The invention provides a water treatment composition comprising a cathodic inhibitor comprising at least one rare earth metal, an anodic inhibitor comprising at least one polycarboxylic acid, and a polymer dispersant comprising at least one sulfonic group. The invention also provides a method of inhibiting corrosion of a metal in an industrial water system, which method includes treating water of the industrial water system with the composition of the invention, to provide treated water.

Glycine is an organic compound that can be used in the making of a synthetic base that obviates all the drawbacks of strong bases such as sodium hydroxide. The new compound is made by dissolving glycine in water and adding calcium hydroxide at a molar ration of about 1:1. Next, sodium percarbonate is dissolved in the solution to produce the new compound, which can be referred to as glycine hydroxide.

Described is a system and corresponding method for remediating liquid waste streams. The system includes an electro-oxidation (EO) chamber, an electro-deposition (ED) chamber, and an electro-adsorption (EA) chamber. In the method, a waste stream is subjected to electro-oxidation, followed by electro-deposition and/or electro-adsorption. The method removes both organic and inorganic pollutants, as well as metals present as free ions or bound into organic or inorganic complexes.

The present invention makes public a method and an apparatus for the revalorization of various organic waste, by means of physics and mechanics. The bubbles are produced and injected into the mixture in the sealed tank under depressure, then establish the movement of toric rotation in the vertical direction. The high-speed movement bubble carrying focused energy vigorously collide into the mixture, thus showing the Rheo-fluidizing effect (Shear thinning), decreasing the viscosity and depolymerizing long-chain molecules. This achieves active bacteria killing, separation, concentration and de-emulsification; the solution's advantage is applied to various organic residue, with short and efficient processing cycles, without producing unpleasant odors and is non-polluting, chemical free, at low temperature, low energy consumption, no GHG emission, preserving the microorganisms and nutrients of organic matter, and separating the pollutants such as the oils and fats. The usage of the output is unlimited, the invention is helpful to restore the ecosystem.

This invention proposes the use of Thermal Hydrolysis (or Thermal Carbonization) at different temperatures and pressures in alternate waste streams to achieve an optimal mix of high digestion rates and pasteurization rates while still achieving large viscosity reduction. In the disclosed embodiments means of combining Thermal Hydrolysis (or Thermal Carbonization) and Pasteurization including but not limited to placing the waste streams in parallel, placing them in series, utilizing heat input in parallel and heat exchangers in series are explored to optimize hydrolysis rates, minimize the use of high pressure tanks, optimize energy used, and manage viscosity characteristics of the solids.

Aspects of the invention include a porous and water-permeable electrode for electrocatalysis comprising: a porous and water-permeable reactive electrochemical membrane (“REM”) comprising: a porous and water-permeable support membrane; wherein the support membrane comprises a titanium metal; and an electrocatalytic coating on at least a portion of the metal support membrane, the electrocatalytic coating being a tin oxide bilayer comprising: a first layer adjacent to and directly contacting the metal support membrane; wherein the first layer comprises tin oxide doped with antimony; and a second layer adjacent to and directly contacting the first layer; wherein the second layer forms a surface of the REM such that the second layer is in direct contact with an aqueous solution when the REM is in contact with the aqueous solution; wherein the second layer comprises tin oxide doped with antimony and nickel or cerium. Preferably, the support membrane is formed of a titanium metal.

The present invention relates to the technical field of environmental engineering, and particularly relates to a method for treating and recycling waste slurry in bobbin paper production. The present invention employs aerobic granular sludge technology-based two-stage process of treating and recycling waste slurry in bobbin paper production, and has features of low agent feeding, small floor space occupation, a short operating cycle, and easy controllability. By treating a high-load waste slurry in an adsorption section having aerobic granular sludge, fibrous materials in the waste slurry can be concentrated efficiently and resource substances can be recycled. By treating water discharged from the adsorption section with aerobic granular sludge in a biochemistry section, a water release can be guaranteed to stably meet the standard. By employing the method, the amounts of the fibrous materials and proteins adsorbed by the aerobic granular sludge in the adsorption section reach 710 mg/g MLSS and 140 mg/g MLSS respectively, the concentrations of COD, NH4-N, TP and SS of water released from the biochemistry section are 98 mg/L, 4.1 mg/L, 0.8 mg/L and 100 mg/L respectively, and the removal rates of COD and SS reach 98.8% and 96.2% respectively, enabling water release to meet a corresponding release standard.

A process for the treatment of wastewater (S1) formed during the production of starches, in particular of chemically modified starches, and which contains dissolved salts and organic compounds, in which process it is proposed that the wastewater (S1) or pretreated wastewater (S1) containing substantially the dissolved salts and the organic compounds of the wastewater (S1) is subjected to a membrane separation process in which a separation of the wastewater (S1) supplied to the membrane separation process into a first volume flow (S3) with a higher concentration of dissolved salts in relation to the supplied wastewater (S1) and a second volume flow (S2) with a reduced concentration of dissolved salts in relation to the supplied wastewater (S1) is performed, wherein the first volume flow (S3) is subjected to thermal treatment for the separation of the dissolved salts and of a third volume flow (S9) which contains a fraction of the organic compounds of the wastewater (S1). By means of the invention, a process for the treatment of the wastewater (S1) from the production of modified starches with recovery of utilizable contents is provided.

In some embodiments, a method may include reducing the microbial load in contaminated water of water recycle loops. These water recycling loops may include pulp and paper mills, cooling towers and water loops, evaporation ponds, feedstock processing systems and/or non-potable water systems. The methods may include providing a peracetate oxidant solution. The peracetate solution may include peracetate anions and a peracid. In some embodiments, the peracetate solution may include a pH from about pH 10 to about pH 12. In some embodiments, the peracetate solution has a molar ratio of peracetate anions to peracid ranging from about 60:1 to about 6000:1. In some embodiments, the peracetate solution has a molar ratio of peracetate to hydrogen peroxide of greater than about 16:1. The peracetate solution may provide bleaching, sanitizing and/or disinfection of contaminated water and surfaces. The peracetate oxidant solution may provide enhanced separation of microbes from contaminated water.

A method is disclosed for monitoring and controlling treatment of a waste water stream. The method includes measuring UV absorbance of a waste water influent and/or waste water effluent, measuring turbidity of the waste water influent and/or waste water effluent, and determining the concentration of dissolved organics in the waste water influent and/or waste water effluent based on the measured UV absorbance. The method includes controlling the dosing of at least one coagulant to the waste water influent based on the measured UV absorbance and/or the determined concentration of the dissolved organics, and optionally based on the measured turbidity, and optionally controlling the dosing of at least one flocculant to the waste water influent based on the measured turbidity.