A fluid filtration assembly includes a filter housing having first and second ends and a connector for fluid communication with a fluid storage vessel. A filter element is disposable within the filter housing, and first and second pumps are coupled at the first and second ends of the filter housing. A controller may coordinate the operation of the first and second pumps to induce alternating tangential flow of fluid between the filter housing and the first and second pumps. At least one of the first and second pumps is a diaphragm pump or a plunger pump. The fluid storage vessel can be a bioreactor.

Methods for controlling a spinning membrane separator so as to limit fouling of the membrane by changing the rotation rate of the spinning membrane in response to the fouling rate, while maintaining a constant outlet cellular concentration. Increasing the spinner rotation rate will increase the strength of the Taylor vortices generated within the separator by the spinning of the membrane, which should reduce fouling of the membrane. The goal of the method is to rotate the spinning membrane at the slowest rate possible without unacceptable fouling. Two specific methods to control fouling are disclosed. In a first, unidirectional method, the spin rate of the membrane is only increased in response to undesirable fouling in order to prevent the fouling from continuing. In a second, bidirectional method, the spin rate of the membrane may be either increased or decreased in response to the measured fouling rate in order to maintain the fouling rate within a desired range.

A method of removing carbon dioxide from a carbonate-containing diaminoalkane solution, the method including passing the carbonate-containing diaminoalkane solution through a membrane module, and a method of preparing diaminoalkane including the same.

A dehydration method is a dehydration method for selectively separating water from a mixture that contains water, using a zeolite membrane having an AFX structure, and the method includes a step of supplying the mixture to a supply side space of the zeolite membrane having an AFX structure, and a step of making a pressure difference between the supply side space and a permeation side space of the zeolite membrane having an AFX structure.

Embodiments described herein relate to methods and systems for dewatering solutions via forward osmosis.

Embodiments described herein relate to methods and systems for dewatering solutions via forward osmosis.

Disclosed is a filtering method for isolating a substance from a sample. The method includes: providing a filter module having a sample inlet, a sample outlet, and a filter covering the sample outlet; introducing, via a sample inlet a first quantity of the sample into the filter module; conducting the sample from the sample inlet through the filter and the sample outlet by applying a pressure difference between a side of the filter facing the sample inlet and a side of the filter facing away from the sample inlet; measuring the pressure difference and/or a volumetric flow through the filter; comparing the measurement values to a predefined reference value; and ending the method if successively detected measurement values lie within a predefined range of values around the reference value. Disclosed also is a device with which the method can be carried out.

An outlet (3) for fluid feed of a first membrane module (1a) is connected to a fluid inlet (2) of a second membrane module (1b), and if further membrane module(s) is/are present, the outlet (3) for fluid feed of a previous membrane module (n−1) is connected to the fluid inlet (2) of a following membrane module (n), and for the last membrane module (n), the outlet (3) for fluid feed is connected to the fluid inlet (2) for fluid feed of the first membrane module (1a). An amount of fluid feed is continuously pumped with pressure PB through a loop of n membrane modules that are serially connected, the fluid feed and permeate flow concurrently through each of the n membrane module(s), generated permeate is continuously drained from each membrane module through a permeate outlet, permeate pressure at the permeate outlet of each membrane module is controlled within a range.

A fluid treatment assembly comprises one or more cross flow fluid treatment units positioned between opposite end pieces. The fluid treatment unit includes a permeable fluid treatment medium having a feed side and a permeate side. The fluid treatment assembly further comprises a feed inlet and feed passage, a permeate outlet and a permeate passage, and a retentate outlet and a retentate passage. The feed passage directs feed fluid from the feed inlet to the permeable medium and tangentially along the feed side of the permeable medium. The permeate passage directs permeate from the permeate side of the permeable medium to the permeate outlet. The retentate passage directs retentate from the feed side of the permeable medium to the retentate outlet. A flow restrictor is positioned in the retentate passage.

A membrane separation unit can include a cartridge, at least one membrane disposed within the cartridge, at least one seal plate, and a sealing ring seated in an outer groove of the seal plate. The at least one seal plate can seal one end of the cartridge. The seal plate can have at least one venting hole that forms a passage between the interior of the cartridge and the outer groove. The sealing ring can have a cross-sectional shape that forms a circular venting path between the sealing ring and the seal plate. The sealing ring can include one or more grooves to allow fluid to vent into an annular space between a device housing and the membrane separation unit. The sealing ring can include an outer surface having, in cross-section, two flattened surfaces that form an angle of between 90° and 175° there between.