Optimization of isopropanol and ammonium sulfate precipitation steps in the purification of plasmid DNA

Large-scale processes used to manufacture grams of plasmid DNA (pDNA) should be cGMP compliant, economically feasible, and environmentally friendly. Alcohol and salt precipitation techniques are frequently used in plasmid DNA (pDNA) downstream processing, as concentration and prepurification steps, respectively. This work describes a study of a standard 2-propanol (IsopOH; 0.7 v/v) and ammonium sulfate (AS; 2.5 M) precipitation. When inserted in a full process, this tandem precipitation scheme represents a high economic and environmental impact due to the large amounts of the two precipitant agents and their environmental relevance. Thus, major goals of the study were the minimization of precipitants and the selection of the best operating conditions for high pDNA recovery and purity. The pDNA concentration in the starting Escherichia coli alkaline lysate strongly affected the efficiency of IsopOH precipitation as a concentration step. The results showed that although an IsopOH concentration of at least 0.6 (v/v) was required to maximize recovery when using lysates with less than 80 microg pDNA/mL, concentrations as low as 0.4 v/v could be used with more concentrated lysates (170 microg pDNA/mL). Following resuspension of pDNA pellets generated by 0.6 v/v IsopOH, precipitation at 4 degrees C with 2.4 M AS consistently resulted in recoveries higher than 80% and in removal of more than 90% of the impurities (essentially RNA). An experimental design further indicated that AS concentrations could be reduced down to 2.0 M, resulting in an acceptable purity (21-23%) without compromising recovery (84-86%). Plasmid recovery and purity after the sequential IsopOH/AS precipitation could be further improved by increasing the concentration factor (CF) upon IsopOH precipitation from 2 up to 25. Under these conditions, IsopOH and AS concentrations of 0.60 v/v and 1.6 M resulted in high recovery (approximately 100%) and purity (32%). In conclusion, it is possible to reduce substantially the mass of precipitation agents used without affecting recovery, if a small concession is made regarding purity. This directly translates into an improvement of the process economics and in a reduction of the environmental impact of the process.     

Economic simulation of batch and continuous aqueous two-phase purification for viral products

Vaccine manufacturing strategies that lower capital and production costs could improve vaccine access by reducing the cost per dose and encouraging localized manufacturing. Continuous processing is increasingly utilized to drive lower costs in biological manufacturing by requiring fewer capital and operating resources. Aqueous two-phase systems (ATPS) are a liquid–liquid extraction technique that enables continuous processing for viral vectors. To date, no economic comparison between viral vector purifications using traditional methods and ATPS has been published. In this work, economic simulations of traditional chromatography-based virus purification were compared to ATPS-based virus purification for the same product output in both batch and continuous modes. First, the modeling strategy was validated by re-creating a viral subunit manufacturing economic simulation. Then, ATPS capital and operating costs were compared to that of a traditional chromatography purification at multiple scales. At all scales, ATPS purification required less than 10% of the capital expenditure compared to chromatography-based purification. At an 11 kg per year production scale, the ATPS production costs were 50% less than purification with chromatography. Other chromatography configurations were explored, and may provide a production cost benefit to ATPS, but the purity and recovery were not experimentally verified. Batch and continuous ATPS were similar in capital and production costs. However, manual price adjustments suggest that continuous ATPS plant-building costs could be less than half that of batch ATPS at the 11 kg per year production scale. These simulations show the significant reduction in manufacturing costs that ATPS-based purification could deliver to the vaccine industry.     

