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In this work we present a general procedure for the model-based optimization of a polypeptide crude mixture purification process through its application to a case of industrial relevance.
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Efforts to determine the effects of pollutants in a mixture during the water purification process should be enhanced, in particular for enzyme-mediated processes.
This biofuel mixture currently named Ecodiesel is able to directly operate diesel engines, alone or in whichever mixture with diesel fuel, without anymore separation or purification process.
A two-dimensional un-steady reaction model which includes both physical adsorption and catalytic reaction process was developed for binary gas mixture purification in fixed-bed.
This work proposes methodologies using a model-based approach to gain knowledge on and assist the development of an ion-exchange step in a protein purification process; the separation of IgG from a mixture containing IgG, insulin and transferrin.
We used 250 μL of QIA buffer PE to carry out the purification process for 50 μL of the ligation mixture.
A method using a model-based approach to design and optimize an ion-exchange step in a protein purification process is proposed for the separation of IgG from a mixture containing IgG, BSA and myoglobin.
Additionally, HSA exhibits structural heterogeneity and batch-to-batch variability; its pharmacopoeial purity requirement is only ≥ 96%, with the undesired components being a mixture of polymers of HSA and other contaminating plasma proteins remaining from the purification process [ 54].
A multi-step purification process to separate metal catalysts and their support materials from mixtures of straight and spiral multi-walled carbon nanotubes (MWNTs), synthesised via fluidised-bed chemical vapour deposition (CVD) is described.
This purification process efficiently recovers highly active rFIX and shows that even complex mixtures like pig milk, which contains 60 g/l total endogenous milk protein and multiple subpopulations of rFIX, can be processed using conventional, non-immunoaffinity chromatographic methods.
Overall, a simple and steady small-batch purification process for the large-scale production of 25(R -OCH3-PPD fR -OCH3-PPD-PPD epimeR -OCH3-PPD was developed.
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