1788 results about "Sodium chlorate" patented technology

A system is provided for producing hydrogen and oxygen based on decomposition of sodium chlorate (NaClO₃). In a service station, NaClO₃ is produced by a sodium chloride (NaCl) electrolyser. The service station is supplied with water (H₂O), NaCl, and energy in order to carry out an electrolysis reaction in the electroyser, to produce NaClO₃ and gaseous hydrogen (H₂). The NaClO₃ and H₂ are supplied to vehicles. Each vehicle includes a reactor for decomposing the NaClO₃ and producing reaction products of NaCl and oxygen, with the oxygen being supplied to a fuel cell.

A method and device for removing, deodorizing and purifying odor, smoke and harmful substances from exhaust gas or flue gas employs a water solution containing hypohalogen acid such as hypochlorous acid soda, an alkaline electrolyte such as potassium hydroxide or sodium hydroxide and a saline electrolyte such as sodium chloride, potassium chloride, sodium bromide or potassium bromide which is electrolyzed to produce an electrolytic water solution which is fed to a deodorizing tower and brought into contact with exhaust gas or flue gas to remove odor, smoke and harmful substances in the exhaust gas or flue gas.

An aqueous cleaning and disinfecting composition is disclosed that is a synergistic combination of (a) a sufficient amount of a chlorine-containing bleach compound such as sodium hypochlorite or sodium dichloroisocyanurate to provide from about 1,100 parts per million by weight of available chlorine level with (b) from about 600 to 800 parts per million by weight of bactericidal quaternary ammonium compounds such as mixtures of didecyldimethylammonium chloride and (C12-C16 alkyl)dimethylbenzylammonium chlorides. Such compositions are tuberculocidal at unexpectedly low concentrations. Also disclosed are two component compositions and methods of disinfecting surfaces containing tubercule bacilli and other pathogenic micro-organisms such as bacteria and viruses.

The invention relates to a preparation method for a coal combustion improver. After common coal is added with coal additives for combustion, the effect of energy saving and emission reduction is obvious and effective. The preparation method comprises the following steps that: 1. high-stability sodium chlorate and potassium chloride react with each other to produce potassium chlorate when water is added and the sodium chlorate and the potassium chloride are dissolved; 2. leavening agent sodium acetate is introduced to conduct base exchange with humate in coal, low ignition point humate is produced and the ignition performance of the coal is reduced; and 3. ferric oxide required by the formula is compound insoluble in water. Thereby, ferric chloride and calcium oxide are used to react with each other to produce ferric oxide when water is added and the ferric chloride and the calcium oxide are dissolved. Other products in the market do not at all have the preparation and application characteristics of the three compounds.

The invention discloses a stabilized chlorine dioxide disinfection solution and its preparation method. The disinfection solution is composed of component A and component B, wherein component A is stabilized sodium chlorite solution consisting of chlorite, a stabilizing agent, a complexing agent, a pH stabilizing agent, and the balance a pH conditioning agent and water; component B is an activating agent, which can be at least one of citric acid and hydrochloric acid. The product of the invention has the advantages of stability, long shelf-life, and a validity period up to 2 years, and can be used as a disinfectant. The disinfection solution of the invention has simple process and convenient usage. In the invention, the original mode of pH value adjusting by acid is changed, and zinc chloride and zinc acetate are employed to remove sodium hydroxide in raw materials and reach the purpose of pH value adjusting. Simultaneously, zinc acetate and sodium hydroxide generate no amphoteric substance, and the actual operation is easier.

An ordinary-temp phosphating liquid for the phosphate treatment of surface of iron and steel contains phosphoric acid (2-4 wt.%), zinc oxide (0.4-0.6 wt.%), zinc nitrate (0.5-1.5 wt.%), nickel nitrate (3-5 wt.%), manganese nitrate (2-4 wt.%), sodium borofluorate (0.2-1 wt.%), sodium chlorate (2-3 wt.%), citric acid (0.5-2 wt.%), and softened water (the rest). Its advantages are high stability, long film-forming time, and high film strength and resistance to corrosion.

The invention discloses a method for extracting platinum-palladium out of copper anode mud. The method is characterized in that the platinum-palladium is extracted by employing a secondary gold dust chlorination gold leaching liquid, and the method comprises the following process steps of: firstly, carrying out sulfation roasting on the copper anode mud, carrying out primary chlorination gold leaching, carrying out sulfur dioxide gas reduction so as to obtain a primary reduction liquid, and subsequently carrying out zinc powder replacement so as to enrich gold, silver, platinum and palladium into secondary gold powder; secondly, dissolving the secondary gold powder, removing the impurities, filtering the obtained filtered residue, carrying out secondary chlorination gold leaching, adding ammonium chloride and a reduction inhibitor sodium chlorate into the filtered liquid, and reacting so as to obtain platinum and palladium precipitate; and finally reducing the filtered liquid by using a liquid sulfur dioxide to leach the gold. The method is simple in process equipment arrangement and convenient to operate; the recycling rate of the gold in the copper anode mud is increased; and meanwhile the platinum-palladium is effectively enriched in platinum-palladium concentrate.

