The direct capture of bacteria produced in high cell density fermentation by filtration is not possible once the milliliter-scale has been surpassed. Filtration in the presence of a filter aid (body feed filtration) constitutes a putative and scalable alternative, but only if conditions proposed by industry for large-scale filtration processes, namely, flow rates (for aqueous solutions) in the range of 500-1,500 L/(m(2) x h) and a filter aid concentration of
Combining capture and lysis of the bacteria with partial purification of the plasmid DNA is beneficial for the design of efficient plasmid production processes at larger scale. Such an approach is possible when the bacteria are captured by filtration. Taking industrial requirements into account, however, such a capture requires complex filtration mixtures containing retentive additives such as bentonite and polycations. This makes the straightforward transfer of established lysis protocols to in situ lysis difficult. In this contribution, the different steps of such a protocol are designed for complex filter cakes, including fragilization (by lysozyme), lysis (alkaline pH/acidic pH, 70/37 degrees C, urea/NaCl/Triton), and specific elution (pH, NaCl, CaCl2, guanidinium hydrochloride). Results are compared in regard to plasmid quality (topoisomeric form) and quantity (compared to the yield obtained by a commercial miniprep of a small aliquot of the bacteria suspension from the bioreactor). Best results in these terms were obtained by the Triton lysis protocol performed at 37 degrees C (30 min of contact with a lysis buffer composed of 50 mM Tris pH 8, 1% Triton, 1 g/L lysozyme, and 6 M guanidinium hydrochloride) followed by the specific elution of the plasmid DNA in 50 mM Tris buffer pH 8.
Combining capture and lysis of the bacteria with partial purification of the plasmid DNA is beneficial for the design of efficient plasmid production processes at larger scale. Such an approach is possible when the bacteria are captured by filtration. Taking industrial requirements into account, however, such a capture requires complex filtration mixtures containing retentive additives such as bentonite and polycations. This makes the straightforward transfer of established lysis protocols to in situ lysis difficult. In this contribution, the different steps of such a protocol are designed for complex filter cakes, including fragilization (by lysozyme), lysis (alkaline pH/acidic pH, 70/37 degrees C, urea/NaCl/Triton), and specific elution (pH, NaCl, CaCl2, guanidinium hydrochloride). Results are compared in regard to plasmid quality (topoisomeric form) and quantity (compared to the yield obtained by a commercial miniprep of a small aliquot of the bacteria suspension from the bioreactor). Best results in these terms were obtained by the Triton lysis protocol performed at 37 degrees C (30 min of contact with a lysis buffer composed of 50 mM Tris pH 8, 1% Triton, 1 g/L lysozyme, and 6 M guanidinium hydrochloride) followed by the specific elution of the plasmid DNA in 50 mM Tris buffer pH 8.
To enhance the performance of organic devices, doping and graded mixed‐layer structures, formed by co‐evaporation methods, have been extensively adopted in the formation of organic thin films. Among the criteria for selecting materials systems, much attention has been paid to the materials' energy‐band structure and carrier‐transport behavior. As a result, some other important characteristics may have been overlooked, such as material compatibility or solubility. In this paper, we propose a new doping method utilizing fused organic solid solutions (FOSSs) which are prepared via high‐pressure and high‐temperature processing. By preparing fused solid solutions of organic compounds, the stable materials systems can be selected for device fabrication. Furthermore, by using these FOSSs, doping concentration and uniformity can be precisely controlled using only one thermal source. As an example of application in organic thin films, high‐performance organic light‐emitting diodes with both single‐color and white‐light emission have been prepared using this new method. Compared to the traditional co‐evaporation method, a FOSS provides us with a more convenient way to optimize the doping system and fabricate relatively complicated organic devices.
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