A system for producing steam includes a source of superheated water with superheated water output; a membrane filtration system in fluid communication with the superheated water output and including a membrane filter with a permeate side and an opposing retentate side. The membrane filter includes a separation membrane constructed to reject organic molecules. The system may be used for removing organic compounds, such as anti-corrosion agents or contaminants, from superheated water to produce steam. A method for producing steam includes directing a cross-flow of heated pressurized water including a first concentration of an organic compound across a membrane filter. The membrane filter includes a separation membrane constructed to reject the organic compound; and one or more support layers adjacent the separation membrane. A steam permeate including a second concentration of the organic compound is collected, where the second concentration is lower than the first.

A multi tank water softener system in which multiple softeners can be selectively operated in parallel, alternating, or in series in either order. The system reduces risk of Legionella and pathogen grown while also reducing salt usage by up to 40%.

Methods and systems directed to the separation of a heavy hydrogen isotope, e.g., tritium, from an aqueous stream are described. The methods and systems incorporate a separation media that includes a proton conducting ceramic that at low temperatures preferentially adsorbs heavy hydrogen isotopes and at high temperature preferentially adsorbs lighter heavy hydrogen isotopes. The methods can be temperature controlled to sequentially purify a contaminated stream and regenerate the separation media. The separation media can be free of traditional hydrogen isotope exchange catalyst materials.

The present invention relates to a method for monitoring operational status in a column capture chromatography system configured for cyclical repetitive purification performed on a volume of sample feed comprising at least one product configured to be captured in the column during loading. The method comprises: performing (51) a purification cycle; measuring (52) at least one parameter during the purification cycle indicative of breakthrough of the at least one captured product after the column during loading of sample feed; when breakthrough is detected, reducing (56a) the amount of sample feed loaded during loading in the next purification cycle; and repeating the steps to perform another purification cycle. Each purification cycle comprising: loading an amount of sample feed onto the column, washing the column and eluting the at least one product.

Examples of the present disclosure describe systems and methods for detecting and mitigating stack pivoting exploits. In aspects, various “checkpoints” may be identified in software code. At each checkpoint, the current stack pointer, stack base, and stack limit for each mode of execution may be obtained. The current stack pointer for each mode of execution may be evaluated to determine whether the stack pointer falls within a stack range between the stack base and the stack limit of the respective mode of execution. When the stack pointer is determined to be outside of the expected stack range, a stack pivot exploit is detected and one or more remedial actions may be automatically performed.

Provided is a bioreactor arrangement for producing a biopolymer expressed by a cell and a continuous process for a capturing the biopolymer employing two chromatography units operated in series or independently.

The present invention relates to a bioreactor arrangement for producing a biopolymer expressed by a cell and a continuous process for a capturing the biopolymer employing two chromatography units operated in series or independently.

A water softener apparatus comprises two water softener tanks one of which is always operating, valves controlling the flow of water and a flow-meter, wherein, after a set volume of water has passed through one tank, water is passed through the other tank. The apparatus uses ion-exchange tanks which may be regenerated by brine when not softening hard water. The flow-meter preferably comprises an actuator which moves in a cyclic movement in response to the flow of a set quantity of water and actuates two service valves which send pressured water signals to a drain shuttle valve. The drain shuttle valve then diverts hard water from one tank to another and initiates regeneration of the first tank. A regeneration meter terminates the alternate regeneration of the two tanks. The regeneration meter is positioned in the apparatus of a point where brine for regeneration of the two water softener components is received into the apparatus.

A liquid chromatographic (LC) system is introduced which comprises at least one fluidic stream, the fluidic stream comprising a sample-injection valve, a trap-bypass-selection valve, a column-bypass valve, a load-elute valve and a trap-selection valve. Also, a liquid chromatographic (LC) system is introduced which comprises at least one fluidic stream. The fluidic stream comprises a first substream and a second substream. The first substream comprises a first sample-injection valve, a load-elute valve and a trap-selection valve. The second substream comprises a second sample-injection valve and a column-bypass valve. The fluidic stream further comprises a trap-LC substream transfer valve and a substream-selection valve. The LC systems provide a broad choice of chromatographic options and modes and enable to flexibly and rapidly switch between them.

The present application provides methods and systems for viral clearance for purifying an antibody from a sample comprising one or more impurities including viral particles. The method is conducted in a system which includes a hydrophobic interaction chromatography (HIC) column and a virus retentive filtration (VRF) system. The HIC column and the VRF system are connected inline in a continuous processing system, and the VRF system comprises at least two filter trains in parallel.