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.     

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.     

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.     

Supercoiled plasmid DNA purification by integrating membrane technology with a monolithic chromatography

The present study describes the integration of membrane technology with monolithic chromatography to obtain plasmid DNA with high quality. Isolation and clarification of plasmid DNA lysate were first conducted by a microfiltration step, by using a hydrophilic nylon microfiltration membrane, avoiding the need of centrifugation. For the total elimination of the remaining impurities, a suitable purification step is required. Monolithic stationary phases have been successfully applied as an alternative to conventional supports. Thus, the sample recovered from the membrane process was applied into a nongrafted CarbonylDiImidazole disk. Throughout the global procedure, a reduced level of impurities such as proteins and RNA was obtained, and no genomic DNA was detectable in the plasmid DNA sample. The chromatographic process demonstrated an efficient performance on supercoiled plasmid DNA purity and recovery (100 and 84.44%, respectively). Thereby, combining the membrane technology to eliminate some impurities from lysate sample with an efficient chromatographic strategy to purify the supercoiled plasmid DNA arises as a powerful approach for industrial‐scale systems aiming at plasmid DNA purification.     

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.     

Dynamic binding capacity of plasmid DNA in histidine-agarose chromatography

The use of histidine-agarose chromatography in the purification of supercoiled (sc) plasmid DNA (pDNA) from Escherichia coli lysates has been reported recently. In the current work we describe a set of breakthrough experiments which were designed to study the effect of parameters such as flow-rate, temperature, concentration and conformation on the dynamic binding capacity of pDNA to the histidine support. One of the most striking results shows that the dynamic binding capacity for sc pDNA decreases linearly from 250.8 to 192.0 microg sc pDNA/mL when the temperature is varied from 5 to 24 degrees C. This behaviour was attributed to temperature-induced, pre-denaturation conformational changes which promote the removal of negative superhelical turns in sc pDNA molecules and decrease the interaction of DNA bases with the histidine ligands. The capacity for sc pDNA was highly improved when using feeds with higher pDNA concentrations, a phenomenon which was attributed to the fact that pDNA molecules in more concentrated solutions are significantly compressed. A maximum capacity of 530.0 microg pDNA/mL gel was obtained when using a 125 microg/mL pDNA feed at 1 mL/min and 5 degrees C, a figure which is comparable to the plasmid capacity values published for other chromatographic supports. Finally, a more than 2-fold increase in capacity was obtained when changing from open circular to sc pDNA solutions. Overall, the results obtained provide valuable information for the future development and implementation of histidine chromatography in the process scale purification of pDNA.     

Binding and elution strategy for improved performance of arginine affinity chromatography in supercoiled plasmid DNA purification

New interesting strategies for plasmid DNA (pDNA) purification were designed, exploiting affinity interactions between amino acids and nucleic acids. The potential application of arginine-based chromatography to purify pDNA has been recently described in our work; however, to achieve higher efficiency and selectivity in arginine affinity chromatography, it is essential to characterize the behaviour of binding/elution of supercoiled (sc) isoforms. In this study, two different strategies based on increased sodium chloride (225-250 mm) or arginine (20-70 mm) stepwise gradients are described to purify sc isoforms. Thus, it was proved that well-defined binding/elution conditions are crucial to enhance the purification performance, resulting in an improvement of the final plasmids yields and transfection efficiency, as this could represent a significant impact on therapeutic applications of the purified sc isoform.     

