An automated single-use filtration device, in particular for large-volume filtration processes, comprises an unfiltrate inlet, one or more filter elements, a filtrate outlet and sensors for detecting specific process parameters and regulating mechanisms for adjusting specific process parameters. The sensors and regulating mechanisms are connected to an external monitoring and control system, which is adapted for evaluating and processing sensor data and for piloting the regulating mechanisms based on one or more control algorithms.

A membrane surface monitoring system (MSM) and membrane surface monitoring cell for direct and unambiguous detection of membrane surface fouling and mineral scaling. The system includes a membrane surface monitoring system cell, a control valve, a retentate flow meter/transmitter and a controller. The MSM cell has a visually-observable membrane, an edge-lit light guide, an edge illumination light source, a retentate module, and a permeate module. A pressurized inlet stream is fed into the MSM cell. The feed contacts a membrane sheet, leading to membrane-based separation operation to produce retentate and permeate streams. The MSM cell integrates surface illumination and imaging components to allow direct real-time visualization and spectral imaging of the membrane surface in real time. The pressure on the feed-side of the MSM cells is approximately that of the membrane plant element being monitored such that the plant control system can adjust plant operating conditions.

A water purification apparatus and method for optimizing efficiency of the water purification apparatus comprising a fluid circuit including a Reverse Osmosis, RO, unit (3), providing a permeate flow, and an electrically controlled deionization unit (4) downstream the RO unit (3) receiving at least part of the permeate flow. The method comprises obtaining (S1) a value indicative of power consumption by the electrically controlled deionization unit and determining (S2) whether the obtained value indicative of the power consumption meets at least one criterion. The method further comprises controlling recirculation of reject water produced by the water purification apparatus, based on a result of the determining (S2), in order to optimize efficiency of the water purification apparatus.

The water treatment device according to the present disclosure includes: an electrochemical cell having electrodes including a positive electrode and a negative electrode, and a bipolar membrane; a tank; a power supply configured to apply power to the electrodes; a water circulation flow path having at least the tank and the electrochemical cell and through which water circulates; a circulation device configured to circulate water in the water circulation flow path; a raw water supply path configured to supply raw water to the water circulation flow path; and a control device. In performing water softening treatment in the electrochemical cell where power is applied to the electrodes so as to remove ions from raw water and soft water is produced, the control device drives the circulation device so as to circulate water in the water circulation flow path.

Device for water disinfection by ultrafiltration. The device comprises a filtering assembly with at least one ultrafiltration membrane (6) inside a casing (10); a pump (5, 15), powered with electrical energy, configured for driving water to be filtered to said at least one ultrafiltration membrane (6); and an electric supply connection (2) for powering said pump (5) from a power supply. Said at least one ultrafiltration membrane is located in said casing (10) in a position in which it receives the feed flow of the water to be filtered by gravity or pressure; the electric power supply is provided by a battery included in a portable communication device (4); and the intensity of the current consumed by the pump (5, 15) is below 1.2 A, with a supply voltage of up to 24 V.

The present invention concerns an electronic safety system for a RO-device (RO) which is designed to be used with at least one dialysis device (D). The system comprises the RO-device (RO), which is designed for the production of ultrapure water and which is developed with a sensor unit (S) for collecting sensor data and whereby the RO-device (RO) comprises an electronic data interface (RO-S) in order to send the sensor data collected by the sensor unit (5); and it also comprises an analysis unit (AE) which is designed to analyse a water sample with regards to safety requirements and especially with regard to contamination and to generate result data whereby the analysis unit (AE) is also developed with a analysis interface (AE-S) in order to send the generated result data in electronic form; and a network (NW) for the data exchange between the medical-technical entities, especially between the RO-device (RO) and the analysis unit (AE).

A system for separating a suspension of biological cells is disclosed comprising a single-use fluid circuit and a durable hardware component. The fluid circuit comprises a separator having a housing that includes an inlet for introducing the suspension of biological cells into the gap, a first outlet in communication with the gap for flowing a first type of cells from the separator, and a second outlet in communication with the second side of the filter membrane for flowing a second type of cells from the separator. The hardware component comprises a pump for flowing the suspension of biological cells to the inlet of the separator and at least one flow control device associated with the first outlet and the second outlet of the separator for selectively opening and closing the outlets so as to permit one of the first type of cells and the second type of cells to flow out of the separator in accordance with a predetermined duty cycle equal to the ratio of a target flow rate of first type of cells through the first outlet to the predetermined inlet flow rate.

A fluid system includes a membrane module including a first section and a second section that are separated by a semipermeable membrane, a feed pump connected to the first section, a draw pump connected to the second section, a load connected to the second section, a flush valve, and an electronic control unit (ECU) configured to control one or more of the feed pump, the draw pump, the flush valve, and the load. The ECU may be configured to control the feed pump, the draw pump, the flush valve, and/or the load according based on or according to net power generation.

A system for separating a suspension of biological cells is disclosed comprising a single-use fluid circuit and a durable hardware component. The fluid circuit comprises a separator having a housing that includes an inlet for introducing the suspension of biological cells into the gap, a first outlet in communication with the gap for flowing a first type of cells from the separator, and a second outlet in communication with the second side of the filter membrane for flowing a second type of cells from the separator. The hardware component comprises a pump for flowing the suspension of biological cells to the inlet of the separator and at least one flow control device associated with the first outlet and the second outlet of the separator for selectively opening and closing the outlets so as to permit one of the first type of cells and the second type of cells to flow out of the separator in accordance with a predetermined duty cycle equal to the ratio of a target flow rate of first type of cells through the first outlet to the predetermined inlet flow rate.

Filtering systems can process wastewater to provide a primary output of clear water and a secondary output of sludge. The filtering systems are compact, optionally mobile and optionally truck-mountable, and have a high throughput capacity and cleaning effectiveness. For a system having a volume VS, and for wastewater having a TSS content of TSS1 and a COD of COD1, the primary output may have a TSS<1% of TSS1, a COD<2% of COD1, and a turbidity of <1, or 0.5, or 0.3 NTU. The system may receive the wastewater at a flow rate F1 and provide the primary output while receiving the wastewater, and F1/VS may be 0.2 hr.sup.1. F1 may be 1 L/sec, and VS may be 5 m.sup.3, or 30 m.sup.3, or in a range from 20-30 m.sup.3. The primary output may have a flow rate 40%, or 50%, or 60% of F1.