Patent classifications
B01D2321/44
AUTOMATIC OFF-LINE GAS-WATER COMBINED-WASHING MEMBRANE BIOREACTOR (MBR)
The invention discloses an automatic off-line gas-water combined-washing membrane bioreactor, comprising a PLC automation control cabinet, a MBR reactor, a MBR membrane assembly, a rotating hood, an annular guide rail, a lifting device, a washing pipe network, an external interface, a gas washing pipe, a water washing pipe, a gas pump and a water pump, wherein the gas pump, the water pump and the three-way change valve are all connected with the PLC automation control cabinet, the washing pipe network is provided with several nozzles. The present invention adopts a full PLC automation control system, the PLC automation control cabinet controls a pressure washing pump (gas pump and water pump), and gas or water is injected into the washing pipe network by flexibly adjusting the three-way change valve, so that the operation is simple, the cleaning is complete, and the manual operation load is reduced.
WASTEWATER TREATMENT AND SOLIDS RECLAMATION SYSTEM
A fixed or mobile water treatment system comprises a primary screening tank that filters wastewater to remove inorganic and organic pollutants from the wastewater, and includes an electro-coagulation unit that provides an electrical charge to wastewater exiting the primary screening tank, ultraviolet light and oxidation processes in one or more settling tanks that remove pollutants from the wastewater, and one or more filters that remove pollutants from the wastewater.
FORWARD OSMOTIC AND WATER HAMMER METHOD OF MEMBRANE CLEANING
Apparatus and method for semi-permeable membrane cleaning in particular, applying series of pulsed water stroke, made simultaneously with osmosis backward flow causing superposed membrane directional shaking and fouling detachment. Pulsed water stroke provided by water stroke generator as several momentum sharp changes in gauge pressure and induce velocity pulse of residual brine flow. The pulsed water strokes ideally induce resonance in the membrane. Osmosis backward wash may be provided either by injection for predetermined injection time, additional solution selected in such way that net driving pressure be-comes opposite to normal osmotic operation thereby providing a backward flow of permeate towards to the side opposite to normal operation mode, so as to lift said foulant, or by throttling permeate exiting from the permeate enclosure, until the net driving pressure value become equal to zero, during application of precise synchronized and opposing brine and permeate pressure strokes thereby providing a plurality of quick RO-FO-RO process changes. These procedures allow a membrane to be kept continuously clean and operate at higher recovery.
Air separation module (ASM) contamination apparatus and removal process
An apparatus and method for cleaning and restoring air separation modules (ASMs). The present invention cleans and restores ASMs that comprise a gas permeable fiber module that uses a fiber composition in the polyimide hollow fiber family. The present invention removes contaminants, such as fuel, from an ASM by blowing air at environmental temperature into the ASM, and then restores the ASM by blowing hot air into the ASM.
Forward osmotic and water hammer method of membrane cleaning
Apparatus and method for semi-permeable membrane cleaning in particular, applying series of pulsed water stroke, made simultaneously with osmosis backward flow causing superposed membrane directional shaking and fouling detachment. Pulsed water stroke provided by water stroke generator as several momentum sharp changes in gauge pressure and induce velocity pulse of residual brine flow. The pulsed water strokes ideally induce resonance in the membrane. Osmosis backward wash may be provided either by injection for predetermined injection time, additional solution selected in such way that net driving pressure becomes opposite to normal osmotic operation thereby providing a backward flow of permeate towards to the side opposite to normal operation mode, so as to lift said foulant, or by throttling permeate exiting from the permeate enclosure, until the net driving pressure value become equal to zero, during application of precise synchronized and opposing brine and permeate pressure strokes thereby providing a plurality of quick RO-FO-RO process changes. These procedures allow a membrane to be kept continuously clean and operate at higher recovery.
MEMBRANE FILTRATION CELL WITH ELECTRIC FIELD AND ACOUSTIC FIELD
A membrane filtration cell is provided which includes a fluid passageway and a filtration membrane positioned within the passageway, the filtration membrane dividing the fluid passageway into two chambers, a retentate chamber and a permeate chamber. A first electrode is positioned in the retentate chamber and a second electrode is positioned in the permeate chamber, where the first electrode and the second electrode are configured to apply an electric field across the filtration membrane. The membrane filtration cell also includes an acoustic device configured to apply an acoustic field across the retentate chamber, where the synergistic combination of the electric field and the acoustic field prevents fouling on the filtration membrane. A method of filtering water is provided which includes generating an electric field across a filtration membrane with a first electrode positioned in the retentate chamber and a second electrode positioned in the permeate chamber, and generating an acoustic field across the retentate chamber with an acoustic device, where the synergistic combination of the electric field and the acoustic field prevents fouling on the filtration membrane.
SYSTEMS AND METHODS FOR TREATING OILFIELD WASTEWATER
A wastewater treatment system is disclosed that includes a desanding hydrocyclone, a deoiling hydrocyclone, an electrocoagulation apparatus that is adapted to receive a flow of treated wastewater from the desanding and deoiling hydrocyclones, a floc separator that is adapted to receive a flow of a first effluent from the electrocoagulation apparatus, and an ultrafiltration membrane apparatus that is adapted to receive at least a portion of a flow of a second effluent from the floc separator.
WATER PURIFYING SYSTEM AND BACKWASH MODULE CONTROL METHOD THEREOF
Disclosed herein is a water purifying system, including: a raw water tank configured to store raw water; a filter unit configured to include a plurality of filtration modules for purifying the raw water and a plurality of valves for feeding or cutting off the raw water; a raw water pump configured to feed the raw water from the raw water tank to the filter unit; and a backwash module configured to feed backwash water to the filter unit, in which some of permeate water permeated by the filter unit is fed to the backwash module to be used as the backwash water and a feed pressure of the backwash water is fed by the raw water pump.
FILTER CLEANING METHODS AND APPARATUSES
A method for cleaning a filter includes flowing a cleaning fluid through a filter housing to clean the filter in the filter housing and obtaining flowing parameters of the cleaning fluid. The method further includes determining a condition of the filter based on the flowing parameters of the cleaning fluid, and associating the flowing parameters to attributes of the filter when the condition of the filter is clean.
SYSTEM AND METHODS FOR MIMICKING MEMBRANE CLEANING-IN-PLACE CONDITIONS
Cleaning-in-place (CIP) systems utilize membrane filters for purifying liquid substances in many industries, including but not limited to, the dairy industry, breweries, pharmaceutical industry, and the food industry. These membrane filters undergo a rigorous cleaning process that despite cleaning can leave foulants on the membranes which hamper filter effectiveness. In addition to the cleaning, enzymes can be applied to the membranes to remove foulants and restore filtering effectiveness. However, introduction of enzymes into these CIP systems can be problematic if enzymes remain after cleaning. This disclosure provides a system and methods to mimic the membrane modules and verify that a correct inactivation procedure occurred. The systems and methods include a separate membrane sample so that no membrane modules need be removed to verify full enzyme inactivation.