초록 ▼

A process is provided for selectively removing protein aggregates from a protein solution in a normal flow (NFF) filtration process. Preferably, it relates to a process for selectively removing protein aggregates from a protein solution in a normal flow (NFF) filtration process and virus particles f

A process is provided for selectively removing protein aggregates from a protein solution in a normal flow (NFF) filtration process. Preferably, it relates to a process for selectively removing protein aggregates from a protein solution in a normal flow (NFF) filtration process and virus particles from a protein solution in a two-step filtration process. In a first step, a protein solution is filtered through one or more layers of adsorptive depth filters, charged or surface modified microporous membranes or a small bed of chromatography media in a normal flow filtration mode of operation, to produce a protein aggregate free stream. The aggregate free protein stream can then be filtered through one or more ultrafiltration membranes to retain virus particles at a retention level of at least 3 LRV and to allow passage therethrough of an aggregate free and virus free protein solution.

대표청구항 ▼

The invention claimed is: 1. A process for selectively removing protein aggregates and virus particles from an aqueous solution of proteins that consists essentially of: first filtering a protein solution containing said protein aggregates and viruses through a device selected from the group consis

The invention claimed is: 1. A process for selectively removing protein aggregates and virus particles from an aqueous solution of proteins that consists essentially of: first filtering a protein solution containing said protein aggregates and viruses through a device selected from the group consisting of one or more layers of adsorptive depth filters and one or more layers of charged or surface modified microporous membranes, in a normal flow filtration mode of operation, recovering the aggregate free protein solution, and secondly filtering said aggregate free protein solution through one or more ultrafiltration membranes having a molecular weight cut off of between about 200 kD and about 1000 kD to retain virus particles in said one or more ultrafiltration membranes at a level of at least 3 LRV, and to recover an aqueous, virus-free protein solution. 2. The process of claim 1 that includes the further step of flushing retained protein from said one or more ultrafiltration membranes. 3. The process of claim 1 wherein the first filtration step is through one or more layers of charged microporous membranes. 4. The process of claim 1 wherein the first filtration step is through one or more layers of charged or surface modified microporous membranes wherein the membranes are formed of a material selected from the group consisting of regenerated cellulose, polyethersulfone, polyarylsulphone, polysulfone, polyimide, polyamide and polyvinylidenedifluoride. 5. A process for selectively removing protein aggregates and virus particles from an aqueous solution of proteins that consists essentially of: first filtering a protein solution containing said protein aggregates and viruses through a device selected from the group consisting of one or more layers of adsorptive depth filters and one or more layers of charged or surface modified microporous membranes, in a normal flow filtration and constant pressure mode of operation, recovering the aggregate free protein solution, and secondly filtering said protein solution through one or more ultrafiltration membranes having a molecular weight cut off of between about 200 kD and about 1000 kD to retain virus particles in said one or more ultrafiltration membranes at a level of at least 3 LRV, and to recover an aqueous, virus-free protein solution. 6. A process for selectively removing protein aggregates and virus particles from an aqueous solution of proteins that consists essentially of: first filtering a protein solution containing said protein aggregates and viruses through a device selected from the group consisting of one or more layers of adsorptive depth filters and one or more layers of charged or surface modified microporous membranes, in a normal flow filtration and constant flow mode of operation, recovering the aggregate free protein solution, and secondly filtering said protein solution through one or more ultrafiltration membranes having a molecular weight cut off of between about 200 kD and about 1000 kD to retain virus particles in said one or more ultrafiltration membranes at a level of at least 3 LRV, and to recover an aqueous, virus-free protein solution. 7. A process for selectively removing protein aggregates and virus particles from an aqueous solution of proteins that consists essentially of: first filtering a protein solution containing said protein aggregates and viruses through a device containing one or more layers of charged or surface modified microporous membranes, in a normal flow filtration mode of operation, recovering the aggregate free protein solution, and secondly filtering said protein solution through one or more ultrafiltration membranes having a molecular weight cut off of between about 200 kD and about 1000 kD to retain virus particles in said one or more ultrafiltration membranes at a level of at least 3 LRV, and to recover an aqueous, virus-free protein solution.