A recycled water treatment system is equipped with different bio-treatment devices to decompose nitrogen-containing inorganic compounds and nitrogen-containing organic compounds in order to enhance efficiency of treating nitrogen-containing organic compounds, wherein an organism-carrying fixed-bed unit is used to efficiently decompose nitrogen-containing organic compounds.

A water processing system includes a pretreatment system disposed within the water processing system. The pretreatment system may treat a feed stream including oil and brine and to generate a first brine stream. The pretreatment system includes a first filtration system that may receive the feed stream, the first filtration system may separate the feed stream into a hydrocarbon stream and an intermediate brine stream, the intermediate brine stream includes a plurality of minerals, and the hydrocarbon stream includes water, the oil, and suspended solids. The water processing system also includes a mineral removal system fluidly coupled to and disposed downstream from the first filtration system. The mineral removal system may receive and remove the plurality of minerals from the first brine stream output from the pretreatment system. The mineral removal system includes a first mineral removal unit that may remove a first portion of the plurality of minerals from the first brine stream and to generate a second brine stream. The water processing system also includes a hydrocarbon removal system disposed within the pretreatment system and fluidly coupled to the first filtration system. The hydrocarbon removal system may receive the hydrocarbon stream, to recover the oil, and to generate a recovered oil stream.

Provided is an aerobic biological treatment method for treating water to be treated with aerobic organisms by dissolving oxygen in the water to be treated within a reaction tank using an oxygen dissolution membrane module disposed in the reaction tank, wherein a bioadhesive carrier within the reaction tank is suspended or fluidized to prevent adhesion of organisms to the oxygen dissolution membrane module.

A composition for use in remediation of soil and groundwater containing hydrocarbons and halogenated compounds. The remediation composition includes: (a) a first bioremediation material including a first blend of organisms capable of degrading the hydrocarbons; (b) a second bioremediation material including a second blend of organisms differing from the first blend of organisms that is chosen for degrading the halogenated compounds; (c) an organic compound such as a complex carbohydrate (e.g., food grade starch); and (d) a third blend of organisms capable of degrading the organic compound. The degrading of the organic compound by the third blend of organisms breaks the complex carbohydrate into smaller molecules that are utilized by the microorganisms of at least one of the first and second bioremediation materials during the degrading of the hydrocarbons and the halogenated compounds. The first bioremediation composition typically includes activated carbon capable of adsorbing the hydrocarbons and the halogenated compounds.

A mixture comprising liquid water, a gas and at least one organic compound are injected into a non-thermal gas-liquid plasma discharge reactor to generate a flowing liquid film region with a gas stream flowing alongside. A plasma discharge is propagated along the flowing liquid film region. Water is dissociated and reactive species such as hydroxyl radicals, hydrogen peroxide and nitrogen oxides are formed. The organic compound reacts with the reactive species such as hydroxyl radicals and hydrogen peroxide present in the flowing liquid film region and in the flowing gas stream to produce organic compound dissociation products. At least some organic compound dissociation products and nitrogen oxides are transferred to a bioreactor for further degradation of organic compounds. The nitrogen oxides are used as nutrients for bacteria in the bioreactor. Feedback control of the plasma reactor is based on conditions detected and determined in the biological reactor.

In some implementations, a method may include introducing into a contaminated media a suspension of a bioremediation composition. In addition, the method may include where the bioremediation composition may include a first bioremediation composition having a first blend of one or more electrolyte solutions capable of ionic conduction and a second bioremediation composition having a second blend of one or more active materials and being capable of electric conduction.

Provided herein is a process for treating water containing natural organic matter (NOM) to produce potable water, the process comprising a plurality of oxidation steps for degrading NOM, wherein the plurality of oxidation steps comprise one or more of subjecting water to inorganic oxidant, oxygenation, catalytic oxidation, and catalytically advanced oxidation (CAO). Also provided herein is a process for treating water for producing potable water, the process comprising a plurality of oxidation steps; wherein the plurality of oxidation steps comprise one or more of fragmentation of NOM with ozone, homogeneous catalytic oxidation with ozone, and catalytically advanced oxidation using granular metal oxide catalyst.

The present invention discloses a purification method for purifying contaminated water, comprising at least one biological purification path as well as a filtration purification path, wherein the filtration purification path is operated at least partially in parallel to the biological purification path with a partial flow which is removed from the biological purification path. The purification method according to the invention can be used as, preferably last, stage of a purification process in a wastewater treatment plant prior to introducing the purified water into a river, lake or the ocean.

There are provided herein methods and systems for increasing efficiency in a multi-stage activated carbon system. The methods and systems provide a cleaned carbon solids fraction and a waste liquor from wet air regeneration, and direct the same to a second stage and a first stage, respectively, of the multi-stage activated carbon system to enhance removal efficiency therein.

A biological wastewater treatment process utilizes biology carriers having recesses or pores defined on their surfaces. Biology form a biofilm or granular biofilm on the surface of the biology carriers and within. The pores or recesses protect the biology. As dissolved oxygen is consumed by biology close to the openings of the recesses or pores, less dissolved oxygen reaches biology living deeper within the pores. The pores thereby define aerobic, anoxic, and anaerobic regions within each biology carrier. Some examples of the biology carriers may be made at least in part from biochar or other partially charred materials. The resulting biological process requires less physical space than conventional flocculant sludge based processes and is more readily established and maintained verses traditional aerobic granular sludge.