Abstract: A method for obtaining Alpha-1 Proteinase Inhibitor for obtaining highly-concentrated Alpha-1 Proteinase Inhibitor (A1PI) includes preparing a solution of A1PI by concentrating an initial solution of A1PI by tangential flow filtration (TFF) against water. The final concentration of A1PI in the concentrated solution is at least 110 mg/ml. The TFF can be carried out against water for injection (WFD).

Abstract: Disclosed is both a method for preparing a plasminogen and a method for preparing a reversibly inactive acidified plasmin by activating the plasminogen. The prepared plasminogen is typically purified from a fraction obtained in the separation of immunoglobulin from Fraction II+III chromatographic process and eluted at a low pH. The prepared plasmin is isolated and stored with a low pH-buffering capacity agent to provide a substantially stable formulation. The reversibly inactive acidified plasmin may be used in the administration of a thrombolytic therapy.

Abstract: Disclosed is both a method for preparing a plasminogen and a method for preparing a reversibly inactive acidified plasmin by activating the plasminogen. The prepared plasminogen is typically purified from a fraction obtained in the separation of immunoglobulin from Fraction II+III chromatographic process and eluted at a low pH. The prepared plasmin is isolated and stored with a low pH-buffering capacity agent to provide a substantially stable formulation. The reversibly inactive acidified plasmin may be used in the administration of a thrombolytic therapy.

Abstract: Disclosed is both a process for producing a reversibly inactive acidified plasmin by activating plasminogen and a process for producing a purified plasminogen. The produced plasmin is isolated and stored with a low pH-buffering capacity agent to provide a substantially stable formulation. The purified plasminogen is typically purified from a fraction obtained in the separation of immunoglobulin from Fraction II+III chromatographic process and eluted at a low pH. The reversibly inactive acidified plasmin may be used in the administration of a thrombolytic therapy.

Abstract: Disclosed is both a process for producing a reversibly inactive acidified plasmin by activating plasminogen and a process for producing a purified plasminogen. The produced plasmin is isolated and stored with a low pH-buffering capacity agent to provide a substantially stable formulation. The purified plasminogen is typically purified from a fraction obtained in the separation of immunoglobulin from Fraction II+III chromatographic process and eluted at a low pH. The reversibly inactive acidified plasmin may be used in the administration of a thrombolytic therapy.