Disclosed herein are the water clarification compositions and method of using the disclosed water clarification compositions for clarifying a water system or waste water source. Specifically, the disclosed compositions comprise and methods use multiple charged cationic or anionic compounds that are derived from polyamines through an aza-Michael addition with an activated olefin having an ionic group. The disclosed water clarification methods or compositions are found to be more effective than those methods or compositions including commonly used single quaternary compounds for reducing turbidity in water systems or waste water sources.

A water treatment system including a filter compartment having a filter material adapted for removing at least one of neutrons and alpha particles from water. The filter material may comprise at least one of paraffin, cadmium, and bismuth. The filter compartment can also have a second filter material adapted for removing at least one of chloride ions and transmuted chlorine ions from the water. The second filter material may comprise at least one of coconut carbon, silicon dioxide, and ionized sand. The system can further include a container downstream of the filter compartment, the container having paraffin therein. Additionally, the system can include an absorptive manifold designed for absorbing hydrogen ions and reducing the pH of the water. A method for treating contaminated water using the water treatment system is also provided.

A method and system for effectively desalinating a feed stream is provided. In one embodiment, a feed stream is desalinated by a Brine Forward (BF) desalination system, which comprises an enabling de-scaling step combined with a plurality of multi-stage flash (MSF) trains arranged in series, wherein the de-scaling step is conducted within a MSF first train at a top temperature. With the aid of the de-scaling step, the system obviates or reduces many of the well known disadvantages of the desalination practice along with their expenditures and environmental burdens. The elimination of otherwise intractable substantial operating and silent environmental costs of such disadvantages, in itself, may over defray the de-scaling step's cost and with greater benefits to the overall system's performance and distillate production. Furthermore, all of the products from the de-scaling step are commercially viable, and if desirable or necessary, all of the de-scaling step's additives are also recyclable.

The purpose of the present invention is to provide a treatment method by which, even for wastewater with organic constituents constituting a large portion of organic wastewater as a whole and suspended solids (SS) and with a large negative charge ratio, organic nitrogen constituents and phosphorus compounds can be efficiently separated and collected and good-quality separated water can be obtained by reducing the quantity of SS, BOD, COD, and nitrogen constituents in the separated water. Provided is a treatment method for organic waste water, in which a flock is formed by adding a polymer flocculant to organic waste water with organic nitrogen constituent content in relation to suspended solids (SS) being 4-50%/SS and organic nitrogen constituent content being 250-50,000 mg/L, and thereafter, the flock is separated from the organic wastewater by solid-liquid separation.

A method for detecting and controlling the amount of cationic species in a water stream in accordance with embodiments of the present disclosure is carried out by adding a solution containing a pre-determined quantity of a fluorescent tracer to the sample of water stream to obtain a solution comprising a complex. The fluorescence emission spectra of the solution is measured for detecting the presence or absence of the cationic species based on the attenuation and shift of the emission peak in the range of 640 nm to 655 nm.

Provided is a polymer composition containing a water-soluble cationic copolymer P2 structured in micro-blocks obtained by radical polymerization of at least one non-ionic monomer and at least one cationic monomer, in the presence of a homopolymer P1 having an average molecular weight between 5,000 and 100,000 daltons, the homopolymer P1 having been prepared from 2-acrylamido-2-methylpropane sulphonate in salified form and in the presence of 200 to 20,000 ppm by weight of 2-methyl-2-propenyl-sulphonic acid in salified form. Related methods are also provided.

A method for gelation of a waste water stream comprising the steps of: Introducing water soluble, crosslinkable polysaccharide into a waste water stream to form a treated stream having an initial liquid content; and drying the treated stream to remove at least 50% by weight of the initial liquid content in the treated stream. The treated waste stream may be solidified to pass the paint filter test.

[Solution] Provided is a water purification agent suitable for use in an automated purification treatment device, when a wastewater purification treatment using a plant-derived water purification agent is performed with the automated purification treatment device. The water purification agent is a granulated product containing a mixture of a plant powder and a polymer coagulant.

Disclosed herein are the water clarification compositions and method of using the disclosed water clarification compositions for clarifying a water system or waste water source. Specifically, the disclosed compositions comprise and methods use multiple charged cationic or anionic compounds that are derived from polyamines through an aza-Michael addition with an activated olefin having an ionic group. The disclosed water clarification methods or compositions are found to be more effective than those methods or compositions including commonly used single quaternary compounds for reducing turbidity in water systems or waste water sources.

A carbon disulfide-modified amine additive may be introduced to an aqueous stream in an effective amount to separate oil from the water in the aqueous stream, such as separating at least some of the oil from emulsified oil-in-water in a production fluid, where the oil is crude oil. The carbon disulfide-modified amine additive may be produced from a reaction of synthetic amine, natural amines, or chemically modified natural amines with carbon disulfide and an ,-unsaturated compound and/or an epoxide in one step. In one non-limiting embodiment, the amine is a natural amine or chemically modified natural amine of a polysaccharide containing amino functional group(s). Optionally, a base catalyst is used to make the carbon disulfide-modified amine additive.