Downstream processing of human antibodies integrating an extraction capture step and cation exchange chromatography

In this paper we explore an alternative process for the purification of human antibodies from a Chinese hamster ovary (CHO) cell supernatant comprising a ligand-enhanced extraction capture step and cation exchange chromatography (CEX). The extraction of human antibodies was performed in an aqueous two-phase system (ATPS) composed of dextran and polyethylene glycol (PEG), in which the terminal hydroxyl groups of the PEG molecule were modified with an amino acid mimetic ligand in order to enhance the partition of the antibodies to the PEG-rich phase. This capture step was optimized using a design of experiments and a central composite design allowed the determination of the conditions that favor the partition of the antibodies to the phase containing the PEG diglutaric acid (PEG-GA) polymer, in terms of system composition. Accordingly, higher recovery yields were obtained for higher concentrations of PEG-GA and lower concentrations of dextran. The highest yield experimentally obtained was observed for an ATPS composed of 5.17% (w/w) dextran and 8% (w/w) PEG-GA. Higher purities were however predicted for higher concentrations of both polymers. A compromise between yield and purity was achieved using 5% dextran and 10% PEG-GA, which allowed the recovery of 82% of the antibodies with a protein purity of 96% and a total purity of 63%, determined by size-exclusion chromatography. ATPS top phases were further purified by cation exchange chromatography and it was observed that the most adequate cation exchange ligand was carboxymethyl, as the sulfopropyl ligand induced the formation of multi-aggregates or denatured forms. This column allowed the elution of 89% of the antibodies present in the top phase, with a protein purity of 100% and a total purity of 91%. The overall process containing a ligand-enhanced extraction step and a cation exchange chromatography step had an overall yield of 73%.     

The potential application of aqueous two-phase systems for in situ recovery of 6-pentyl-infinity-pyrone produced by Trichoderma harzianum

Commercial production of aroma compounds by de novo microbial biosynthesis has been principally limited by the low productivity so far achieved. Production of 6-pentyl-alpha-pyrone (6PP), a coconut-like aroma compound, by Trichoderma harzianum has been limited by the toxic effect that occurs even at low concentration (<100 ppm). This work evaluated the feasibility of the use of aqueous-two phase systems (ATPS), as in situ extraction systems, in order to overcome the toxic effects of 6PP and to improve culture productivity. The partition behaviour of 6-pentyl-alpha-pyrone and Trichoderma harzianum mycelium in polyethylene glycol (PEG)-salt and PEG-dextran two-phase systems was investigated and it is reported for the first time. The evaluation of system parameters such as PEG molecular mass, concentration of PEG as well as salt, volume ratio (Vr) and dextran molecular mass, was carried out to determine under which conditions the 6PP partitions to the opposite phase that mycelium does. PEG-dextran systems proved to be unsuitable for the in situ recovery of 6PP because either 6PP and biomass partitioned to the same phase or a large extraction phase was required for the process. ATPS extraction comprising Vr = 0.26, PEG 1450 (7.2% w/w) and sulphate (16.6% w/w) provided the best conditions for the maximum accumulation of the biomass into the bottom phase and concentrated the 6PP in the opposite phase (i.e. 86% of biomass and 56% of 6PP of the total amount loaded from the fermentation extract into the ATPS) for ex situ bioseparation. However, this system caused complete inhibition of the growth of the microorganism during the in situ bioseparation, probably as a consequence of the high ionic strength resulting from the salt concentration. Consequently, two ATPS PEG 8000-sulphate (12%/7% and 6%/14%) were evaluated and proved to be more suitable in the potential application for the in situ recovery of 6PP.     

Technical improvement in the purification of enzymes from red algae using an aqueous two-phase partitioning system

The effective elimination of phycobiliproteins from crude enzyme preparation of the red alga Caloglossa continua (Okamura) King et Puttock (Ceramiales, Florideophyceae) was investigated in an aqueous two‐phase partitioning system (ATPS) by changing the concentrations of polyethylene glycol (PEG) and ammonium sulfate (AS). The phycobiliproteins shifted from the AS‐rich lower phase to the PEG‐rich upper phase in high PEG and AS concentrations. The best ATPS condition for the elimination of phycobiliproteins from the lower phase was obtained by the combination of 20% (weight/volume; w/v) PEG and 16% (w/v) AS. However, the recovery of aldolase and mannitol‐1‐phos‐phatase activities was significantly reduced. For purification of the enzymes, a combination of 15% (w/v) PEG and 16% (w/v) AS was the best ATPS condition, because a high specific activity and recovery of the enzymes were obtained. Under these conditions, 98% of the phycobiliproteins were removed from the lower phase. Therefore, the ATPS proved to be a very useful method as a first step in the purification of enzymes from red algae.     

