C02F2303/10

DESALINATION SYSTEM

A desalination system includes: a pressurized vessel which generates concentrate water and permeate water by causing treatment target water to pass through a reverse osmosis membrane element built in the pressurized vessel; an energy recovery device which is located on a discharge channel so as to discharge the permeate water, and recovers energy of the permeate water; a bypass discharge channel which branches off from the discharge channel and is located between the pressurized vessel and the energy recovery device, and which discharges the permeate water; and a bypass control mechanism which is located on the bypass discharge channel and controls a discharge volume of the permeate water.

APPARATUS SYSTEM AND METHOD TO EXTRACT MINERALS AND METALS FROM WATER
20190300410 · 2019-10-03 ·

A new apparatus, system and method to purified produced water and removed valuable metals and minerals is described. The apparatus comprises a device for flowing produced water wellbore from a wellbore to the produced water purification apparatus; at least one device to remove heavy metals from the produced water; at least one brine removal device to remove brine from the produced water. The method comprises steps to use the apparatus and the system comprises a control panel that operates the at least one device for removing heavy metals and at least one sensor in a coordinated manner.

SYSTEMS AND METHODS FOR TREATING HIGH SULFATE WATER AND INJECTING TREATED WATER
20190299162 · 2019-10-03 ·

A method for treating water high in sulfate includes passing the water at a temperature of 10 C. to 45 C. through a nanofiltration membrane module and a reverse osmosis membrane module in series such that the retentate stream from the nanofiltration membrane module is fed to the reverse osmosis membrane module. A first permeate stream from the nanofiltration membrane module has at least 90% lower sulfate content than the feed stream. A second permeate stream from the reverse osmosis membrane module has at least 95% lower sulfate content than the retentate stream from the nanofiltration membrane module. The first and second permeate streams are combined to form a treated stream containing less than 40 ppm sulfate. A system including the nanofiltration and reverse osmosis membrane modules in series is also disclosed.

Ultraviolet Irradiation of a Flowing Fluid

A solution for irradiating a flowing fluid through a channel with ultraviolet radiation is provided. Ultraviolet radiation sources can be located within the channel in order to direct ultraviolet radiation towards the flowing fluid and/or the interior of the channel. A valve can be located adjacent to the channel to control the flow rate of the fluid. A control system can control and adjust the ultraviolet radiation based on the flow rate of the fluid and a user input component can receive a user input for the control system to adjust the ultraviolet radiation. The ultraviolet radiation sources, the control system, the user input component, and any other components that require electricity can receive power from a rechargeable power supply. An electrical generator located within the channel can convert energy from the fluid flowing through the channel into electricity for charging the rechargeable power supply.

Reverse osmosis treatment system for recovering energy generated both at brine and permeate sides during seawater desalination

Provided is a reverse osmosis treatment system capable of simultaneously and efficiently recovering energy generated both at brine and permeate sides. The system comprises a branched portion configured to divide second to-be-treated water into third and fourth to-be-treated water; a high-pressure pump configured to pressurize the third to-be-treated water thereby to feed fifth to-be-treated water having a higher pressure than the to-be-treated water before divided; a displacement type of first energy recovery device configured to exchange pressures between the fourth to-be-treated water and brine thus separated by a reverse osmosis treatment device, thereby to produce sixth to-be-treated water having a higher pressure than the fourth one; and a second energy recovery device configured to raise a pressure of the third to-be-treated water located at a downstream side of the branched portion with a pressure of first permeate thus separated by the reverse osmosis treatment device.

Water distilling and purifying unit and variants thereof
10427068 · 2019-10-01 ·

A method for distilling water includes moving raw water into an evaporator. Water is pumped into a liquid-driven condensing ejector. Water vapor is discharged from a vapor outlet of the evaporator into a gas inlet of the ejector. Fluid from an outlet of the ejector is conducted into a heat exchanger. Heat from fluid conducted from the ejector is transferred in the heat exchanger to the raw water entering the evaporator.

SOLAR THERMAL BASED WATER TREATMENT SYSTEM FOR IMPURE AND INDUSTRIAL WASTEWATER

A solar thermal based water treatment system and a process for treating impure/industrial wastewater is disclosed. The solar thermal based water treatment system vaporizes impure/wastewater using incident solar radiations in a third unit with only air as a medium. The system has a fourth unit and a fifth unit for condensing water vapor and obtaining purified water in the form of condensate. The system also includes an eighth unit for drying the sludge or slurry using dry air for obtaining dry solid waste. The system also includes a ninth unit to remove the undesirable gases from exhaust air before releasing in the atmosphere.

PROCESS AND PLANT FOR THE THERMAL ABATEMENT OF MALODOROUS EMISSION FROM A PURIFICATION PLANT WITH ENERGY RECOVERY FROM SAID ABATEMENT
20190291047 · 2019-09-26 · ·

A process and a plant for the thermal abatement of foul air containing malodorous substances emitted by a purification system with energy recovery from said abatement are described, the process comprising the steps of: feeding a flow of foul air containing malodorous substances emitted from a purification plant, as combustive air into the combustion chamber of a unit for production and recovery of energy, thus producing a flow of high-temperature exhaust gas; feeding said flow of exhaust gas into a scrubber for the abatement of polluting substances, said scrubber using water for the washing of the flow of exhaust gas, thus producing a flow of low-temperature purified gas and a heated washing liquid; conveying the heated washing liquid to at least one heating jacket of a storage tank for the biological treatment of sewage of the aforementioned purification plant; a method for revamping a pre-existing purification plant, so as to make the plant suitable for implementation of the process described above, is also described.

Stabilization of biomimetic membranes

The present disclosure provides methods, compositions, kits and apparatuses for stabilizing membranes, membrane proteins, and/or membranes containing membrane proteins using hydrophobin.

Energy-saving seawater desalination system using steam generated in nuclear reactor, and method for desalinating seawater
10413842 · 2019-09-17 ·

The present disclosure relates to a seawater desalination system which improves energy efficiency by applying a heated cooling water discharged from a nuclear power plant and high-temperature steam generated in a nuclear reactor to seawater desalination. A seawater desalination system related to an exemplary embodiment of the present disclosure includes: a steam supply pipe 40 which supplies heat exchange steam that is a part of the steam discharged from a turbine 20; a seawater supply pipe 36 which diverges from a discharge pipe 34; and a heat exchanger 50 which is connected to the steam supply pipe 40 so as to be supplied with the heat exchange steam, and connected to the seawater supply pipe 36 so as to be supplied with first seawater that is a part of the seawater discharged from a condenser 30, in which the heat exchanger 50 increases a water temperature of the first seawater by using heat included in the heat exchange steam, and the first seawater with the increased water temperature is supplied to the fresh water-generating unit 2 through a connection pipe 4, such that desalination of the first seawater is performed.