673 results about "Calcium hypochlorite" patented technology

A method of treating a coal combustion flue gas, which includes injecting a molecular halogen or thermolabile molecular halogen precursor, such as calcium hypochlorite, able to decompose to form molecular halogen at flue gas temperature. The molecular halogen converts elemental mercury to mercuric halide, which is adsorbable by alkaline solids such as subbituminous or lignite coal ash, alkali fused bituminous coal ash, and dry flue gas desulphurization solids, capturable in whole or part by electrostatic precipitators (ESPs), baghouses (BHs), and fabric filters (FFs), with or without subsequent adsorption by a liquid such as a flue gas desulphurization scrubbing liquor.

The invention relates to a method for realizing desulfuration, denitration and demercuration of boiler smoke synchronously, wherein it comprises feeding smoke into cycle fluidize bed reactor, and injecting oxygen-enriched active absorber; said absorber is formed by coal ash at 20-70, lime hydrate at 27-80, additive at 0.5- 3 as kalii permangana KMnO4, sodium chlorite NaClO2, natrii chloridum NaCl, calcium hypochlorite Ca(ClO)2 or acetic hyctro peroxide CH3COOH. The invention's desulfuration efficiency can reach 90%, the denitration efficiency can reach 60%, and the demercuration can reach 50%, with low cost and non pollution.

The invention discloses a wet method smoke gas denitration technology of two segments of liquid phase oxidation and absorption, which adopts solution or mixtures of one or more of potassium permanganate, sodium chlorite, sodium hypochlorite, calcium hypochlorite, oxyful and chlorine dioxide as oxidizing agents to ensure nitrogen oxide in smoke gas contact and react with the oxidizing agents. After the nitrogen oxide is partially oxidized into nitrogen dioxide, oxidized nitrogen oxide in the smoke gas is absorbed by alkali liquid to generate corresponding nitrite. The technology adopts liquid phase oxidation to replace gas phase oxidation so as to reduce the investment and the running cost, simplify the technical process and the system structure, and enhance the operability. Compared with a method that oxidation and absorption are simultaneously carried out in the liquid phase, the two-segment technology not only can increase the removal efficiency, avoid secondary pollution caused by incomplete absorption of NO2, but also can achieve the purposes of selectively generating and recovering the nitrite in the absorption stage by controlling the oxidation degree of the oxidation stage.

An Anti-Terrorism water quality monitoring system for continuously monitoring a potable water treatment system and related potable water distribution network that provides potable water to a municipality, city, housing development or other potable water consumer. The system includes the collection of data from the water distribution system and from the water treatment facility and from advanced separation processes which are integrated into analytical instruments. The data collected are stored in a remote database on a remote server computer or bank of computers and accessible by Homeland Security or its designated agency. Preferred parameters of monitoring include the turbidity and disinfectant such as chlorine, hypochlorous acid, sodium hypochlorite, calcium hypochlorite, ozone, chlorine dioxide, chloramines, hydrogen peroxide, peracetic acid.

A non-Division 5.1 Oxidizer tablet consisting essentially of a blend of hydrated calcium hypochlorite with magnesium sulfate heptahydrate, wherein the blend contains at least about 17% by weight of water based on the total weight of the blend; contains from about 0.1% to about 10% of lime based on the total weight of the hydrated calcium hypochlorate and magnesium sulfate heptahydrate and the average dissolving rate of the tablet is less than 150 grams per day.

A non-Division 5.1 Oxidizer tablet consisting essentially of a blend of hydrated calcium hypochlorite with magnesium sulfate heptahydrate, wherein the blend contains at least about 17% by weight of water based on the total weight of the blend and the dissolving rate of the tablet is less than 150 grams per day.