Bioprocess intensification: a potential aqueous two-phase process for the primary recovery of B-phycoerythrin from Porphyridium cruentum

A process for the primary recovery of B-phycoerythrin from Porphyridium cruentum exploiting aqueous two-phase systems (ATPS) was developed in order to reduce the number of unit operations and benefit from an increased yield of the protein product. The evaluation of system parameters such as poly(ethylene glycol) (PEG) molecular mass, concentration of PEG as well as salt, system pH and volume ratio was carried out to determine under which conditions the B-phycoerythrin and contaminants concentrate to opposite phases. PEG 1450-phosphate ATPS proved to be suitable for the recovery of B-phycoerythrin because the target protein concentrated to the top phase whilst the protein contaminants and cell debris concentrated in the bottom phase. An extraction ATPS stage comprising volume ratio (Vr) equal to 1.0, PEG 1450 24.9% (w/w), phosphate 12.6% (w/w) and system pH of 8.0 allowed B-phycoerythrin recovery with a purity of 2.9 (estimated as the relation of the 545-280 nm absorbances). The use of ATPS resulted in a primary recovery process that produced a protein purity of 2.9 +/- 0.2 and an overall product yield of 77.0% (w/w). The results reported demonstrated the practical implementation of ATPS for the design of a primary recovery process as a first step for the commercial purification of B-phycoerythrin produced by P. cruentum.     

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.     

Individualizing the aorto-radial pressure transfer function: feasibility of a model-based approach

We fitted a three-segment transmission line model for the radial-carotid/aorta pressure transfer function (TFF) in 31 controls and 30 patients with coronary artery disease using noninvasively measured (tonometry) radial and carotid artery pressures (P(car)). Except for the distal reflection coefficient (0.85 +/- 0.21 in patients vs. 0.71 +/- 0.25 in controls; P < 0.05), model parameters were not different between patients or controls. Parameters were not related to blood pressure, age, or heart rate. We further assessed a point-to-point averaged TFF (TFF(avg)) as well as upper (TFF(max)) and lower (TFF(min)) enveloping TFF. Pulse pressure (PP) and augmentation index (AIx) were derived on original and reconstructed P(car) (P(car,r)). TFF(avg) yielded closest morphological agreement between P(car) and P(car,r) (root mean square = 4.3 +/- 2.3 mmHg), and TTF(avg) best predicted PP (41.5 +/- 11.8 vs. 41.1 +/- 10.0 mmHg measured) and AIx (-0.02 +/- 0.19 vs. 0.01 +/- 0.19). PP and AIx, calculated from P(car) or P(car,r), were higher in patients than in controls, irrespectively of the TFF used. We conclude that 1) averaged TFF yield significant discrepancies between reconstructed and measured pressure waveforms and subsequent derived AIx; and 2) different TFFs seem to preserve the information in the pressure wave that discriminates between controls and patients.     