Comparison of CIM~ C4-HLD monolithic column with Sartobind phenyl membrane column for pIDKE2 purification

The main component of the Center for Genetic Engineering and Biotechnology(CIGB)candidate vaccine against Hepatitis C virus(HCV)is the pIDKE2 plasmid.The current designed downstream process for the production of pIDKE2 fulfils all regulatory requirements and renders the required quantities of pharmaceuticalgrade plasmid DNA(pDNA)with 95%purity.The advantages of this procedure include high plasmid purity and the elimination of undesirable additives,such as toxic organic extractants and animal-derived enzymes.However,yields and consequently the productivity of the process are low.Previous work demonstrated that the most critical step of the process is the reverse phase chromatography,where conventional porous particle resins are used.Therefore,to increase the process productivity,alternative technologies such as membranes and chromatographic monoliths were tested as alternative options for this critical step.Here,a comparison between the behaviors of CIM~ C4-HLD and Sartobind phenyl matrices was performed.To obtain higher productivities and purities,the dynamic binding capacities and selectivities were evaluated.The results showed that both matrices had a similar capacity for pIDKE2 plasmid,but the separation of pDNA isoforms using CIM~ technology was much better than that with Sartobind.Additionally,the optimal conditions for loading plasmid DNA on a CIMC4-HLD 800-mL monolithic column in a real production process were determined.These optimizations will allow production levels to satisfy the high plasmid consumption demanded by clinical trials.     

3,3′‐Diamino‐N‐methyldipropylamine as a versatile affinity ligand

Currently, in biomedicine and biotechnology fields, there is a growing need to develop and produce biomolecules with a high degree of purity. To accomplish this goal, new purification methods are being developed looking for higher performance, efficiency, selectivity, and cost‐effectiveness. Affinity chromatography is considered one of the most highly selective methods for biomolecules purification. The purpose of this work is to explore a new type of a structurally simple ligand immobilized onto an agarose matrix to be used in affinity chromatography. The ligand in this study, 3,3′‐diamino‐N‐methyldipropylamine has shown low toxicity and low cost of preparation. Moreover, the ability of the ligand to be used in affinity chromatography to purify proteins and nucleic acids was verified. An increasing sodium chloride gradient, using salt concentrations up to 500 mM, was suitable to accomplish the purification of these biomolecules, meaning that the new support allows the recovery of target biomolecules under mild conditions. Thus, the 3,3′‐diamino‐N‐methyldipropylamine ligand is shown to be a useful and versatile tool in chromatographic experiments, with very good results either for proteins or supercoiled plasmid isoform purification.     

Chromatography of plasmid DNA

Liquid chromatography plays a central role in process-scale manufacturing of therapeutic plasmid DNA (pDNA) for gene therapy and DNA vaccination. Apart from its use as a preparative purification step, it is also very useful as an analytical tool to monitor and control pDNA quality during processing and in final formulations. This paper gives an overview of the use of pDNA chromatography. The specificity of pDNA purification and the consequent limitations to the performance of chromatography are described. Strategies currently used to overcome those limitations, as well as other possible solutions are presented. Applications of the different types of chromatography to the purification of therapeutic pDNA are reviewed, and the main advantages and disadvantages behind each technique highlighted.     

质粒DNA在灌注色谱基质上的吸附行为

Anion exchange chromatography is the most popular chromatographic method for plasmid separation.POROS R1 50 is a perfusio n chro mato graphic suppo rt w hich is a reversed phase matrix and is an alternative to co nventio nal o nes due to its mass transfer pro perties.The adso rptio n and elutio n o f the pIDKE2 plasmid o nto reversed phase POROS R1 50 w as studied.Langmuir iso therm mo del w as adjusted in o rder to get the max imum adso rptio n capacity and the disso ciatio n co nstant fo r POROS R1 50-plasmid DNA(pDNA) system.Breakthro ugh curves w ere o btained fo r vo lumetric flo w s betw een 0.69-3.33 mL/min,given dynamic capacity up to 2.3 times higher than tho se repo rted fo r io nic ex change matrix used during the purificatio n pro cess o f plasmids w ith similar size to that o f pIDKE2.The efficiency w as less than 45% fo r the flo w co nditio ns and initial co ncentratio n studied,w hich means that the suppo rt w ill no t be o perated under saturatio n circumstances.     