An Anti-Terrorism water quality monitoring system for continuously monitoring a potable water treatment system and related potable water distribution network that provides potable water to a municipality, city, housing development or other potable water consumer. The system includes the collection of data from the water distribution system and from the water treatment facility and from advanced separation processes which are integrated into analytical instruments. The data collected are stored in a remote database on a remote server computer or bank of computers and accessible by Homeland Security or its designated agency. Preferred parameters of monitoring include the turbidity and disinfectant such as chlorine, hypochlorous acid, sodium hypochlorite, calcium hypochlorite, ozone, chlorine dioxide, chloramines, hydrogen peroxide, peracetic acid.

The wet combined fume desulfurizing and denitrifying process with chloric strong oxidant enhanced urea has the fume to be treated contacted sufficiently with the mixed absorbent liquid containing urea and chloric strong oxidant inside the absorbing reactor so as to eliminate NOx and SO2 through absorption before being exhausted. The chloric strong oxidant is sodium chlorite, sodium hypochlorite, bleaching powder or their mixture. The process has high denitrifying efficiency, high fume purifying effect, simple structure, easy operation and small occupied land. The said process can reach NOx eliminating rate of 75-98 % and desulfurizing efficiency over 95 %.

Stable compositions of calcium hypochlorite containing selected hydrated inorganic salts having a sufficiently high enthalpy and the ability to provide water release to sufficiently quench reactions and reduce the potential for conflagration.

A solid calcium hypochlorite composition comprising a mixture of: solid calcium hypochlorite; a scale-inhibiting effective amount of a primarily scale-inhibiting alkali metal phosphate; and an effective residue-dispersing amount of primarily residue-dispersing alkali metal phosphate.

The invention relates to a method for preparing a composite potassium ferrate solution, which belongs to the chemistry and chemical industry and water treatment agent preparation process technical field. The method comprises the following preparation processes that: firstly, a sodium hypochlorite solution reacts with sodium hydroxide, a white salt substance is generated first and is subject to pumping filtration, then ferric nitrate is added according to a molar mass ratio of sodium hypochlorite to ferric nitrate being equal to between 1.5 and 2.0 to 1, the reaction temperature is between 20 and 45 DEG C, and the pumping filtration is performed after 1.5 to 2.0 hours of reaction; and then a filtrate is added with a saturated potassium hydroxide solution to ensure that the filtrate is transformed into a potassium ferrate solution. Then 0.06 to 0.16mol / L of calcium hypochlorite is added, the reaction temperature is controlled to between 10 and 30 DEG C, the reaction time is between 10 and 30 minutes, and finally the composite potassium ferrate solution with good stability is produced. The composite potassium ferrate solution prepared by the method has good stability, long preservation time, difficult decrease of high iron content, and easiness for industrialized production. The product can be widely used for purification treatment of algae-laden water, city domestic sewage and so on.

The invention provides a chloration method for phenoxyacetic acid and derivatives thereof, which comprises the following steps that: raw materials of the phenoxyacetic acid or the derivatives of the phenoxyacetic acid and chlorinating agents take reaction at a certain temperature in organic solvents under the effect of catalysts, wherein the chlorinating agents can be chlorine gas, sodium hypochlorite, calcium hypochlorite and sulfuryl chloride, the catalysts can be lewis acid and sulfurated substances, and solvents can be dichloromethane, dichloroethane, trichloromethane, carbon tetrachloride, formic acid, ethyl acetate, benzene, toluene, dimethylbenzene, chlorobenzene and o-dichlorobenzene. The method has the advantages that the operation can be carried out under the waterless condition, the generation of a large amount of industrial waste water is avoided, the used catalysts are safe and are easy to obtain, the solvents can be cyclically used, and the industrialization is easy.

Calcium hypochlorite for use in a laundry washing process. The calcium hypochlorite may be provided in a solid form such as a tablet, granule, and / or powder. The calcium hypochlorite of the present invention may also utilize a sequestering agent. Additionally, other adjunct materials may be included. The present invention also relates to a process for using calcium hypochlorite in a laundry washing process.