A study on the use of caprylic acid and ammonium sulfate in combination for the fractionation of equine antivenom F(ab')(2)

This study involved the fractionation of equine antivenom F(ab′)₂ by combined stepwise ammonium sulfate (AS) and caprylic acid (CA) precipitation without intermediate separation of precipitate. Using a microplate format, 55 conditions with combinations of AS (0–20% saturation) and CA (0–5% v/v), were tested. AS significantly reduced the turbidity raised by CA. High specific antibody activity was observed in the area containing 2–5% CA and 10–20% AS. From these results, 12 precipitation conditions were selected for detailed quantitative studies. Two combinations, one with 4% CA and 15% AS and another with 5% CA and 20% AS, gave the highest fold-purification (1.79 and 1.83) with antibody recoveries at 68% and 59%, respectively. These combinations offered a benefit over CA alone in reducing the turbidity and in increasing the purity but not the recovery of antibody. The conditions giving more favorable overall results were with 2% CA alone and another with a combination of 1.5% CA and 10% AS. These preparations of F(ab′)₂ were homogeneous and without protein aggregate under size-exclusion HPLC. Lastly, 1 h precipitation showed better results than those of overnight precipitation. These results could be useful for the production of therapeutic antivenoms.     

Two-step process for initial capture of plasmid DNA and partial removal of RNA using aqueous two-phase systems

In this paper, a two-step process for initial capture of plasmid DNA (pDNA) and partial removal of RNA using polyethylene glycol (PEG) and di-potassium hydrogen phosphate aqueous two-phase systems (ATPS) has been investigated. A Kühni-type ATPS extraction column was prepared with 50 ml (12% (w/w) PEG 1450, 12% (w/w) phosphate) of stationary phase and loaded with crude mobile phase (26% (w/w) PEG 1450, 4% (w/w) phosphate and 70% (w/w) lysate) at a flow rate of 6 ml min⁻¹ at an impeller speed of 200 rpm. The experiment was terminated after 100 min, and after complete resettling of the phases, 45 ml of stationary phase was harvested. During a subsequent second extraction step contained 18% (w/w) PEG 300 and 14% (w/w) phosphate, a proportion of RNA, which was also concentrated during the column process, was removed. It was demonstrated that the recovery of pDNA in the second bottom phase was 89.4%, which was similar to the initial recovery after column extraction (92.1%).     

中国有机肥料养分资源潜力和环境风险分析

基于<中国农业年鉴2006)和其他文献的基础数据,计算了2005年中国人畜禽排泄物和秸秆数量及其产生的养分量.结果表明,2005年中国人畜禽排泄物总量为46.25亿t,秸秆总产量为6.43亿t.中国有机肥料养分资源潜力巨大,2005年人畜禽排泄物和秸秆共产生N、P2O5、K2O养分量分别为2824.52、1282.93、2947.99万t,分别为化肥N、P2O5、K2O投入量的1.08、0.86和4.56倍.但不同区域差异较大,其中河南、山东和四川省人畜禽排泄物产生N、P2O5、K2O量最多,均>400万t,西北地区和北京、天津、上海等地人畜禽排泄物产生的养分总量较少.秸秆中N、P2O5、K2O含量在河南和山东2个粮食主产省最高,均>150万t;西北地区秸秆养分产生量相对较少.单位农田面积人畜禽排泄物的N、P2O5和K2O养分负荷量以北京最高,达到787.26 kg·hm-2,其次是天津和上海,分别为515.31和505.35 kg·hm-2,环境风险较大.     

Affinity separation by protein conjugated IgG in aqueous two-phase systems using horseradish peroxidase as a ligand carrier

A novel affinity separation method in an aqueous two-phase system (ATPS) is suggested, using protein conjugated IgG as a ligand. For verification of the proposed approach, horseradish peroxidase (HRP) and human IgG was used as a ligand carrier and affinity ligand, respectively. The partition of the affinity ligand, human IgG, was controlled by the conjugation of HRP. Two ATPSs, one consisting of potassium phosphate (15%, w/w) and polyethylene glycol (PEG, M.W. 1450, 10%, w/w) and the other of dextran T500 (5%, w/w) and PEG (M.W. 8000, 5%, w/w), were used. The conjugated human IgG-HRP favored a PEG-rich top phase, whereas human IgG, rabbit anti-human IgG and goat anti-mouse IgG preferred a salt or dextran-rich bottom phase. Using the conjugated human IgG-HRP, rabbit anti-human IgG was successfully separated into a PEG-rich top phase from the mixture with goat anti-mouse IgG. The appropriate molar ratio between human IgG-HRP and rabbit anti-human IgG was around 3:1 and 1:1 for the salt and dextran-based ATPS, respectively. The dextran-based ATPS showed a better recovery yield and purity than the salt-based ATPS for the range of test conditions employed in this experiment. The yield and purity of the recovered rabbit anti-human IgG were 90.8 and 87.7%, respectively, in the dextran-based ATPS, while those in the salt-based ATPS were 78.2 and 73.2%.     

