Abstract: Herein is reported a method for producing a bispecific antibody comprising a first antigen-binding site that specifically binds to a first antigen and a second antigen-binding site that specifically binds to a second antigen comprising the following steps a) cultivating a cell comprising a nucleic acid encoding the bispecific antibody, b) recovering the bispecific antibody from the cell or the cultivation medium, c) contacting the bispecific antibody with an affinity chromatography material, d) washing the affinity chromatography material with a low conductivity aqueous solution, wherein the low conductivity aqueous solution has a conductivity value of about 0.5 mS/cm or less, e) recovering the bispecific antibody from the affinity chromatography material, f) performing a further chromatography step and thereby producing the bispecific antibody.

Abstract: For the removal of high molecular weight compounds from recombinantly produced polypeptides generally chromatographic methods are employed. It has been found that underivatized controlled pore glass (uCPG) selectively binds high molecular weight compounds present in a solution. The purified polypeptide can be recovered e.g. from the flow through of a chromatography column containing uCPG as chromatography material. It has been found that this effect is pronounced at a pH value of about 4 to 6 in buffered solutions. With approximately 100 m2 to 150 m2 uCPG surface per g of polypeptide almost 80% to 95% of the high molecular weight compounds are removed with a yield of 80% to 90% of polypeptide.

Abstract: The present invention provides methods of purifying multispecific antibodies. The methods comprise the sequential steps of performing a capture chromatography, a first mixed mode chromatography and a second mixed mode chromatography. In some aspects, the invention provides compositions of multispecific antibodies, which compositions have reduced levels of one or more product-specific impurities and/or process-specific impurities.

Abstract: Herein is reported a method for producing a bispecific antibody comprising a first antigen-binding site that specifically binds to a first antigen and a second antigen-binding site that specifically binds to a second antigen comprising the following steps a) cultivating a cell comprising a nucleic acid encoding the bispecific antibody, b) recovering the bispecific antibody from the cell or the cultivation medium, c) contacting the bispecific antibody with an affinity chromatography material, d) washing the affinity chromatography material with a low conductivity aqueous solution, wherein the low conductivity aqueous solution has a conductivity value of about 0.5 mS/cm or less, e) recovering the bispecific antibody from the affinity chromatography material, f) performing a further chromatography step and thereby producing the bispecific antibody.

Abstract: For the removal of high molecular weight compounds from recombinantly produced polypeptides generally chromatographic methods are employed. It has been found that underivatized controlled pore glass (uCPG) selectively binds high molecular weight compounds present in a solution. The purified polypeptide can be recovered e.g. from the flow through of a chromatography column containing uCPG as chromatography material. It has been found that this effect is pronounced at a pH value of about 4 to 6 in buffered solutions. With approximately 100 m2 to 150 m2 uCPG surface per g of polypeptide almost 80% to 95% of the high molecular weight compounds are removed with a yield of 80% to 90% of polypeptide.

Abstract: For the removal of high molecular weight compounds from recombinantly produced polypeptides generally chromatographic methods are employed. It has been found that underivatized controlled pore glass (uCPG) selectively binds high molecular weight compounds present in a solution. The purified polypeptide can be recovered e.g. from the flow through of a chromatography column containing uCPG as chromatography material. It has been found that this effect is pronounced at a pH value of about 4 to 6 in buffered solutions. With approximately 100 m2 to 150 m2 uCPG surface per g of polypeptide almost 80% to 95% of the high molecular weight compounds are removed with a yield of 80% to 90% of polypeptide.

Abstract: Herein is reported a tangential flow filtration method with a pre-filtration solute concentration adjustment in order to ensure a defined concentration of the components of the solution after tangential flow filtration.

Abstract: The current invention reports a method for concentrating an immunoglobulin solution by tangential flow filtration wherein the transmembrane pressure and the cross-flow are variable.

Abstract: The current invention reports a method for concentrating an immunoglobulin solution by tangential flow filtration wherein the transmembrane pressure and the cross-flow are variable.

Abstract: Herein is reported a tangential flow filtration method with a pre-filtration solute concentration adjustment in order to ensure a defined concentration of the components of the solution after tangential flow filtration.

Abstract: The current invention reports a method for concentrating an immunoglobulin solution by tangential flow filtration wherein the immunoglobulin in polymeric form can be removed after the concentration.

Abstract: The current invention reports a method for concentrating an immunoglobulin solution by tangential flow filtration wherein the transmembrane pressure and the cross-flow are variable.