High Molecular Weight Poly(ethylenimine)‐Based Water‐Soluble Lipopolymer for Transfection of Cancer Cells

Over the past decade, search for novel materials for nucleic acid delivery has prompted a special interest in polymeric nanoparticles (NPs). In this study, the biological applicability of a water‐soluble cationic lipopolymer (WSLP) obtained by the modification of high molecular weight branched poly(ethylenimine) (PEI) with cholesteryl chloroformate is characterized and assessed for better cellular membrane permeability. To test the delivery efficiency of the produced lipopolymer, plasmid DNA (pDNA) encoding the enhanced green fluorescent protein and WSLP are mixed at different charge ratios. WSLP and WSLP/pDNA complexes are characterized by dynamic and static light scattering, particle charge detection, scanning electron microscopy, and transmission electron microscopy. The pDNA loading of WSLP is also verified by agarose gel electrophoresis. Cytotoxicity of PEI, WSLP, and of WSLP/pDNA is evaluated on human A549 and HeLa cells. A remarkable dependence of the toxicity on the dose, cholesterylation, and charge ratio is detected. Transfection is monitored by flow cytometry and by fluorescence microscopy. Importantly, cholesterylation decreases the toxicity of the polymer, while promoting high transfection efficiency in both cell lines. This work indicates a possible optimization mode of the high molecular weight PEI‐based WSLP rendering it a promising candidate for gene delivery.     

Interactions of New Synthesized Fluorescent Cationic Amphiphiles Bearing Pyrene Hydrophobe with Plasmid DNA: Binding Affinities,Aggregation and Intracellular Uptake

In this work, we prepared a novel series of cationic amphiphiles denoted as the Py‐cations (Py‐Gly, Py‐Ala, Py‐Cap, Py‐G₁‐Lys and Py‐G₂‐Lys) bearing fluorescent pyrene and various hydrocarbon linkers between the pyrene hydrophobe and cationic block. Employing these new cationic amphiphiles with pyrene as the fluorescent probe, the interactions between these Py‐cations and plasmid DNA (pDNA) in distilled water and 0.1 M PBS buffer solution have been explored by means of UV‐vis and fluorescent spectrometers, and ethidium bromide dye displacement and agarose‐gel retardant assays were also implemented to evaluate their pDNA binding affinities in aqueous solution. Furthermore, the average sizes and morphologies of self‐assembled Py‐cation/pDNA lipoplex aggregates were examined by dynamic laser light scattering (DLS) and atomic force microscopy (AFM). It was found that these fluorescent cationic amphiphiles showed blue fluorescence emission of pyrene probe at λ = 340 nm in distilled water while their interactions with pDNA led to new strong green emission at λ = 490 nm, and this may be due to the stacking of pyrene and new formation of excimers via the rigid pDNA templated self‐assembly. It was also revealed that the binding between new Py‐cations and pDNA in aqueous solution was strongly influenced by the Py‐cation hydrophobicity, charges of the cation and the presence of electrolytes. With respect to the Py‐cation/pDNA aggregate morphologies, very interesting 1‐D hybrid nanofibers were predominantly observed by AFM for the Py‐Cap/pDNA aggregates. In addition, utilizing a COS‐7 cell‐line, in‐vitro cellular uptakes of new cationic amphiphiles with pyrene probe were studied and visualized by fluorescent microscopy. As a result, this may provide a new approach to investigate the interactions between synthetic cationic lipids and nucleic acids, and pave an alternative clue to design new organic gene delivery carriers.

     

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.     