Rotavirus-like particles primary recovery from insect cells in aqueous two-phase systems

Virus-like particles have a wide range of applications, including vaccination, gene therapy, and even as nanomaterials. Their successful utilization depends on the availability of selective and scalable methods of product recovery and purification that integrate effectively with upstream operations. In this work, a strategy based on aqueous two phase system (ATPS) was developed for the recovery of double-layered rotavirus-like particles (dlRLP) produced by the insect cell-baculovirus expression system. Polyethylene glycol (PEG) molecular mass, PEG and salt concentrations, and volume ratio (Vr, volume of top phase/volume of bottom phase) were evaluated in order to determine the conditions where dlRLP and contaminants concentrated to opposite phases. Two-stage ATPS consisting of PEG 400-phosphate with a Vr of 13.0 and a tie-line length (TLL) of 35% (w/w) at pH 7.0 provided the best conditions for processing highly concentrated crude extract from disrupted cells (dlRLP concentration of 5 microg/mL). In such conditions intracellular dlRLP accumulated in the top phase (recovery of 90%), whereas cell debris remained in the interface. Furthermore, dlRLP from culture supernatants accumulated preferentially in the interface (recovery of 82%) using ATPS with a Vr of 1.0, pH of 7.0, PEG 3350 (10.1%, w/w) and phosphate (10.9%, w/w). The purity of dlRLP from culture supernatant increased up to 55 times after ATPS. The use of ATPS resulted in a recovery process that produced dlRLP with a purity between 6 and 11% and an overall product yield of 85% (w/w), considering purification from intracellular and extracellular dlRLP. Overall, the strategy proposed in this study is simpler than traditional methods for recovering dlRLP, and represents a scalable and economically viable alternative for production processes of vaccines against rotavirus infection with significant scope for generic commercial application.     

Purification and Characterization of Polyphenol Oxidase From Waste Potato Peel by Aqueous Two-Phase Extraction

Potato peel from food industrial waste is a good source of polyphenol oxidase (PPO). This work illustrates the application of an aqueous two-phase system (ATPS) for the extraction and purification of PPO from potato peel. ATPS was composed of polyethylene glycol (PEG) and potassium phosphate buffer. Effect of different process parameters, namely, PEG, potassium phosphate buffer, NaCl concentration, and pH of the system, on partition coefficient, purification factor, and yield of PPO enzyme were evaluated. Response surface methodology (RSM) was utilized as a statistical tool for the optimization of ATPS. Optimized experimental conditions were found to be PEG1500 17.62% (w/w), potassium phosphate buffer 15.11% (w/w), and NaCl 2.08 mM at pH 7. At optimized condition, maximum partition coefficient, purification factor, and yield were found to be 3.7, 4.5, and 77.8%, respectively. After partial purification of PPO from ATPS, further purification was done by gel chromatography where its purity was increased up to 12.6-fold. The purified PPO enzyme was characterized by sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE), followed by K_m value 3.3 mM, and V_max value 3333 U/mL, and enzyme stable ranges for temperature and pH of PPO were determined. These results revealed that ATPS would be an attractive option for obtaining purified PPO from waste potato peel.     

