很大,因此有必要开发大规模的质粒制备技术。该文以双孔型流通色谱介质为基质,以巯基吡啶为配基,制得了液相色谱固定相,并考察了其对质粒DNA的纯化效果,分析了分离机理。结果表明:该分离介质对质粒的纯化是基于疏水作用;当上样量为10 mL (质粒质量浓度为0.30 mg/mL)、流速高达4 mL/min时,质粒仍然能以100%的收率实现纯化,其纯度为100%。该色谱介质对RNA的柱容量高达2.2 mg/mL。     

Integrated process for purification of plasmid DNA using aqueous two-phase systems combined with membrane filtration and lid bead chromatography

An integrated process for purifying a 6.1 kilo base pair (kbp) plasmid from a clarified Escherichia coli cell lysate based on an ultra/diafiltration step combined with polymer/polymer aqueous two-phase system and a new type of chromatography is described. The process starts with a volume reduction (ultrafiltration) and buffer exchange (diafiltration) of the clarified lysate using a hollow fibre membrane system. The concentrated and desalted plasmid solution is then extracted in a thermoseparating aqueous two-phase system, where the contaminants (RNA and proteins) to a large extent are removed. While the buffer exchange (diafiltration) is necessary in order to extract the plasmid DNA exclusively to the top phase, experiments showed that the ultrafiltration step increased the productivity of the aqueous two-phase system by a factor of more than 10. The thermoseparated water phase was then subjected to a polishing step using lid bead chromatography. Lid beads are a new type of restricted access chromatography beads, here with a positively charged inner core that adsorbed the remaining RNA while its inert surface layer prevented adsorption of the plasmid DNA thus passing in the flow-through of the column. Differently-sized plasmid DNA in the range of 2.7-20.5 kbp were also partitioned in the aqueous two-phase system. Within this size range, all plasmid DNA was exclusively extracted to the top phase. The complete process is free of additives and easy scalable for use in large scale production of plasmid DNA. The overall process yield for plasmid DNA was 69%.     

Monolith-based immobilized metal affinity chromatography increases production efficiency for plasmid DNA purification

Immobilized metal affinity monolith column as a new class of chromatographic support is shown to be superior to conventional particle-based column as plasmid DNA (pDNA) purification platform. By harnessing the affinity of endotoxin to copper ions in the solution, a majority of endotoxin (90%) was removed from the alkaline cell lysate using CuCl(2)-induced precipitation. RNA and remaining endotoxin were subsequently removed to below detection limit with minimal loss of pDNA using either monolith or particle-based column. Monolith column has the additional advantage of feed concentration and flowrate-independent dynamic binding capacity for RNA molecules, enabling purification process to be conducted at high feed RNA concentration and flowrate. The use of monolith column gives three fold increased productivity of pDNA as compared to particle-based column, providing a more rapid and economical platform for pDNA purification.     

质粒DNA的阴离子交换色谱法纯化及内毒素去除

采用Fractogel EMD TMAE(M)强阴离子交换介质分离纯化质粒脱氧核糖核酸（DNA）,该介质对质粒DNA的动态载样量达0.62 mg/mL。用Triton X-114或Triton X-100预先处理质粒DNA的裂解澄清液后,经阴离子交换色谱分离纯化获得的质粒DNA中内毒素含量分别为6.42 EU/mg和9.50 EU/mg,显著低于未经Triton处理的裂解澄清液（67.82 EU/mg）。该法实现了阴离子交换色谱一步纯化质粒DNA的目的,具有简便、省时、成本低等特点。     

Application of arginine as an efficient eluent in cation exchange chromatographic purification of a PEGylated peptide

A cation exchange chromatographic purification process step was developed for the purification of human PEGylated PYY 3–36 from the PEGylation reaction mixture. In this publication we describe experiments carried out to evaluate the chromatographic performance of arginine chloride as an effective cation exchange chromatography eluent. Using arginine we obtained improved recovery and resolution during chromatographic purification of a peptide PEGylation reaction mixture. The chromatographic elution performance of arginine was compared to other cationic amino acids and sodium chloride. Arginine provided higher yield and better resolution of product from other process impurities. The process was successfully scaled up to produce clinical supplies. The basis for improvement in process performance with arginine was characterized by examining the effect of buffer and concentration of the PEGylated peptide on hydrodynamic volume of the molecule in solution. These results were used to predict the behavior of the molecule in the chromatography process. The enhanced chromatographic performance could be attributed to changes in molecular size with concentration, higher eluent strength of arginine, and resulting changes in mass transfer resistance.     

