A method for treating a wastewater effluent includes carbon pollution, nitrogen pollution and phosphorus pollution, in a sequencing batch reactor (SBR), the SBR comprising: a chamber capable of containing a wastewater-sludge mixture comprising various levels; a sludge bed, comprising PAOs, located at the bottom of the chamber, above which a sludge blanket level is defined; means for determining a minimum level and a maximum level for extracting sludge in the chamber; extraction means capable of extracting sludge at variable levels between the minimum extraction level and the maximum extraction level; the method comprising: a step of supplying the SBR, during which an amount of effluent to be treated is introduced near the bottom of the chamber, in the sludge bed; a reaction sequence comprising: at least a first anaerobic step, during which the PAOs capture the carbon pollution and release phosphorus compounds; optionally, a second step of anoxic denitrification; a third aeration step, allowing the dephosphatation of the effluent by the PAOs to be carried out; a decanting step, during which sludge is deposited at the bottom of the chamber and the content of the chamber clarifies in the vicinity of its surface; a recovery step, during which a clarified fraction is drawn off from the content of the chamber, with the recovery and supply steps taking place simultaneously; and a step of extracting at least a portion of the light sludge at a predetermined level.

Waste water is remanufactured with ozone in a series of mixing vessels. The ozone is dispersed to both a top and a bottom portion of each mixing vessel, but in different amounts. This creates an electrical potential difference across the height of each mixing vessel which significantly improves the oxidation of organic carbon-based impurities and eliminates H2S and bacteria. Sludge and solids floating to the top of each mixing vessels are removed, as well as sludge and solids settling to the bottom of the mixing vessels. When oil and gas well waste water is treated in this manner, the resulting treated water is purified and has a high salt content suitable for oil or gas well injection.

A method of preparing and separating biopolymers and biopolymer fractions is useful for wastewater treatment applications from sewage sludge. The method comprising the steps of disrupting the bacterial cell walls of bacteria present in the sewage sludge by at least 75% to release the intracellular contents of the bacterial cells and separating the biopolymers from any contaminants present.

Methods of delivering microorganisms loaded onto an inorganic porous medium. Methods of treating wastewater to increase effluent and biosolids quality. Methods of reducing ammonia and denitrifying wastewater effluent. Methods of reducing phosphorous concentration in wastewater effluent. Composition of biosolids derived from wastewater treatment. Wastewater treatment assemblage for increasing wastewater effluent and biosolids quality.

The present invention discloses a treatment process for a submerged lifting circulation type bio-membrane filter, wherein the treatment process comprises the following steps: two groups of symmetrically staggered filter curtains (2A and 2B) are adopted; the two groups of filter curtains (2A and 2B) are periodically lifted up and down in a reciprocating manner in a biofilter (1) under the action of a lifting mechanism (4), so that bio-membranes on the two groups of filter curtains (2A and 2B) are in contact with the atmosphere and sewage in turns, absorb organic matters in the sewage when lifting down for submerging, absorb oxygen when lifting up and exposing into to the atmosphere, and bring oxygen into the sewage and cause sewage turbulence in a water tank when lifting down for submerging again, so that the dissolved oxygen is uniformly distributed, thereby purifying the sewage.

In a system and process, sludge from a wastewater treatment plant is treated in a high solids digester, optionally a mechanically mixed wet digester. Sludge (i.e. digestate) from the anaerobic digester is thickened or dewatered. Part of the thickened or dewatered digestate is thermally hydrolysed. The hydrolysed digestate may be, or may be further treated to produce, Class A biosolids. The hydrolysed digestate can be dewatered producing a liquid fraction that is recycled to the digester. Another part of the thickened or dewatered digestate is returned to the digester. The return of thickened or dewatered digestate to the digester allows for a smaller tank to be used (compared to a system without a recycle of thickened or dewatered digestate) while maintaining the same solids residence time (SRT) and volatile solids reduction (VSR). In some examples, the hydraulic residence time (HRT) of the digester is 10 days or less.

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.

An oil sludge treatment system includes: a reduced-pressure fermentation dryer; a filtration apparatus; and a cleaner. The reduced-pressure fermentation dryer is configured to: store oil sludge in an airtight container; heat and stir the oil sludge under reduced pressure so that a temperature of the oil sludge is within a predetermined temperature range; decompose organic matter contained in the oil sludge using microorganisms while evaporating water; and obtain volume-reduced dried product. The filtration apparatus filters oil from the dried product. The cleaner cleans, by steam, the dried product from which the oil has been filtered.

A method of processing enhanced biosolids from a wastewater treatment plant to produce an output mixture. The method includes providing one or more volumes of an input mixture that has an input mixture viscosity. The input mixture includes the enhanced biosolids, which have been subjected to shear forces and mixed in a mixing vessel. The enhanced biosolids are partially hydrolyzed biosolids with an input solids content between 4% and 16% by weight of the input mixture. The input mixture also includes sufficient process liquid to result in the output mixture having an output solids content between 3% and 13% by weight of the output mixture. The input mixture is stored in a storage vessel in which the input mixture is subjected to anaerobic conditions and hydrolysis over a predetermined tie period, to form the output mixture having an output mixture viscosity that is less than the input mixture viscosity.