Environmental impact assessment of centralized municipal wastewater management in Thailand

Purpose

Urbanization and industrial development intensify water utilization and wastewater generation. The efficiency of wastewater treatment systems varies and depends on system design and wastewater condition. The research aims to examine seven existing centralized municipal wastewater treatment plants (WWTPs) in Bangkok to discover which system configuration yields the best environmental and economic performance. The degree of environmental impact and operational costs from different system designs were investigated to help select future wastewater treatment systems.

Methods

Life cycle assessment (LCA) has been conducted to evaluate environmental impacts from centralized municipal wastewater treatment systems. Life cycle impact assessment method based on endpoint modeling (LIME) was applied, with three major potential environmental impact categories including eutrophication, global warming, and acidification. All seven centralized municipal WWTPs in Bangkok were investigated as case studies. The system configurations are classified into five types of activated sludge (AS) systems. The contribution of impacts from individual processes in each type of AS system was analyzed. The methodology covered major on-site and off-site operational processes excluding construction and maintenance phases. Average annual data were calculated to develop an inventory dataset. JEMAI-Pro software was utilized in this study to analyze the life cycle impact of the systems.

Results and discussion

The level of environmental impact from a WWTP depends on the configuration of the AS system. The highest potential environmental impact from a municipal WWTP is eutrophication, which is obviously affected by ammonium and phosphorous discharges into water bodies. The vertical loop reactor activated sludge (VLRAS) system yielded the best treatment performance among the five AS sub-systems. The consumption of electricity used to operate the system contributed significantly to global warming potential and correlated considerably with operating costs. Comparing among three system sizes, the large-scale WWTP revealed inefficient electricity consumption, whereas the medium plant provided better performance in chemical use and operating costs.

Conclusions

Centralized municipal WWTPs with capacities ranging from 10 to 350?×?10³ m³/day were evaluated with respect to environmental performance and costs during the operating phase. Among all case studies, a medium-scale WWTP with a VLRAS system offered the best operating performance in terms of low environmental impact, resource consumption, and cost. To enhance WWTP management, it is vital to improve the efficiency of electricity consumption in primary and secondary treatment processes and increase wastewater collection efficiency to maximize the plant operating capacity and minimize overall environmental impacts.

     

Partitioning of protease from stomach of albacore tuna (Thunnus alalunga) by aqueous two-phase systems

Partitioning of protease from stomach of albacore tuna using an aqueous two-phase system (ATPS) was investigated. The best ATPS conditions for protease partitioning from stomach extract (SE) and acidified counterpart (ASE) were 25% PEG1000–20% MgSO₄ and 15% PEG2000–15% MgSO₄, which increased the purity by 7.2-fold and 2.4-fold with the recovered activity of 85.7% and 89.1%, respectively. Electrophoretic study revealed that SE had a major protein with a molecular weight (MW) of 40.6 kDa, while protein with MW of 32.7 kDa was predominant in ASE and ATPS fractions. Pepsinogen in SE might be activated to pepsin by acidification and partitioning process. SE was quite stable at 0 and 4 °C up to 14 days. The loss in protease activity in ASE and selected ATPS fractions was more pronounced when storage time and temperature increased. Therefore, ATPS can be effectively used to recover and purify protease from albacore tuna stomach.     

Microalgae production: technical and economic evaluations

A review of the various literature data for large-scale algae production costs is described. Costs were updated and recomputed in order to compare the different schemes. Total production costs of a nonprocessed biomass range from US$0.15 to US$4.0 kg(-1), according to various authors. Process performance hypotheses and proposed technologies are analyzed to explain these variations. A cost analysis for a tubular bioreactor system is then presented that shows that, assuming a productivity of 60 tons/ha yr, production costs would range from FF24 to FF29 kg(-1) for such a system. Operating costs as well as fixed charges account for approximately 50% of the cost. Parametric sensitivity of these costs is then analyzed: If productivity would be 30, 45, or 90 tons/ha yr, total cost would be around FF48, FF33 and FF19 kg(-1). Advantages and disadvantages of the proposed tubular technology are finally discussed.     