The present invention is directed to a water treatment composition, comprising: calcium hypochlorite coated with a coating comprising at least one hydrated or anhydrous salt. The present invention is also directed to a water treatment composition, comprising: (a) an inner core layer comprising calcium hypochlorite; (b) one or more interlayers of selected salts positioned on top of said inner core layer, and (c) one or more outer layers of selected salts positioned on top of said interlayer(s).

The invention provides a process for eliminating algae in cooling water system comprising the steps of, filling bactericide and basic substance into cooling water, making the pH value to be 9-14, mixing one or more from Li2O, Na2O, K2O, LiOH, NaOH, KOH, Li2Co3, Na2Co3, K2Co3, LiHCo3, NaiHCo3, KHCo3, Na3PO4, K3PO4, sodium acetate and postassium acetate. While the bactericidal agent is a mixture two or more selected from chlorine, sodium hypochlorite, potassium hypochlorite, calcium hypochlorite, dichloroisocyanuric acid, trichloroiminocyanuric acid, chlorine dioxide, bromine, sodium hypochlorite, potassium hypochlorite, calcium hypochlorite, hydrogen dioxide solution, ozone, quaternaries, and glutaric dialdehyde.

The invention discloses a treatment method for removing total phosphorus from glyphosate weedicide wastewater, which comprises the following process steps of: performing an alkaline hydrolysis and precipitation reaction, performing a Fenton oxidizing reaction, performing catalytic oxidation and precipitation on calcium hypochlorite and the like. The glyphosate wastewater treated by the method has an excellent dephosphorization effect, the total phosphorus content in effluent reaches the three-level standard (TP is less than or equal to 0.5 mg / L) of the national sewage discharge standard (GB 8978-1996). The dephosphorization process is safe, advanced, clean and low in wastewater treatment cost.

The invention aims at floatation separation of arsenic from sulfur in arsenic-containing pyrites. The floatation separation comprises the following steps of: adjusting an ore pulp to keep the pH value of the pulp between 9 and 10; adjusting the potential of the ore pulp to between 350 and 380 millivolts by adding oxidant medicaments of sodium persulfate and calcium hypochlorite; introducing air to increase oxygen content in the ore pulp; and stabilize electrochemical conditions of mineral floatation. During the floatation separation of the pyrites from the arsenopyrites, the potential of the ore pulp is stabilized by adding the oxidant medicaments of sodium persulfate and calcium hypochlorite; the arsenopyrite is suppressed by using a new collector of dianilino dithiophosphoric acid, and regulators of sodium silicate and sodium humate according to a principle of an electrochemical floatation process to make the pyrites such as arsenopyrites, iron pyrites, pyrrhotites and the like acted with a medicament selectively in the subsequent floatation process; and the floatation separation of the pyrites from the arsenopyrites is performed so as to form a sulfur concentrate with low arsenic content.

The invention relates to a method and equipment for standards-reaching treatment of chemical nickel plating waste liquid. The method comprises the steps: adsorbing nickel ions from the chemical nickel plating waste liquid by using an ion exchange method; treating the chemical nickel plating waste liquid subjected to the ion exchange method treatment by using a Fenton method so as to carry out oxygenolysis on part of organic pollutants in wastewater, achieve an oxidated decomplexing effect and convert complex-form metal nickel ions into free-form nickel ions, meanwhile, oxidating organic substances in the waste liquid, destroying carbon chain structures of the organic substances, finally converting the organic substances into carbon dioxide and water, and lowering the COD of the wastewater; treating the chemical nickel plating waste liquid subjected to the Fenton method treatment by using an ammoniomagnesium phosphate precipitation method, carrying out a reaction so as to produce indissoluble ammoniomagnesium phosphate precipitates, thereby removing ammonia nitrogen from the wastewater; carrying out further ammonia nitrogen removal by using a break-point chlorination method; and removing phosphorus from the wastewater by using ozone as an oxidant and calcium hypochlorite precipitation. According to the method and equipment for the standards-reaching treatment of the chemical nickel plating waste liquid, disclosed by the invention, the standards-reaching emission of nickel, phosphorus, COD and ammonia nitrogen can be simultaneously achieved.