Performance of hydrophobic interaction ligands for human membrane‐bound catechol‐O‐methyltransferase purification

Despite of membrane catechol‐O‐methyltransferase (MBCOMT, EC 2.1.1.6) physiological importance on catecholamines’ O‐methylation, no studies allowed their total isolation. Therefore, for the first time, we compare the performance of three hydrophobic adsorbents (butyl‐, epoxy‐, and octyl‐Sepharose) in purification of recombinant human COMT (hMBCOMT) from crude Brevibacillus choshinensis cell lysates to develop a sustainable chromatographic process. Hydrophobic matrices were evaluated in terms of selectivity and hMBCOMT's binding and elution conditions. Results show that hMBCOMT's adsorption was promoted on octyl and butyl at ≤375 mM NaH₂PO_4, while on epoxy higher concentrations (>850 mM) were required. Additionally, hMBCOMT's elution was promoted on epoxy, butyl, and octyl using respectively 0.1–0.5, 0.25–1, and 1% of Triton X‐100. On butyl media, a stepwise strategy using 375 and 0 mM NaH₂PO₄, followed by three elution steps at 0.25, 0.7 and 1% Triton X‐100, allowed selective hMBCOMT isolation. In conclusion, significant amounts of MBCOMT were purified with high selectivity on a single chromatography procedure, despite its elution occurs on multiple peaks. Although successful applications of hydrophobic interaction chromatography in purification of membrane proteins are uncommon, we proved that traditional hydrophobic matrices can open a promising unexplored field to fulfill specific requirements for kinetic and pharmacological trials.     

High‐Flux Membranes Based on the Covalent Organic Framework COF‐LZU1 for Selective Dye Separation by Nanofiltration

Covalent organic frameworks (COFs) are attractive candidates for advanced water‐treatment membranes owing to their high porosity and well‐organized channel structures. Herein, the continuous two‐dimensional imine‐linked COF‐LZU1 membrane with a thickness of only 400 nm was prepared on alumina tubes by in situ solvothermal synthesis. The membrane shows excellent water permeance (ca. 760 L m^?2 h^?1 MPa^?1) and favorable rejection rates exceeding 90 % for water‐soluble dyes larger than 1.2 nm. The water permeance through the COF‐LZU1 membrane is much higher than that of most membranes with similar rejection rates. Long‐time operation demonstrates the outstanding stability of the COF‐LZU1 membrane. As the membrane has no selectivity for hydrated salt ions (selectivity <12 %), it is also suitable for the purification of dye products from saline solutions. The excellent performance and the outstanding water stability render the COF‐LZU1 membrane an interesting system for water purification.     

Improved purification of immunoglobulin G from plasma by mixed‐mode chromatography

Efficient loading of immunoglobulin G in mixed‐mode chromatography is often a serious bottleneck in the chromatographic purification of immunoglobulin G. In this work, a mixed‐mode ligand, 4‐(1H‐imidazol‐1‐yl) aniline, was coupled to Sepharose Fast Flow to fabricate AN SepFF adsorbents with ligand densities of 15–64 mmol/L, and the chromatographic performances of these adsorbents were thoroughly investigated to identify a feasible approach to improve immunoglobulin G purification. The results indicate that a critical ligand density exists for immunoglobulin G on the AN SepFF adsorbents. Above the critical ligand density, the adsorbents showed superior selectivity to immunoglobulin G at high salt concentrations, and also exhibited much higher dynamic binding capacities. For immunoglobulin G purification, both the yield and binding capacity increased with adsorbent ligand density along with a decrease in purity. It is difficult to improve the binding capacity, purity, and yield of immunoglobulin G simultaneously in AN SepFF chromatography. By using tandem AN SepFF chromatography, a threefold increase in binding capacity as well as high purity and yield of immunoglobulin G were achieved. Therefore, the tandem chromatography demonstrates that AN SepFF adsorbent is a practical and feasible alternative to MEP HyperCel adsorbents for immunoglobulin G purification.     