Purification of IgG and albumin from human plasma by aqueous two phase system fractionation

The current shortages in human plasma products at global levels justify the development of new, cost effective plasma fractionation methods. We have developed a fractionation process to obtain immunoglobulin G (IgG) and albumin‐enriched fractions based on polymer‐salt aqueous two phase system (ATPS). A small‐scale (0.02 L) ATPS composed of polyethyleneglycol 3350 (PEG), potassium phosphate and sodium chloride, at pH 6.1, was evaluated and subjected to 50‐fold scale‐up (1 L). Further purification of the fractions was performed using caprylic acid precipitation and ion exchange chromatography. Similar yield and purity were obtained at both small and large scales. IgG precipitated in the PEG rich upper phase at 83% recovery and 2.75‐fold purification factor. An 81% pure albumin fraction was obtained in the salt rich bottom phase with a 91% yield. After polishing, IgG was obtained at a recovery of 70% and a purity of 92%. Corresponding values for albumin were 91% and 90%. This IgG and albumin fractionation technology deserves further evaluation as it may represent a potential alternative to conventional plasma fractionation methods. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 28: 1005–1011, 2012     

Application of a PEG/salt aqueous two-phase partition system for the recovery of monoclonal antibodies from unclarified transgenic tobacco extract

Aqueous two-phase partition systems (ATPS) have been widely used for the separation of a large variety of biomolecules. In the present report, the application of a polyethylene glycol/phosphate (PEG/phosphate) ATPS for the separation of anti-HIV monoclonal antibodies 2G12 (mAb 2G12) and 4E10 (mAb 4E10) from unclarified transgenic tobacco crude extract was investigated. Optimal conditions that favor opposite phase partitioning of plant debris/mAb as well as high recovery and purification were found to be 13.1% w/w (PEG 1500), 12.5% w/w (phosphate) at pH 5 with a phase ratio of 1.3 and 8.25% w/w unclarified tobacco extract load. Under these conditions, mAb 2G12 and mAb 4E10 were partitioned at the bottom phosphate phase with 85 and 84% yield and 2.4- and 2.1-fold purification, respectively. The proposed ATPS was successfully integrated in an affinity-based purification protocol, using Protein A, yielding antibodies of high purity and yield. In this study, ATPS was shown to be suitable for initial protein recovery and partial purification of mAb from unclarified transgenic tobacco crude extract.     

Naked Plasmid DNA Formulation: Effect of Different Disaccharides on Stability after Lyophilisation

Since plasmid DNA (pDNA) is unstable in solution, lyophilisation can be used to increase product shelf life. To prevent stress on pDNA molecules during lyophilisation, cryo- and lyoprotectants have to be added to the formulation. This study assessed the effect of disaccharides on naked pDNA stability after lyophilisation using accelerated stability studies. Naked pDNA was lyophilised with sucrose, trehalose, maltose or lactose in an excipient/DNA w/w ratio of 20. To one part of the vials extra residual moisture was introduced by placing the vials half opened in a 25°C/60% RH climate chamber, before placing all vials in climate chambers (25°C/60% RH and 40°C/75% RH) for stability studies. An ex vivo human skin model was used to assess the effect of disaccharides on transfection efficiency. Lyophilisation resulted in amorphous cakes for all disaccharides with a residual water content of 0.8% w/w. Storage at 40°C/75% RH resulted in decreasing supercoiled (SC) purity levels (sucrose and trehalose maintained approximately 80% SC purity), but not in physical collapse. The addition of residual moisture (values between 7.5% and 10% w/w) resulted in rapid collapse except for trehalose and decreasing SC purity for all formulations. In a separate experiment disaccharide formulation solutions show a slight but significant reduction (<3% with sucrose and maltose) in transfection efficiency when compared to pDNA dissolved in water. We demonstrate that disaccharides, like sucrose and trehalose, are effective lyoprotectants for naked pDNA.