A floating dispenser is provided for dispensing a solid, dissolvable water treatment chemical into ambient water. The dispenser includes a bucket having top and bottom ends, a top wall covering the top end, an opening for admitting ambient water into the bucket interior, and a floatation ring that keeps only the top end above water such that the interior is water filled when the dispenser floats. A basket is disposed in the interior of the bucket for carrying a solid, dissolvable water treatment chemical, such as calcium hypochlorite. The basket is buoyant and movable vertically toward the top wall of the bucket. The dispenser includes a refill indicator that indicates when most of a full load of said chemical has dissolved. The refill indicator includes a pair of tabs that are connected to the basket and slidably mounted in slots in the top wall. The tabs extend above the top wall when the buoyant basket floats upwardly, providing a visual indication of the need for a refill that can easily be seen from a side angle.

A method of handling reclaiming assumed pure water for circulating water system comprising the steps of, removing oil from the assumed pure water, depositing, introducing into the circulating water system, charging inorganic alkaline substance to make the pH of cycle water to be 7.0-11, charging germicidal agent and antisludging agent, wherein the alkaline substance is a mixture of two or more selected from NaOH, KOH, Na2Co3, K2Co3, NaiHCo3, and KHCO3, While the bactericidal agent is a mixture two or more selected from chlorine, sodium hypochlorite, potassium hypochlorite, calcium hypochlorite, dichloroisocyanuric acid, trichloroiminocyanuric acid, chlorine dioxide, bromine, sodium hypochlorite, potassium hypochlorite, calcium hypochlorite, and quaternary ammonium salt.

The present invention discloses a wallpaper and a preparation method thereof, wherein the wallpaper comprises 40-80 parts of paper pulp, 10-15 parts of tree bark powder, 1-2 parts of borosilicate, 0.4-0.8 part of nanometer powder, 2-4 parts of calcium hypochlorite, 4-7 parts of polycarbonate, 3-6 parts of polyethylene terephthalic acid ester, 3-5 parts of 2,6-dibenzylidene cyclohexanone, 2-4 parts of carbon fibers, 3-6 parts of diethyl phthalate, 2-5 parts of glass fiber filament, 1-3 parts of carboxymethyl cellulose, 2-4 parts of polyacrylic acid fibers, 0.4-1 part of an anti-forming agent, 8-10 parts of a film forming agent, and 1-3 parts of a dispersant. The wallpaper has characteristics of high reflective property, visual angle balance improving and gain increasing so as to provide high projection effect, good image saturation degree and high definition, and further has characteristics of green environmental protection, wear resistance and good stability.

The invention provides a production method of special anti-counterfeiting rice paper for a postage stamp, which comprises the following steps: adopting wingceltis barks and straws from sand fields as raw materials, preparing pulp through soaking, beating and bleaching with calcium hypochlorite bleach solution; purifying the prepared pulp, fetching paper, drying, and cutting to manufacture raw rice paper; performing the alum dragging treatment of the raw rice paper in alum solution, and naturally drying the rice paper to obtain non-absorbent rice paper; and applying glue on the back of the non-absorbent rice paper, and drying and flattening to manufacture the special anti-counterfeiting rice paper for the postage stamp. Since the production method in the invention is an improvement based on the conventional production process, the produced rice paper not only preserves the properties of the conventional rice paper, but also has excellent printing applicability. Therefore, the rice paper can be used as the special anti-counterfeiting rice paper for stamps, stamped postcards and other postage stamps.

The present invention is directed to a granular water treatment composition, comprising: 35-95 wt % calcium hypochlorite; 1 to 50 wt % magnesium sulfate or a hydrate thereof; 0.1 to 10 wt % lime; and 0.1 to 55 wt % of a water soluble zinc salt or a hydrate thereof; wherein the weight percents are based on the total weight of the composition. The present invention is also directed to a water treatment tablet, comprising 35-95 wt % calcium hypochlorite; 1 to 50 wt % magnesium sulfate or a hydrate thereof; 0.1 to 10 wt % lime; and 0.1 to 10 wt % of a water soluble zinc salt or a hydrate thereof; wherein the weight percents are based on the total weight of the composition.