An online coupled peritoneal macrophage/cell membrane chromatography and high‐performance liquid chromatography/mass spectrometry method to screen for anti‐inflammatory components from the Chinese traditional medicine Chloranthus multistachys Pei

Cell membrane chromatography (CMC) is a chromatographic biological affinity method that uses specific cell membranes as the stationary phase. In this study, a novel peritoneal macrophage/cell membrane chromatography (PM/CMC)–online‐high performance liquid chromatography/mass spectrometry (HPLC/MS) method was established to screen for the anti‐inflammatory components from traditional Chinese medicines using hydrocortisone and dexamethasone as standards. The stationary phase of the CMC employed mouse peritoneal macrophage cell membranes. This method was applied to the purification and identification of components in extracts of Chloranthus multistachys Pei. The major component retained by CMC was identified as isofraxidin by HPLC/MS. In vitro experiments revealed that IF was able to inhibit the production of nitric oxide and tumor necrosis factor‐α in lipopolysaccharide‐stimulated mice and peritoneal macrophages in a dose‐dependent manner. The results demonstrated that the PM/CMC‐online‐HPLC/MS is an effective screening system for the rapid detection, enrichment, and identification of target components from complex samples. Copyright © 2013 John Wiley & Sons, Ltd.     

Hydrogel membranes with mesh size asymmetry based on the gradient crosslinking of poly(vinyl alcohol)

Poly(vinyl alcohol) (PVA) hydrogel membranes with mesh size asymmetry were prepared and their transport properties were studied. Homogeneous membranes with water contents of 82%, 76% and 72% were prepared by crosslinking PVA with glutaraldehyde. These membranes were then modified to create asymmetry by establishing a glutaraldehyde concentration gradient across the hydrogel thickness. The reaction time and magnitude of the glutaraldehyde concentration gradient were varied to determine the optimum values of permeability and selectivity. Permeation experiments with creatinine, Fab and IgG were performed in a stirred diffusion cell through homogeneous and asymmetric PVA hydrogels. A modified version of the multiple-membrane technique was used to determine boundary layer resistance in order to determine the intrinsic membrane permeability. As expected, the selectivity of creatinine over IgG increased as the modification time increased. However, the selectivity of Fab over IgG initially increased as the modification time increased, but then decreased at longer times, indicating that the increased crosslinking at the surface effectively blocks both proteins. At a given value of IgG rejection, the asymmetric membranes had higher creatinine and Fab permeabilities than the corresponding homogeneous membranes. This indicates that creating mesh size asymmetry in a hydrogel can result in a high-flux, high-selectivity membrane for cell encapsulation or bioseparations.     

Surface‐initiated atom transfer radical polymerization from porous poly(tetrafluoroethylene) membranes using the C?F groups as initiators

This work reports the surface‐initiated atom transfer radical polymerization (ATRP) from hydrogen plasma‐treated porous poly(tetrafluoroethylene) (PTFE) membranes using the C? F groups as initiators. Hydrogen plasma treatment on PTFE membrane surfaces changes their chemical environment through defluorination and hydrogenation reactions. With the hydrogen plasma treatment, the C? F groups of the modified PTFE membrane surface become effective initiators of ATRP. Surface‐initiated ATRP of poly(ethylene glycol) methacrylate (PEGMA) is carried out to graft PPEGMA chains to PTFE membrane surfaces. The chain lengths of poly(PEGMA) (PPEGMA) grafted on PTFE surfaces increase with increasing the reaction time of ATRP. Furthermore, the chain ends of PPEGMA grown on PTFE membrane surfaces then serve as macroinitiators for the ATRP of N‐isopropylacrylamide (NIPAAm) to build up the PPEGMA‐b‐PNIPAAm block copolymer chains on the PTFE membrane surfaces. The chemical structures of the modified PTFE membranes are characterized using X‐ray photoelectron spectroscopy. The modification increases the surface hydrophilicity of the PTFE membranes with reductions in their water‐contact angles from 120° to 60°. The modified PTFE membranes also show temperature‐responsive properties and protein repulsion features owing to the presence of PNIPAAM and PPEGMA chains. © 2010 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 48: 2076–2083, 2010