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A new experimental set-up for on-line visualization of the intra-particle uptake kinetics during packed bed chromatography has been designed and tested. Confocal laser scanning microscopy was used to analyze the dynamics of protein adsorption to porous stationary phases. In combination with this, a flow cell was developed that could be packed with chromatography media and operated as a fully functional mini-scale chromatography column. Adsorption profiles of single- and two-component mixtures containing BSA and IgG 2a during packed bed cation-exchange chromatography were investigated. The two proteins appear to exhibit different transport characteristics. For BSA a classical "shrinking core" behavior could be detected. The profiles obtained during IgG 2a adsorption point toward a different transport mode, which deviates from the classical pore-diffusion picture. For the two-component system, a superposition of the single-component profiles combined with a classical displacement of the weaker bound protein species was found. The results indicate that depending on the adsorbed protein the uptake can vary tremendously, even for adsorption to the same chromatographic support. It is clearly shown that the new microcolumn allows in situ quantitative investigations of protein adsorption dynamics within a single particle, which adds a new tool to the available methods for characterizing and optimizing protein adsorption chromatography., (Copyright 2002 Wiley Periodicals, Inc.)

Expanded bed adsorption (EBA) is an integrated technology for the primary recovery of proteins from crude feedstock. Interactions between solid matter in the feed suspension and fluidised adsorbent particles influence bed stability and therefore have a significant impact on protein adsorption in expanded beds. In order to design efficient and reliable EBA processes a strategy is needed, which allows to find operating conditions, where these adverse events do not take place. In this paper a methodological approach is presented, which allows systematic characterisation and minimisation of cell/adsorbent interactions with as little experimental effort as possible. Adsorption of BSA to the anion exchanger Streamline Q XL from a suspension containing S. cerevisiae cells was chosen as a model system with a strong affinity of the biomass towards the stationary phase. Finite bath biomass adsorption experiments were developed as an initial screening method to estimate a potential interference. The adhesiveness of S. cerevisiae to the anion exchanger could be reduced significantly by increasing the conductivity of the feedstock. A biomass pulse response method was used to find optimal operation conditions showing no cell/adsorbent interactions. A good correlation was found between the finite bath test and the pulse experiment for a variety of suspensions (intact yeast cells, E. coli homogenate and hybridoma cells) and adsorbents (Streamline Q XL, DEAE and SP), which allows to predict cell/adsorbent interactions in expanded beds just from finite bath adsorption tests. Under the optimised operating conditions obtained using the prior methods, the stability of the expanded bed was investigated during fluidisation in biomass containing feedstock (up to 15% yeast on wet weight basis) employing residence time distribution analysis and evaluation by an advanced model. Based on these studies threshold values were defined for the individual experiments, which have to be achieved in order to obtain an efficient EBA process. Breakthrough experiments were conducted to characterise the efficiency of BSA adsorption from S. cerevisiae suspensions in EBA mode under varying operating conditions. This allowed to correlate the stability of the expanded bed with its sorption efficiency and therefore could be used to verify the threshold values defined. The approach presented in this work provides a fast and simple way to minimise cell/adsorbent interactions and to define a window of operation for protein purification using EBA.

The parameters important for an optimisation of cloud point extraction in technical scale were investigated using a genetically engineered fusion protein derived from endoglucanase I expressed in Trichoderma reesei and the nonionic polyoxyethylene Agrimul NRE 1205. The key parameters are temperature, detergent concentration, and additional salts. These parameters are interdependent, thus there is an optimum in the partition coefficient with respect to detergent concentration and a maximum for the partition coefficient and the yield with respect to temperature. These results were confirmed for the detergent C12E5 to demonstrate that these optima are due to the nature of polyoxyethylenes. Cloud point extraction was found to be only slightly affected by pH. In the case studied extraction of whole broth is favourable for a high yield and partition coefficient, since fusion protein adhering to the cells can be solubilized. However some loss of detergent which remains in the fungal biomass was observed.

