摘要:
A method for treating organic waste water, wherein after forming flocs by adding a polymeric flocculant to organic waste water in which organic nitrogen waste components to suspended solids (SS) is 6%/SS to 20%/SS, solids are separated from liquid to separate said flocs from said organic waste water.
摘要:
To efficiently separate water containing components originating from coal tar or crude oil and forming an o/w emulsion, such as ammonia-containing wastewater from a coke oven of an ironworks or wastewater from an atmospheric distillation unit, an FCC unit, an RFCC unit, or a desalter of an oil refinery, into oil and water. A method for separating an o/w emulsion into oil and water includes adding a phenolic resin to an o/w emulsion including a component originating from coal tar and/or crude oil. A coagulant is preferably further added to the o/w emulsion. An organic coagulant is particularly preferable. It is possible to efficiently separate the o/w emulsion into oil and water in a short time to produce treated water in which the amount of oil components has been reduced. Since a phenolic resin is not an inorganic substance, reusing separated oil components including the phenolic resin does not impose any problem.
摘要:
Provided is a water-purifying agent formed of a granulated product including a mixture of a plant powder and a polymeric flocculant, wherein a surface of the granulated product includes a coated portion in which the plant powder is coated with the polymeric flocculant and a non-coated portion in which the plant powder is not coated with the polymeric flocculant.
摘要:
Provided is a water-purifying agent that is excellent in water purifying performance, can be suitably used in an automated wastewater purification apparatus, and is formed of a granulated product including a mixture of a powder of Corchorus olitorius and a polymeric flocculant, wherein a median diameter of the granulated product is 250 micrometers or greater but 850 micrometers or less.
摘要:
The invention relates to a method for treating an aqueous suspension of solid mineral particles arising from the extraction of ores, comprising the following steps: a soluble polymer is prepared in water, comprising: o at least one non-ionic monomer, selected from the group consisting of acrylamide; methacrylamide; N-monoderivatives of acrylamide; N-monoderivatives of methacrylamide; Ν,Ν-derivatives of acrylamide; Ν,Ν-derivatives of methacrylamide; acrylic esters; methacrylic esters; N-vinylformamide; and N-vinylpyrrolidone; o at least one anionic monomer representing between 10 and 70 mol%, selected from the group consisting of monomers having a carboxylic functional group and salts thereof; monomers having a sulphonic acid functional group and salts thereof; monomers having a phosphonic acid functional group and salts thereof; o at least one cationic monomer representing between 0.2 and 6 mol%, selected from the group consisting of diallyldimethylammonium chloride, methacrylamidopropyltrimethylammonium chloride and acrylamidopropyltrimethylammonium chloride; adding said soluble polymer into the water having the aqueous suspension of solid particles. This method is particularly useful for treating residues resulting from the extraction of bituminous sand.
摘要:
A remote submerged chain conveyor system for separating particles from a coal ash/water slurry from one or more remotely located boiler units. A tank forms an ash holding section, a dewatering section, and an ash settling section. The ash holding section receiving the slurry with first and second opposite ends. The dewatering section dewaters the slurry. The settling zone is an elongated trough connected with the ash holding section at one end with a discharge drain trough at near an opposite end. The tank sections being oriented in a generally linear arrangement wherein a net flow of water from the ash/water slurry is in a direction from the settling zone toward the distal and. A drag chain moves along the ash settling conveying the particles settling from the slurry to the dewatering section.
摘要:
The water treatment system comprises: an aluminate ion addition part 14c for adding an aluminate ion additive 14a to water to be treated containing at least salt content and silica; a first precipitation part 16 provided on the downstream side of the aluminate ion addition part 14c so as to precipitate and separate the solid content in the water to be treated 11; a first pH adjustment part 17c provided on the downstream side of the first precipitation part 16 so as to adjust the pH to a first pH level which precipitates the residual aluminum in the water to be treated 11 by supplying a first pH adjusting agent 17a; a first solid/liquid separation part 18A for separating the solid content in the water to be treated 11; a second pH adjustment part 19c for adjusting the pH of the water to be treated 11 from the first solid/liquid separation part 18A to a second pH level; and a first separation membrane (desalination treatment) apparatus 23A provided on the downstream side of the second pH adjustment part 19c so as to separate the water to be treated 11 into first permeated water 21 A and first non-permeated water 22A by removing the salt content in the water to be treated 11.
摘要:
The water treatment system comprises: an aluminate ion addition part 14c for adding an aluminate ion additive 14a to water to be treated containing at least salt content and silica; a first precipitation part 16 provided on the downstream side of the aluminate ion addition part 14c so as to precipitate and separate the solid content in the water to be treated 11; a first pH adjustment part 17c provided on the downstream side of the first precipitation part 16 so as to adjust the pH to a first pH level which precipitates the residual aluminum in the water to be treated 11 by supplying a first pH adjusting agent 17a; a first solid/liquid separation part 18A for separating the solid content in the water to be treated 11; a second pH adjustment part 19c for adjusting the pH of the water to be treated 11 from the first solid/liquid separation part 18A to a second pH level; and a first separation membrane (desalination treatment) apparatus 23A provided on the downstream side of the second pH adjustment part 19c so as to separate the water to be treated 11 into first permeated water 21 A and first non-permeated water 22A by removing the salt content in the water to be treated 11.