An organic solid waste anaerobic digestion device based on uncoupling of hydraulic retention time (HRT) from sludge retention time (SRT) includes a self-sustaining air flotation screening tank. A sludge pipe of the self-sustaining air flotation screening tank is connected with a first separating mechanism. A bottom of the first separating mechanism is connected with a second separating mechanism, and two separating mechanisms are connected with a return pipe of the self-sustaining air flotation screening tank. Through the two separating mechanisms, the heavy inert materials at the bottom of the self-sustaining air flotation screening tank can be subjected to swirl separation, so that the liquid part, the solid part and the gas part can be completely separated, and then the useful active materials are conveyed to the reaction device.

An anammox reactor capable of improving nitrogen removal efficiency by maintaining activity of microorganisms, and a water treatment method using the anammox reactor are provided. The anammox reactor includes a raw water feed pipe through which raw water is supplied, a raw water discharge pipe through which raw water is discharged to an outside, and a first chamber configured to accommodate ammonium oxidizing bacteria (AOB) and anammox bacteria for performing an anammox process, wherein the raw water feed pipe and the raw water discharge pipe are configured to communicate with the first chamber.

An induced sludge bed anaerobic reactor system that includes at least two stages of bioreactor processing, a first-stage feeding system, a second-stage feeding system, a pH balancing system, an effluent recirculation system, a gas management system, and a controller. In addition, any given stage of reactor processing may be comprised of a plurality of reactors that are configured to operate in parallel with each other.

A denitrification biofilter device, including: a regulating pool, a reactor body, a water tank, a first doser, a second doser, a backwash pump, a water inlet pump, and a blower. The regulating pool includes a raw water inlet and a water outlet. The reactor body includes a uniform water distributor, a filler layer, a buffer layer, a filter layer, a supporting layer, a filler supporting plate, a backwash water outlet, a treated water outlet, and a backwash water inlet. The treated water outlet and the backwash water inlet are disposed at the bottom of the reactor body and are connected to the water tank via pipes. The filler layer is filled with zeolites having a grain size of between 4 and 8 mm, a density of between 1.9 and 2.6 g/cm.sup.3, a porosity greater or equal to 48%, and a specific surface area of between 570 and 670 m.sup.2/g.

A system for flushing a conduit having an inlet, an outlet, and at least one flow restricted outlet between said inlet and said outlet. There is a pump operative to periodically be turned on and off for pumping a liquid from a liquid source to the inlet, a pressure pulse being generated when the pump is turned on. A hydraulically actuated indexing valve has an inlet connected to the second outlet end of the conduit, the indexing valve including a valve element assembly indexable between a plurality of indexed positions in response to a plurality of pressure pulses, wherein in at least one of the indexed positions, return flow from the second outlet end of the conduit flows through the outlet of the valve to increase flow rate through the conduit.

Auger cleaned inaccessible floor systems to maximize operational capacity of inaccessible floors. The auger cleaned inaccessible floor system includes a floor having at least one channel beneath the lowest point of the floor extending horizontally at least half the length of the longest dimension of the floor and adapted for receiving an auger cleaner, at least one gate complex that provides fluid communication between the channel and at least one box and further provides access to the floor for the auger cleaner, and at least one box to deliver the auger cleaner to the channel and adapted for equalizing pressure when the inaccessible floor is under water to deliver an auger cleaner for cleaning. Thus, the auger cleaned inaccessible floor system allows cleaning of the inaccessible floor while the inaccessible floor system is in operation increasing the yield from the inaccessible floor system.

A system and method using a subterranean biological reactor can include a pre-reactor storage unit configured to receive a feedstock including a slurry of biologically derived material and at least one pump configured to pump the effluent from the pre-reactor storage unit. The system may include at least one wellbore containing a subterranean biological reactor configured to receive the effluent from the pre-reactor storage unit. At least a portion of the subterranean biological reactor may be configured to perform anaerobic digestion upon the effluent to generate a biogas.

Devices for controlling to remove food waste digestion foam are provided. The device includes a digestion tank. The digestion tank includes two hermetically sealed boxes. Each of the two boxes is opened with a liquid inlet connected to an interior of each of the two boxes. A conveying mechanism is connected between the two boxes. The conveying mechanism conveys a gas in the two boxes in a reciprocal manner. The gas in the two boxes is conveyed in the reciprocal manner through the conveying mechanism to generate a pressure difference between the two boxes distributed left and right to remove the foam, which adopts physical defoaming without adding any reagent, is cost-effective and efficient, and does not affect an anaerobic reaction process due to addition of a chemical defoaming agent. The entire device has a simple structure and is easy to operate, and the process is controllable.

In one or more arrangements, a cleaning system for cleaning a floor of a closed system is presented which has a cleaner configured to clean the floor of the closed system, and the cleaner enters the closed system at a position located below a surface level created by liquid within the closed system. In one or more arrangements, the cleaning system may contain a gate complex configured to allow selective access into the closed system. In one or more arrangements, the cleaning system may contain a box system and wherein the cleaner is initially positioned at least partially within the interior volume of the box system.

Large sealed anaerobic digestor ponds with thin rubber membrane covers to absorb sunlight efficiently in selective sunlight absorption coating and low emissivity in infrared and transparent insulation layers. Flow of pond byproduct gas and heat transfer to circulate slurry liquid controlled by pressurization and weighting of gas collection cover membrane to provide sloped buoyant bubble gas flow gas collection channels in deformed membrane. Low gas pressure used between layers to increase heat transfer to digesting slurry when low wind and prevent wind lift-off with high winds. High gas pressure used between membrane layers to remove sloped collection channels, permit thickened foam over digesting slurry and reduce heat transfer at night. These large-scale solar heating digesting ponds can maintain sufficient digestion temperature to accelerate digestion, maximize gas production efficiency, and minimize greenhouse gas emissions.