The physical behavior of the binary phase systems of the non-ionic polyoxyethylene detergent Agrimul NRE 1205 and water was investigated. This technical detergent can be used for the large-scale recovery of biomolecules in detergent based aqueous two-phase systems. The phase diagram was determined. It shows significant and unexpected differences to highly purified detergents. Very similar to neat detergents the phase diagram can be influenced by auxiliary chemicals thus shifting the entire phase diagram in general to lower temperatures. This was demonstrated by lowering the cloud-point by various additions. The concentration factor, as an important parameter of a first capture step in purification was investigated and modeled. Auxiliary chemicals, temperature change and change in detergent concentration also influence the viscosity and density of the phases. These experimental data are shown. They can help to explain the separation behavior of proteins. In large-scale separations aqueous two-phase systems are separated using disc-stack centrifuges. It is demonstrated that this is not a feasible method for detergent-based aqueous two-phase extraction and the physical reason is presented.

Expanded bed adsorption (EBA) is an integrated technology for the primary recovery of proteins from unclarified feedstock. A method is presented which allows a qualitative and quantitative understanding of the main mechanisms governing the interaction of biomass with fluidized resins. A pulse response technique was used to determine the adsorption of various cell types (yeast, Gram positive and Gram negative bacteria, mammalian cells and yeast homogenate) to a range of commercially available matrices for EBA. Cells and cell debris were found to interact with the ligands of agarose based resins mainly by electrostatic forces. From the adsorbents investigated the anion exchange matrix showed the most severe interactions, while cation exchange and affinity adsorbents appeared to be less affected. Within the range of biologic systems under study E. coli cells had the lowest tendency of binding to all matrices while hybridoma cells attached to all the adsorbents except the protein A affinity matrix. The method presented may be employed for screening of suitable biomass/adsorbent combinations, which yield a robust and reliable initial capture step by expanded bed adsorption from unclarified feedstock.

The application of sodium dodecyl sulfate (SDS)-polymer capillary electrophoresis (CE) to the analysis of proteins of hybridoma cell culture supernatant is demonstrated. All steps of the developed analysis are shown and discussed. Following optimization of sample preparation and concentration, as well as of the mode of injection all main protein components were separated with high resolution and selectivity. Proteolytic degradation of IgG, due to microbial contamination, was observed on SDS-gel CE and capillary zone electrophoresis (CZE). The technique was applied to monitor the cell cultivation process and concentrations of main components are demonstrated. IgG was found to increase from initially 5 mg/L to 20 mg/L after 4 days and to > 130 mg/L after 14 days of cultivation. The techniques may be applied to other biotechnological processes for the production or purification of proteins.

Capillary sodium dodecyl sulfate (SDS) electrophoresis is a powerful and sensitive method for the qualitative and quantitative microanalysis of molecular mass for biopolymers. Usually, a separation is carried out in the long part of the capillary (20-50 cm), before the detection window, with separation times of 15-50 min. The separation of model proteins and real fractions of cell culture broth in the short part (7 cm) of the capillary, behind the window, was investigated. The analysis time could be reduced to less than 5 min. A comparison with established separation techniques is presented. Different modes of injection (by pressure and electrokinetic) were considered. The proposed method can be used for on-line monitoring of biotechnological processes.

Aqueous solutions of nonionic polyoxyethylene detergents form two liquid phases upon temperature increase above the cloud point. One of these phases is detergent-enriched and called the coacervate phase, whereas the other is detergent-depleted. Protein partitioning in such detergent-based aqueous two-phase systems was studied systematically and quantitatively, employing a series of similar polyoxyethylene detergents and proteins of varying hydrophobicity. Increasing the detergent alkyl chain length, temperature or salt concentration leads to an increase of detergent separating into the coacervate phase and a concomitant increase of protein. The positive correlation between protein hydrophobicity and partitioning into the coacervate phase confirms that protein-detergent interactions in such systems are primarily hydrophobic. These detergent-based systems can be applied to membrane proteins as well as water-soluble proteins which possess hydrophobic domains.

A purification method for formate dehydrogenase from Candida boidinii has been designed by using a sequence of membrane-based adsorbents. The membranes carrying ion-exchange and dye ligands (Sartobind) are general-purpose adsorbents for proteins. The membranes were used in an on/off mode. A sequence of cation exchange, dye-ligand and anion exchange allows to purify the enzyme as judged by SDS-PAGE and assay of specific activity. The sequence of ligands and the buffer conditions were chosen in such a way that the fraction eluted from one membrane could be directly loaded on the next membrane. Thereby an integrated version of MDLC was realized with membrane-based adsorbents. The excellent scaleability from micro- to laboratory scale (factor 40) indicates that the method could afford a general approach to develop purification trains since the micro-scale allows for a rapid screening of adsorbent types and sequences.

