Parallel chromatography systems and continuous manufacturing methods are described herein that utilize two or more chromatography column skids having columns operating in parallel with automation controls governing which column to load at a given time.

A multi tank water softener system and method 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 growth while also reducing salt usage by up to 40%.

Various embodiments are directed to a valve switching system for selectively interconnecting components of a bioprocess installation, comprising a valve switching cassette and an actuator block. It is proposed, that the valve switching cassette comprises a perforated backer plate securing a valve membrane structure to a cassette manifold, that the actuator block comprises a drive membrane structure with at least one drive membrane and a perforated backer plate securing the drive membrane structure to an actuator block body, wherein for selectively switching valve units, an actuator of the actuator block may urge the drive membrane structure through aligned perforation holes of both backer plates into engagement with the valve membrane structure.

Parallel chromatography systems and continuous manufacturing methods are described herein that utilize two or more chromatography column skids having columns operating in parallel with automation controls governing which column to load at a given time.

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.

An ion exchanger includes a housing, which includes an inlet and an outlet for a coolant and is open upwardly, and a cartridge mounted within the housing so as to be removable upwardly out of the housing. The cartridge includes a first case and a second case respectively located above and below the inlet and the outlet and capable of containing an ion exchange resin. The first case includes a first flow entrance, which is in fluid communication with the inlet of the housing, and a first flow exit, which is in fluid communication with the outlet of the housing. The second case includes a second flow entrance in fluid communication with the inlet of the housing and a second flow exit in fluid communication with the outlet of the housing.

A parallel assembly of chromatography column modules, the assembly having one common assembly inlet and one common assembly outlet, each column module comprising a bed space filled with chromatography medium and each column module comprises integrated fluid conduits which when the column module is connected with other column modules are adapted to connect the bed space of the column module with the assembly inlet and the assembly outlet, wherein the total length and/or volume of the fluid conduit from the assembly inlet to one bed space together with the length and/or volume of the fluid conduit from the same bed space to the assembly outlet is substantially the same for all bed spaces and modules installed in the parallel assembly.

The present invention relates to a chromatography system wherein the chromatography system comprises an eluting system and a capturing system consisting of at least two chromatography units operated alone or in series and a capturing process employing in-line buffer dilution in, which concentrated buffers are blended with water and provided to the chromatography units.

Methods of preparing highly purified steviol glycosides, particularly Rebaudioside D, are described. The methods include purification from the extraction stage of the Stevia rebaudiana Bertoni plant, purification of steviol glycoside mixtures, Rebaudioside D and Rebaudioside A from a commercial Stevia extract, and purification of Rebaudioside D from remaining solutions obtained after isolation and purification of Rebaudioside A and a high purity mixture of steviol glycosides. The methods are useful for producing high purity Rebaudioside D, Rebaudioside A, and steviol glycoside mixtures. The high purity steviol glycosides are useful as non-caloric sweeteners in edible and chewable compositions such as any beverages, confectioneries, bakery products, cookies, and chewing gums.

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.