The invention concerns biocompatible polymer systems comprising at least one polymer with a plurality of pores, said polymer comprising either polyol or zwitterionic groups designed to adsorb endotoxins and other inflammatory mediator molecules.

The present invention describes a simple purification process for recombinant human serum albumin. The process results in highly purified protein with limited number of purification steps. The broth containing human albumin is clarified by centrifugation and microfiltration, diafiltered and captured by cation exchange chromatography by a process that allows 140-230 mg of albumin to be captured per ml of resin. Product related impurities are removed by hydrophobic interaction chromatography, optimised to allow 87-97% recovery in flow through mode. The final series of processes are so combined that there is easy transition from one step to the next with minimal interventions and adjustments. The entire process of purification is completed within two days from harvest to final product. Thus a cost-effective process with improved recovery of protein at each step is developed. The purified human serum albumin is analyzed for purity and shows physicochemical characteristics that are similar to standard albumin.

Disclosed is a method for removing factor XI (FXI) during plasma protein purification, more specifically a method for removing FXI including dialyzing and concentrating a plasma protein fraction II paste containing FXI and a plasma protein, and then removing the FXI using a ceramic-based cation exchange resin. The method for removing factor XI (FXI) can improve removal efficiency of impurities and thrombogenic substances, thereby producing stable plasma proteins with improved quality.

The present invention relates to a method for controlling a bioprocess purification system comprising a continuous chromatography configured to operate with at least three columns and configured for cyclic operation, wherein the continuous purification is performed on a sample comprising a target product having desired characteristics. The method comprises detecting (82) at least one parameter indicative of characteristics of the target product, performing (83) real time trend analysis of each detected at least one parameter to identify a deviation from the desired characteristics of the target product, and controlling (84) the bioprocess purification system to meet the desired characteristics based on the identified deviation, whereby the target characteristics is within a pre-determined range.

A cell lysis buffer separation apparatus for preparing a polypeptide, and a system and the application thereof. The system comprises a polypeptide enrichment module, wherein the polypeptide enrichment module comprises a cell lysis buffer separation apparatus, and the cell lysis buffer separation apparatus comprises a multi-filtration device and a waste discharge pipeline, the waste discharge pipeline being connected to the multi-filtration device. The system can perform multi-filtration treatment on a lysis buffer. Therefore, the yield of target protein can be increased; and a waste liquid obtained by means of the system contains almost no toxin polypeptide precursor with low toxicity, and has very little toxicity to an operating environment, and same can be directly discharged after simple disinfection treatment, thereby greatly reducing production cost and promoting large-scale industrial production of polypeptide under the conditions of ensuring the safety of the environment and the safety of operators.

A charged depth filter for removing cells and/or cellular debris from a biopharma feedstock having a first functionalized nonwoven layer having a first calculated pore size and a first dynamic charge capacity; a second functionalized nonwoven layer having a second calculated pore size and a second dynamic charge capacity positioned after the first functionalized nonwoven layer in the direction of the biopharma feedstock flow, and wherein the first calculated pore size is greater than the second calculated pore size, and the first dynamic charge capacity is less than the second dynamic charge capacity.

Method and systems are disclosed for selectively removing naturally-occurring sugars in beverages in an effective, affordable and scalable manner.

This invention relates generally to a process for selective adsorption and recovery of lithium from natural and synthetic brines, and more particular to a process for recovering lithium from a natural or synthetic brine solution by passing the brine solution through a lithium selective adsorbent in a continuous countercurrent adsorption and desorption circuit.

Disclosed here includes a method for purifying a biologic composition, comprising diafiltering the biologic composition into a composition comprising phosphate buffered saline (PBS) to obtain a purified composition. The method disclosed here can be particularly useful for removing one or more impurities from the biologic composition, such as bis(2-hydroxyethyl)amino-tris(hydroxymethyl)methane (Bis-tris).

A liquid chromatography system, includes a fluidic flow path, a chromatography column located in the fluidic flow path, a filtration device located in the fluidic flow path before the chromatography column, the filtration device including a housing having a fluidic inlet, a fluidic outlet, wherein at least a portion of the fluidic flow path is located between the fluidic inlet and the fluidic outlet and at least one filter disposed in the portion of the fluidic flow path, wherein the at least one filter is made of a micromachined material. Liquid chromatography filtration methods are further disclosed.