A water treatment system includes a coagulating and flocculating system, an ultrafiltration membrane, and a fluid driver. The coagulating and flocculating system includes a first inlet for receiving water and a second inlet configured to receive a coagulating and flocculating agent. The coagulating and flocculating system is configured to precipitate dissolved phosphorous from the water, and to provide a flocculated effluent at an outlet of the coagulating and flocculating system. The ultrafiltration membrane includes an inlet that is fluidly coupled to an outlet of the coagulating and flocculating system. The ultrafiltration membrane is configured to separate the precipitated phosphorus from the flocculated effluent. The fluid driver is adapted to transfer the flocculated effluent from the outlet of the coagulating and flocculating system to the inlet of the ultrafiltration membrane at sustained flux rates of at least 150 LMH.

Various systems and processes are directed to filtering organic compounds using nanoporous membranes and osmosis. In various implementations, the nanoporous membrane can be trained on one or more organic compounds such that the nanoporous membrane preferentially allows the one or more organic compounds to permeate the nanoporous membrane to the exclusion of other compounds. In some implementations, the nanoporous membrane is trained on ethanol such that the nanoporous membrane preferentially allows ethanol to permeate the nanoporous membrane to the exclusion of other compounds, such as water or other compounds or mixtures. In some implementations, the selective ethanol permeation of the nanoporous membrane may occur even where the other compounds have smaller molecules than ethanol.

The present invention relates to a system and process for treating a feedwater wherein the system includes at least one RO or nanofiltration unit that receives a feed under high pressure and produces a concentrate that is directed to and held at low pressure in a concentrate accumulator. Generally the permeate or the inlet feedwater is maintained at a constant flow rate. Periodically the system is switched from a mode 1 or normal operating process to a mode 2 where the concentrate is drained from the concentrate accumulator. However, in mode 2, the feedwater is still directed into the system and through the RO or nanofiltration unit which produces the permeate and the concentrate.

The present invention relates to the process for molecular separation of hydrocarbons using nanopore membrane comprising passing the hydrocarbon feedstock with or without separation enhancing additive/additives to produce permeate streams having different refractive indices which resonate with that of naphtha, kerosene and heavier molecules.

The present invention relates to a filtration device including: a flow rate control unit; a separation membrane module; a liquid flow rate detection unit detecting a liquid flow rate at a freely-selected part; and an external control unit controlling a state of the flow rate control unit, in which the external control unit includes: a target range setting step of setting a target flow rate range A; a control state recording step of recording a state S of the flow rate control unit when the liquid flow rate at the freely-selected part first enters within the target flow rate range A; a state setting step of setting the flow rate control unit to the state S; and a flow rate controlling step of controlling the liquid flow rate to be within the target flow rate range A.

The present invention relates to the process for molecular separation of hydrocarbons using nanopore membrane comprising passing the hydrocarbon feedstock with or without separation enhancing additive/additives to produce permeate streams having different refractive indices which resonate with that of naphtha, kerosene and heavier molecules.

A crossflow filter includes a rigid cylindrical inner wall and a rigid cylindrical outer wall inner with an inelastic filter membrane positioned therebetween defining a retentate channel inside the filter membrane and a permeate channel outside the filter membrane. Further, the filter includes transition channels shaped and connected to the inner and outer walls to deliver a flow of fluid from an inlet port to the retentate channel and to capture flow flowing longitudinally along the cylindrical inner and outer walls from both the retentate and permeate channels to respective outlet ports.

Filtering systems, methods, and devices, particularly adapted for apheresis of cellular bodies and more specifically for apheresis of circulating tumor cell bodies (CTCs) employs a cross-flow channel. Systems and methods as well as devices for such a system are described. Embodiments include a cylindrical filter that employs a thin micro-machined porous filter membrane with a regular array of pores and reliably pass blood while trapping CTCs.

Drainage water that includes anions and cations dissolved in water and that is received from an agricultural or industrial facility is treated by applying a voltage to an anode and a cathode on opposite sides of an electrically driven separation apparatus that further includes at least one monovalent-selective ion exchange membrane between the anode and the cathode. The drainage water is passed through the electrically driven separation apparatus, wherein monovalent ions are selected from the drainage water through the monovalent-selective ion exchange membrane. The drainage water is then recirculated as treated water through the facility after the monovalent ions are removed.

Drainage water that includes anions and cations dissolved in water and that is received from an agricultural or industrial facility is treated by applying a voltage to an anode and a cathode on opposite sides of an electrically driven separation apparatus that further includes at least one monovalent-selective ion exchange membrane between the anode and the cathode. The drainage water is passed through the electrically driven separation apparatus, wherein monovalent ions are selected from the drainage water through the monovalent-selective ion exchange membrane. The drainage water is then recirculated as treated water through the facility after the monovalent ions are removed.