Calcium hypochlorite compositions that are classified as a Packing Group III Division 5.1 oxidizer material or as a non-Division 5.1 oxidizer material are described. In one embodiment, the compositions comprise an admixture of particulate calcium hypochlorite and particulate metaboric acid. The calcium hypochlorite is present in the composition in an amount and is of a concentration such that the composition would be classified as a Packing Group II Division 5.1 oxidizer in the absence of said particulate metaboric acid. Other embodiments described are solid shaped articles, e.g., tablets, comprising the described calcium hypochlorite-metaboric acid composition.

The invention relates to a processing method of garbage leachate, which comprises the following steps: 1) adding sodium hypochlorite into garbage leachate to carry out preoxidation; 2) adding ferrous iron and hydroxide, stirring, and separating out the supernatant; and 3) adding ferrous iron and hydrogen peroxide into the supernatant, stirring, and regulating the pH value of the effluent water to reach the standard. Aiming at the garbage leachate after biochemical treatment, the invention is composed of sodium hypochlorite reinforced ferrous iron coagulation and Fenton technique. The sodium hypochlorite reinforced ferrous iron coagulation can remove nondegradable organic substances in the leachate, and generate active chlorine to effectively remove ammonia nitrogen. In the Fenton technique, ferrous iron and hydrogen peroxide in a certain proportion are added to generate hydroxy free radicals, thereby further oxidizing the organic substances and implementing partial mineralization, lowering the toxicity of the leachate and enhancing the biochemical quality of the leachate.

The invention relates to a liquid phase method for removing dioxin-like compounds from flue gas and a device thereof. The invention is used for solving the problem of the dioxin-like compound removal in the incineration flue gas, which utilizes an absorbent to absorb the dioxin-like compounds in the flue gas in a jet bubbling reactor at the temperature of 50-120 DEG C and finish the purification process; the absorbent consists of an absorption liquid and an additive and the absorption liquid is the mixing solution of sodium chlorite and sodium hypochlorite, wherein the concentration of NaClO2solution is 0.01M to 0.1M per liter and the concentration of NaClO solution is 0.01M-0.08M per liter. The additive is one of calcium hypochlorite, sodium bicarbonate, hydrogen peroxide or disodium hydrogen phosphate and the dosage of the additive is 0.001M-0.05M per liter. The invention has removal rate of 94 percent to 98 percent and absorbent utilization ratio higher than 97 percent and is characterized by high removal efficiency, low investment and operation cost, simple device, stable operation, convenient use and the like.

The invention discloses a production method of 3,3-biethylene sulfate. The production method comprises the following steps of by using thionyl chloride and erythritol as reaction raw materials, performing addition reaction, so as to obtain an intermediate, namely 3,3-biethylene sulfite; performing oxidizing reaction with sodium bicarbonate, sodium hypochlorite and a catalyst; finally, distilling molecules, so as to obtain the 3,3-biethylene sulfate. The 3,3-biethylene sulfate prepared by the technical scheme has the advantages that the purity can reach 99.5% or above, the water content is less than or equal to 100PPM, and the acid value is less than or equal to 100PPM; after the 3,3-biethylene sulfate is used as an electrolyte additive of a cell, an SEI film is formed on a negative electrode, the negative electrode is effectively protected, the degrading of capacity at high temperature is prevented, and the property of the cell at high temperature is effectively improved.

An environment protection type multifunctional fuel is prepared from 7 primary components including light hydrocarbon, light oil, gasoline, diesel oil, etc and 20 secondary components including sodium hydroxide, water alcohol, hydrogen peroxide, etc. which are divided into 4 groups which take part in chemical reactions to generate cosolvent, oxygen increaser, combustion aid, smoke reducing agent, etc.