A wastewater treatment system consisting of a single tank extended aeration activated sludge process with a continuously operating clarifier skimming device which is capable of producing a clear odorless effluent which meets applicable state discharge standards.

A wastewater treatment system includes a plurality of reaction tanks, a blowing pipe, a blower unit, and an air supply amount controller. The air supply amount controller includes: a water quality measurement unit configured to measure a state of wastewater; a necessary air amount acquisition unit configured to acquire, a necessary air amount for achieving a predetermined target water quality of wastewater; a target in-pipe pressure calculation unit configured to calculate a blowing pipe loss pressure when the necessary amount of air is supplied into the blowing pipe, calculate a target in-pipe pressure based on the blowing pipe loss pressure, and change the calculated target in-pipe pressure in accordance with change of the necessary air amount; and a blowing control unit configured to control air supply from the blower unit so that the pressure in the blowing pipe becomes equal to the target in-pipe pressure.

The present invention provides a gas generator, comprising a water tank and an electrolysis device. The water tank has a first hollow portion for containing electrolyzed water. The electrolysis device is disposed inside the first hollow portion of the water tank for electrolyzing the electrolyzed water to generate a hydrogen-oxygen mixed gas. When the electrolysis device starts to electrolyze the electrolyzed water, the first hollow portion of the water tank is filled with the electrolyzed water for standing at a full level of water. And after the electrolysis device electrolyzed the electrolyzed water, the level of water for the electrolyzed water filled into the first hollow portion of the water tank is higher than 95% of the full level of water. The gas generator of the present invention provides the design for saving space and nearly a zero gas chamber to reduce the possibility of explosions resulting from hydrogen-oxygen mixed gas.

This membrane separation device includes: an organic substance concentration measurement means which measures the organic substance concentration in the treatment target water; a pressure measurement unit which measures a transmembrane pressure of the separation membrane; transmembrane pressure increase speed comparing means which compares a transmembrane pressure increase speed selected on the basis of the value of the organic substance concentration measured by the organic substance concentration measurement means, with a transmembrane pressure increase speed calculated from the transmembrane pressure measured by the pressure measurement unit; and a control unit which controls the membrane surface aeration flow amount of the membrane surface aeration device, wherein the control unit changes the membrane surface aeration flow amount on the basis of the difference between the transmembrane pressure increase speeds, obtained by the transmembrane pressure increase speed comparing means.

A water purification system includes a high temperature water tank, a flameless heat source, a cylindrical vessel (hydrocyclone nest), a first pump, a steam production meter, and a steam condenser and heat exchanger. The contaminated water is heated within the high temperature water tank using the flameless heat source. The heated contaminated water heats the cylindrical vessel and one or more sets of hydrocyclones. The heated contaminated water is pumped into the cylindrical vessel such that the heated contaminated water enters a tangential inlet of the hydrocyclones, the hydrocyclones separate the heated contaminated water into steam and solids/concentrate, the steam exits through an overflow of the hydrocyclones and a first outlet of the cylindrical vessel, the solids/concentrate exit through an underflow of the hydrocyclones and a second outlet of the cylindrical vessel. The steam is condensed into purified water using the steam condenser and heat exchanger.

A vaporizer 10 comprises: a vaporization chamber 12 for storing a liquid; a bottom heater 14B provided in the vaporization chamber 12 which includes a winding portion 141, acting as a heat source, to contact with the liquid stored in the vaporization chamber and an upright portion 142 erected from the winding portion and having an end portion with a heater terminal 143; and a relief valve 16 connected to the vaporization chamber 12. The vaporizer 10 is configured to be able to appropriately vaporize and supply ultrapure water.

A method and apparatus for diffusing or reducing gas into a liquid is described. This invention covers several different methods for infusing or reducing gas into a liquid with a feedback loop that monitors specific parameters of the process and can vary controls to achieve a targeted value or keep within a range of values. The parameter of interest is the ORP (Oxidative Reduction Potential) and one way to determine that value is using an ORP sensor to directly measure it at various points in the process such as on the untreated incoming process fluid, right after infusing the reducing gas, or later in the process such as where the fluid is discharged back into the original tank in the case of a recirculating system or when it is discharged to the next phase of the treatment train.

Disclosed are floating micro-aeration unit (FMU) devices, systems and methods for biological sulfide removal from water/wastewater bodies and streams. In some aspects, a system includes a manifold structure including one or more opening to flow air out of an interior of the manifold structure; one or more support structures connected to the manifold structure, in which the one or more support structures are floatable on a surface of a fluid that includes water or a wastewater; and an air source that flows air to the manifold structure, such that the manifold structure supplies the air containing a predetermined amount of oxygen (e.g., less than 0.1 mg/L of oxygen) to oxidize sulfide of the fluid.

An apparatus for covering a water container having an open top and treating a source water therein. The apparatus has one or more dividing walls mountable to an interior space of the water container for partitioning it into multiple water-treatment zones, and a cover mountable to at least a portion of the open top of the water container above the one or more dividing walls. Each dividing wall has or forms one or more openings for directing the source water from one water-treatment zone to the next. The cover has one or more vaulted cover sections each defining a gas chamber above the dividing walls. Each cover section has a condensation surface in the corresponding gas chamber for condensing a steam evaporated from the source water to clean water, and at least one water-collection channel coupled to at least one side of the condensation surface for collecting the condensed clean water.

A gas hydrate desalination system that includes a reactor with a detachable water jacket and thermocouples. The reactor has a detachable lid having a liquid inlet, a gas inlet, sapphire glass lenses, and lid cameras. An exit concentrate channel is provided at a bottom of the reactor. A mixing unit of the system includes a liquid storage tank connected to the reactor through the liquid inlet, and a gas feed cylinder connected the reactor through the gas inlet. A resolving unit of the system includes a sieve filter column for filtering brine from gas hydrate. The sieve filter column is connected to the exit concentrate channel and a first fraction column, which is connected to a brine column. The channel is further connected to a second fraction column, which is connected to the brine column for separating freshwater from the gas hydrate.