A method may include providing a humidification-dehumidification unit proximate one or more abandoned wells, circulating a water feed through the one or more abandoned wells, using geothermal heat in the one or more abandoned wells to heat the water feed, directing the heated water feed to the humidification-dehumidification unit, and treating the heated water feed in the humidification-dehumidification unit to provide purified water.

The present application relates to a field of excrement treatment equipment in particular, relates to an ultra-high temperature excrement solid-liquid separation extrusion sterilization integrated machine. It includes a solid-liquid separator, a workbench and an extrusion sterilization device. The solid-liquid separator is disposed on the workbench. The extrusion sterilization device includes an extrusion sterilization motor, an extrusion feeding assembly, a receiving pipe, a receiving box and a dehydrating cage.

Disclosed are decoupled systems and methods for producing an oxidized liquid. The method comprises the steps of generating an ozone strong water in a mass transfer unit, mixing the ozone strong water with a process liquid in a mixing unit to form a homogeneous and gas-free mixture of the ozone strong water and the process liquid, forwarding the homogeneous and gas-free mixture to a reaction unit, and producing the oxidized liquid in the reaction unit. The method utilizes the acidic feed liquid to generate ozone dissolved in water having a higher concentration at a saturated or nearly saturated concentration compared to prior art processes at atmospheric pressure and neutral or alkaline pH.

The invention relates to a method and a device for anaerobic digestion from an organic liquid sludge (21), comprising, in a known manner, a step of hydrolysis/acidogenesis of the sludge in a digester (47, 100), a step of acetogenesis for producing acetate from the hydrolysed sludge and a step of methanogenesis from the acetates for producing methane. The method comprises an initial step of creating a hydrolysed sludge emulsion (23) obtained by means of the impact of the sludge with gas (27) injected into the sludge, then continuously supplying the hydrolysed sludge to a reactor (25, 101) pressurised in line relative to the digester, before discharging said sludge from the reactor via a member (29) generating a pressure drop in the hydrolysed sludge, the initial stage being repeated at least once before supplying the, and/or via the, digester.

The present invention relates to a sludge concentration and conditioning device, and a method for treating sludge by using the same. To be specific, there is provided a sludge concentration and conditioning device, comprising: a storage device used for receiving and accommodating sludge and including a body and a cover, the body being provided with a sludge outlet and an overflow port, and the cover including a gas outlet for discharging gas; a filtering device disposed between the sludge outlet and the overflow port and used for filtering the sludge so as to achieve solid-liquid separation; a sludge feed device used for conveying sludge from below the filtering device into the storage device; an additive feed device used for conveying an additive from below the filtering device into the storage device; a sludge discharging device connected to the sludge outlet and used for discharging concentrated and conditioned sludge; and a concentrated sludge adjusting device including an adjusting tank in fluid communication with and surrounding the storage device, and used for adjusting the amount of concentrated sludge in the storage device according to the conditioning requirements. The present invention also provides a method for treating sludge by using the sludge concentration and conditioning device.

A system and method of the purification of drinking water, ethanol and alcohol beverages is based on the action of hydrodynamic cavitation processing of microbiological and chemical contaminants, micro particles and colloidal particles. The fluid flow moves at a high rate through a multi-stage cavitation device and filtration module to generate hydrodynamic cavitation features in the fluid flow. The cavitation features generate changes in the velocity, pressure, temperature, chemical composition and physical properties of the liquid. The cavitation features also prevent the deposition of contaminants upon and remove contaminants from the surface of the filter module, reduce the load on the filter elements and increase the life of the filter module.

Per- and polyfluoroalkyl substances (PFAS) are destroyed by oxidation in supercritical conditions. PFAS in water can be concentrated and prepared for destruction in a pretreatment phase. Following annihilation of the PFAS in supercritical conditions to levels below 5 parts per trillion (ppt), the water effluent can be used to recover heat, returned to sub-critical conditions, and then released back into the environment.

Disclosed techniques include liquid purification with pressure vessels. Access to a set of at least two pressure vessels is obtained. The pressure vessels are interconnected using piping and computer-controlled switching valves. A first pressure vessel of the set is filled with a liquid. A second pressure vessel of the set is filled with a pressurized gas. The pressurized gas is sharp interface immiscible with the liquid. Switching valves are controlled to enable the pressurized gas in the second pressure vessel to force the liquid from the first pressure vessel into a purification chamber. Additional switching valves are controlled to enable a third pressure vessel to fill with liquid while a fourth pressure vessel is filled with purification chamber retentate. The liquid is prepurified prior to filling the first pressure vessel. The prepurifying is enabled by compressed air. The purification chamber includes a reverse osmosis chamber.

The subject of the invention is a device for the production of Redox water characterized by an increased amount of molecular hydrogen in its composition. A device for the production of Redox water of potential below −100 mV uses a spirally wound corrugated pipe, a water source, a water pump, a blow-off valve, a vent, and a gauge. The components are connected into one closed system. Water circulating in the closed system of the spirally wound corrugated pipe is kept under specific pressure. For the pipe, a ratio of diameters is in a fixed diameter range, and a ratio of distances between particular coils parallel to one another is within a distance range.

The devices, systems, and methods of the present disclosure are generally directed to using an increase in gas pressure (e.g., through an increase in heat) to move an actuator that at least partially defines a volume containing a feed fluid in fluid communication with a membrane. As the increase in gas pressure moves the actuator, pressure on the feed fluid in the volume may increase beyond a threshold pressure sufficient to move the feed fluid through the membrane. Movement of the feed fluid through the membrane may reduce a volumetric concentration of one or more components of the feed fluid to form a permeate. For example, the increase in pressure may drive the actuator to increase pressure on salt-water in the volume and, ultimately, move the salt-water through the membrane to form the permeate as part of a reverse osmosis process achieved without the use of a mechanical pump.