Polyethylene glycol (PEG)-oxirane was synthesized by reacting aminated monomethoxy-PEG 5000 (NH2-MPEG 5000) with butanediol diglycidyl ether and used to derivatize bovine serum albumin (BSA) and monoclonal antibodies (mAb) against horseradish peroxidase (HRP) and porcine lactate dehydrogenase isoenzyme 5, respectively. Determination of oxirane end groups revealed a very high number, which arise from the chain breaks of the polymer. Covalent coupling of PEG-oxirane to BSA resulted in 30-50 times higher partition coefficients under optimized conditions. The mAb investigated could be modified with PEG-oxirane while retaining its binding properties and could be used as an affinity ligand for selective extraction of Ag in immunoaffinity partitioning. However, a high degree of modification results in a lower binding constant of mAb anti-HRP and higher [mAb]/[Ag] concentration ratios in immunoaffinity partition experiments.

We report the partition coefficients of lysozyme, chymotrypsinogen-A, albumin and catalase in sixty four Polyethyleneglycol/Dextran/Water systems at 4, 25 and 40 degrees C. We found that the partition coefficients of the four proteins generally increase with increasing temperature. The influence of temperature on the partition coefficient seems to be highly dependent on the kind of protein which is partitioned and on the total polymer concentration, but does not, in general, depend on the molecular weight of the polymers. The partition coefficients of small and hydrophilic proteins like lysozyme and chymotrypsinogen-A are only slightly affected by changes in temperature, while the partition coefficients of bigger and more hydrophobic proteins like albumin and catalase are strongly affected by changes in temperature. The results suggest the incorporation of attractive forces (possible electrostatic) into a model previously reported by us.

Aqueous two-phase extraction systems were developed to separate intracellular proteins from cell debris. To economize on the use of chemicals as well as to minimize environmental pollution, a closed mode of operation was sought. Various approaches to achieve recycling of salt from the primary lower phase containing 30-60% (w/w) of the added salt together with cell debris, proteins and nucleic acids were studied. Techniques assessed included microfiltration, heat treatment and the extraction with phase systems formed by aliphatic alcohols. With 20% (w/w) primary lower phase it was found to be possible to separate 95% of the salt in 3-4 theoretical steps using counter-current extraction.

Microorganisms are a source of protein with catalytic and/or biological activity, which are of increasing commercial interest for applications in industry or therapy. For the isolation of intracellular products cell disruption is necessary. In principle, chemical, biological, or physical means may be employed to release proteins from cells. These different approaches are reviewed with special emphasis on scale-up and possible industrial operation. Mechanical devices have been improved considerably in recent years and appear most universally suited to cell disintegration. Chemical extraction or enzymatic lysis offers improved selectivity but requires individual procedures for each product. For a final process design, product yield and cost of the unit operation must be considered as well as the possible implications for the subsequent steps in product recovery, especially on solid/liquid separation.

Aqueous two-phase systems form the basis for an extraction technology of proteins. Trends in the development of the technology are reviewed and discussed with regard to future applications.

Desired proteins excreted by animal cells usually reach rather low concentrations in the culture supernatant and have to be purified from an excess of serum proteins which are added to the animal cell culture to maintain its viability and/or productivity. Defined media offer among others the advantage of an easier purification procedure. In addition lysis of cells may contribute also to the complexity of the protein mixture encountered. If fetal calf serum or new born calf serum is used in cultivation, bovine serum albumin and globulins will be the most abundant protein in the supernatant. The interaction of albumin especially with hydrophobic proteins represents significant problems for the effective purification of minor constituent. Isolation of a desired protein follows the general scheme: concentration: by precipitation, ultrafiltration, batch adsorption or partition in aqueous phase system; enrichment: by chromatography or partition; high resolution purification: by chromatography and/or immuno adsorption; final concentration and finishing: pyrogen removal, sterilization, formulation. Biochemical engineering aspects of proteins purification are discussed using human interferon-beta produced in a recombinant mouse cell line as an example. The process developed encloses extraction of interferon-beta from the production medium in aqueous two-phase systems and subsequent recovery of interferon-beta from the top phase by high pressure liquid chromatography.