Disclosed is a water treatment apparatus which can extract clean water by means of the pressure of raw water. The disclosed water treatment apparatus comprises: a filter part which filters raw water; a storage part which stores clean water filtered by passing through at least a part of the filter part, the storage part having a first chamber and a second chamber of which the volume changes according to a change in the volume of the first chamber; an extraction part which is installed so as to provide the filtered clean water to a user; and an air supply part which is installed on a flow path connected to the storage part in order to supply air to either one of the first chamber or the second chamber of the storage part.

A separation device for separating a filtrate from a sample fluid, especially for extracting plasma from whole blood, comprising a sample container for receiving the sample fluid and a filter plunger to be introduced under seal into the sample container, which filter plunger has a filter element at its front end and a grip element on the opposite end and will receive in its interior the filtrate obtained. After insertion of the filter plunger into the sample container an annular chamber is formed between the inner wall of the sample container and the outer wall of the filter plunger, which is sealed against the exterior by a sealing lip and in which an air cushion is formed upon introduction of the filter plunger into the sample container, which acts on the sample fluid. A flow connection is provided between the annular chamber and the front side of the filter element after insertion of the filter plunger is terminated.

A method of activating and dewatering sludge through application of acoustic pressure shock waves to wastewater.

A method of vacuum membrane filtration including placing a membrane filter between a filtration base and a pouring funnel, an upper side of the filtration base having a membrane bearing area with a bearing structure and a supporting contour surrounding the bearing structure and the supporting contour having at least one notch in flow connection with a bottom side of the membrane bearing area, detachably mounting the pouring funnel on the filtration base thereby clamping the membrane filter between the filtration base and the pouring funnel, applying suction to the filtration base such that the membrane filter is pulled against the bearing structure and comes into contact with the supporting contour, and dismounting the pouring funnel from the filtration base while still applying the suction, causing an outer rim of the membrane filter to bulge upward from the supporting contour and uncover the at least one notch.

Provided herein are, inter alia, biological manufacturing and downstream purification processes.

Disclosed herein are systems and methods for desalination of salt water based on an engineered acoustic field that causes constructive and destructive interference at precomputed spatial positions. The engineered acoustic field can cause high-pressure and low-pressure regions where desalination membranes are located. The induced pressure from the acoustic field can force pure water through the membranes leaving ionic and dissolved molecular species behind.

A device for separating gases comprises the following components: a source for the gases and flow adjustment means; a membrane unit for the production of a permeate gas and a retentate gas, one of which is the product gas; purity determining means for the product gas; a first control unit for the device; a retentate control system and a product gas pressure measurement, whereby the source has a second control unit for the flow adjustment means as a function of a target value of the gases and the first control unit is connected to the second control unit and to the retentate control system, whereby the first control unit can determine the target value and can control the retentate control system.

Systems and methods for purification and concentration of autologous alpha-2 macroglobulin (A2M) from whole blood and or recombinant A2M are provided. Also provided are methods of treating wounds with A2M. Methods for utilizing A2M in combination with other treatments (e.g., platelets and other growth factors) are provided in addition to combinations with exogenous drugs or carriers. Also provided is a method of producing recombinant A2M wild type or variants thereof where the bait region was modified to enhance the inhibition characteristics of A2M and/or to prolong the half-life of the protein for treating wounds.

A feed of at least one of (a) a source liquid including a solvent with a dissolved impurity and (b) a retentate of the source liquid is pumped in a substantially closed loop through a liquid-separation module. The liquid-separation module includes a membrane that passes at least partially purified solvent to a permeate side of the membrane while diverting the impurity in a retentate on the retentate side of the membrane. The purified solvent is extracted from the permeate side of the membrane; and the retentate from the liquid-separation module is pumped to or through a pressurized reservoir with a variable volume for the feed component and recirculated as a component of the feed. Over time, the volume for the feed is reduced and the pressure applied to the feed in the reservoir is increased to balance against an increasing difference in osmotic pressure across the membrane.

Many hand-held diagnostics are limited in their functionality due to the challenging physics associated with small dimensional systems. An example of this is capillary forces in hydrophilic systems, such as the tight retention of liquid passing through a small pore filtration membrane, or capillary force driven microfluidics where, to keep liquid flowing the dimensions of the system become so small that the flow rates are too low to be useful, or the manufacturing of such devices becomes uneconomical. This disclosure details methods to ‘reset’ the capillary force condition to avoid the requirement of transient pressure spikes associated with the breakthrough pressure of small pore membranes, and avoid the necessity of extremely small microfluidic channels, which can be useful in applications such as filtration of whole blood to plasma using only suction pressure or passive capillary pressure.