Application of monoliths for plasmid DNA purification development and transfer to production

The demand of high-purity plasmid DNA (pDNA) for gene-therapy and genetic vaccination is still increasing. For the large scale production of pharmaceutical grade plasmids generic and economic purification processes are needed. Most of the current processes for pDNA production use at least one chromatography step, which always constitutes as the key-step in the purification sequence. Monolithic chromatographic supports are an alternative to conventional supports due to their excellent mass transfer properties and their high binding capacity for pDNA. Anion-exchange chromatography is the most popular chromatography method for plasmid separation, since polynucleotides are negatively charged independent of the buffer conditions. For the implementation of a monolith-based anion exchange step into a pDNA purification process detailed screening experiments were performed. These studies included supports, ligand-types and ligand-densities and optimization of resolution and productivity. For this purpose model plasmids with a size of 4.3 and 6.9 kilo base pairs (kbp) were used. It could be shown, that up-scaling to the production scale using 800 ml CIM Convective Interaction Media radial flow monoliths is possible under low pressure conditions. CIM DEAE was successfully implemented as intermediate step of the cGMP pDNA manufacturing process. Starting from 2001 fermentation aliquots pilot scale purification runs were performed in order to prove scale-up and to predict further up-scaling to 8 1 tube monolithic columns. The analytical results obtained from these runs confirmed suitability for pharmaceutical applications.     

Effect of salt on purification of plasmid DNA using size-exclusion chromatography

In the present study, we compared the performances of size-exclusion chromatography for the purification of plasmid DNA when different concentrations (0.5M, 1M, 2M, respectively) of two types of salt (NaCl and (NH(4))(2)SO(4)) are present in running buffers. Our experiment results displayed that it is not only the resolution of RNA but also those of supercoiled plasmid DNA and host's genomic DNA were increased greatly in the presence of high concentration of water-structure salt. We deduce that two separation modes may be involved in the process: The supercoiled plasmid DNA is influenced mainly by compaction effect and eluted in the size-exclusion mode; whereas, RNA and genomic DNA are influenced mainly by hydrophobic effect due to their stretched and loose structures and eluted in the interaction mode. This method led to an improved efficiency of size-exclusion chromatography.     

A platform method for plasmid isoforms analysis by capillary gel electrophoresis

In the production of novel biological products, plasmids are often engineered into delivery vectors for target genes, which can be used directly as vaccines or as intermediate products for gene/cell therapy. Plasmid DNA exists in several topological forms such as supercoiled, linear, and open circular. As supercoiled plasmid shows the highest efficiency in transfecting eukaryotic cells, the content of supercoiled plasmids becomes an important indicator of plasmid quality. CGE is an effective analysis method for separating different topological structures of plasmids. For the purpose of providing plasmid manufacturers and regulatory agencies with an efficient and readily used tool for monitoring the quality of plasmids, this article identifies the optimal separation and detection conditions of CGE, presents a platform-based plasmid analytical method, and uses plasmid of different sizes to verify the feasibility of this method. In terms of detector, the LIF detector has obvious advantages over the ultraviolet detector in sensitivity and resolution. Using the optimal CE condition (10× gel buffer), baseline separation of different topological forms and impurities can be achieved for different plasmid sizes (5.9, 7.8, 15.4 kb). In addition, 6.5 kb plasmid was used to compare the different separation technologies such as CGE-LIF, ion exchange chromatography and agarose gel electrophoresis. The result shows that CGE-LIF can provide better resolution and quantitation accuracy than ion exchange chromatography and agarose gel electrophoresis. CGE-LIF, as a quick and convenient method to separate and quantify plasmids, has the advantages of high sensitivity, high resolution, and high quantitative accuracy. Therefore, it is ideal for analysis of plasmids with different sizes, and it can also be used as a platform method for manufacturers and regulatory agencies to monitor the purity and stability of plasmids.     

缬氨酸Schiff碱金属铜配合物对质粒DNA的切割作用

缬氨酸Schiff碱金属铜配合物(PBP-L-Val-Cu)是新合成的一类非酶类切割工具, 合成了4种类型样品分别为L-CH3 Cu, D-CH3 Cu, L-Ph Cu和D-Ph Cu. 以质粒DNA(pUC18)为材料,分别对这4种类型化合物进行核酸切割效率的研究, 得出适合的反应体系后, 通过琼脂糖凝胶电泳对反应不同时间后核酸切割产物进行检测, 最终分别得到每种化合物将超螺旋型DNA切割成为开环型DNA和直线型DNA的切割效率, 经比较得出L-CH3 Cu型的切割效率是最快的. 将直线型DNA切割产物用琼脂糖凝胶回收试剂盒进行回收, 得到的直线型切割产物可以在T4连接酶的作用下重新连接起来. 利用酶切法对切口进行检测, 结果表明, 切割作用是具有特异性的. 另外, 该化合物对质粒pNQ216也具有切割活性.     

Role of recycling in improving the performance of chromatographic solvent gradient purifications

With significant advancement in the upstream processing technology, downstream processing of large bio-molecules is becoming the bottle-neck in the production chain. To face this challenge, design and development of efficient separation processes has become crucial. As a step towards boosting the performance of a chromatographic separation process through improved design, we investigated the potential of recycling as a process option. The most important advantage of recycling is that it can be implemented in an existing batch system without any major investment and consultation. Although impure products are recycled in industries, it is done as additional batch, and only then, when the recoverable product is valuable enough to surpass the loss of productivity in running the additional batches. In our study, on the other hand, it was found that a well-designed recycle can not only improve the yield, but also the productivity of a multi-component purification. A series of multiobjective optimization studies were carried out on multi-component separation to comprehend the role of recycling with reference to an industrially relevant problem, i.e. the chromatographic purification step of the production process of calcitonin.