The invention relates to a method for recovering germanium from flyash by a wet process, belonging to the technical field of wet-process metallurgy. The method comprises the following steps of: (1) crushing flyash to more than 200 meshes by a wet process; (2) carrying out oxidizing leaching twice on wet flyash by using a sulfuric acid solution, sodium chlorate and ammonium fluoride; (3) crushing the flyash to 200-400 meshes for a second time; (4) leaching 3 or 4 times by using the same condition as that of the first leaching; (5) regulating the pH value of the first leached liquid to 2-2.5 by using ammonia water, and then precipitating and leaching out germanium in the liquid by using tannin with a weight percentage content of 80-99 percent; (6) drying and roasting the germanium precipitate to prepare a germanium concentrate; distilling the germanium concentrate with hydrochloric acid by using a conventional method to obtain germanium tetrachloride; and redistilling, rectifying, purifying and hydrolyzing to obtain high-purity germanium dioxide. The invention is used for flyash after recovering germanium by a fire process, sufficiently utilizes rare germanium metal, reduces the pollution of tailings to the environment, and has the advantages of low cost and high recovery rate.

The invention relates to a method for selectively leaching heterogenite, which is based on the whole wet method and characterized in that the method comprises the following steps: ball-milling and pulping heterogenite minerals until the requirement that the particle size is smaller than 150 meshes is met; putting the heterogenite minerals into concentrated sulfuric acid, concentrated hydrochloric acid or a mixed solution of both the concentrated sulfuric acid and the concentrated hydrochloric acid; adding a reducing agent containing ferrous ions to carry out reduction reaction for 5 to 9 hours under the conditions that the pH value of the solution is 1.0 to 2.0 and the reaction temperature is 60 to 90 DEG C; sampling and detecting, and stopping adding the reducing agent when the content of Cobalt in the residue is lower than 0.5% and the content of the ferrous ions in the solution is lower than 2.0g/L; adding sodium chlorate or hydrogen peroxide as an oxidizing agent, or pumping air into the solution, to oxidize the residue ferrous iron into ferric iron; adding sodium carbonate to the solution to adjust the pH value of the solution to 2.5 to 4.5; reacting for 2 to 3 hours, to precipitate the ferric iron in the form of ferric hydroxide; and leaching the waste residue after the reaction. The invention has the advantages of low production cost and low environmental pollution level.

The invention discloses a comprehensive recycling process for polymetallic material containing gold and silver, belongs to the field of non-ferrous metal comprehensive recovery, and mainly comprises the following steps: ball-milling polymetallic material containing gold and silver, leaching bismuth, copper and tin from the polymetallic material by sulfuric acid leaching agent and ferric chloride, recovering the bismuth, copper and tin; retaining lead, gold and silver in the first leaching residue; and recovering the lead, gold and silver. According to the comprehensive recycling process provided by the invention, bismuth, copper and tin are leached from the polymetallic material by sulfuric acid leaching agent and ferric chloride, the oxidation of the ferric in the ferric chloride, and the chloride solution function of the chloride ion to bismuth and tin are creatively utilized, the addition of sulfuric acid and ferric chloride has the effect of changing silver oxide and silver sulfide into silver chloride, so as to reduce the chlorination step cost, and further reduce the dosage of sodium chlorate and hydrochloric acid, and the leaching rate of gold and silver is greatly improved accordingly. The comprehensive recycling process provided by the invention has the advantages that the technology is simple and practicable, the process is short, the device is simple, and the operation is convenient; and the adopted raw material is common, cheap and pollution free.

The invention provides a method for treating reverse osmosis concentrated water. In the method, the process flows of a laminated filter, heterogeneous catalytic ozone oxidation reaction, an ozone destruction tower and a biochemical reaction tank are adopted. The method comprises the following steps of: adding sodium hypochlorite into the reverse osmosis concentrated water produced in the recycling process of oil refining production wastewater subjected to biochemical treatment and membrane process treatment, sterilizing, filtering by using the laminated filter, fully mixing with ozone, adding into a reactor filled with a zirconium titanate catalyst and performing ozone oxidation; and performing biochemical treatment by using a biochemical reactor with special biological bacteria, wherein the chemical oxygen demand (COD) of effluent after the reverse osmosis concentrated water is treated is below 60mg/L.

Composition of Hypochlorous acid characterized because it has the following chemical composition

• • Hypochlorous acid 6.5-7.3%
  • Hydrochloric acid 27.6-28.5%
  • Sodium chloride 13.6-14.2%
  • Sodium hypochlorite 34.8-35.4%
  • Chlorine in solution 7-6.5%
  • Dissolved oxygen 10.5-8.1%

The composition of hypochlorous acid has medical application in humans and in veterinary practice, both prophylactic and therapeutic. It can also be applied in antisepsis and sterilization of foods and in the treatment of water and water supply systems. In flower growing is can be used for the disinfection of crops and the elimination of fusarium and sigatoka negra.

The invention discloses a method adopting a combined technology of pre-oxidation and coagulating sedimentation to process wastewater containing thallium and ammonia-nitrogen. According to the method, a sodium hypochlorite oxidizing agent is added into a wastewater collecting tank so as to oxidize metal ions in wastewater, the monovalent thallium is fully oxidized into trivalent thallium, monovalent thallium is converted into complex under the effect of strong oxidant, and at the same time, the nitrogen in ammonia-nitrogen is degraded and removed in the form of nitrogen gas. After pre-oxidation, the wastewater is lifted to an integral processing facility through a self-sucking pump; ferrous sulfate and poly aluminum chloride (PAC) are added to form alumen ustum flocculus in a precipitation unit, the precipitate is wrapped, the thallium complex is adsorbed, then quicklime is added to adjust the solution to an alkaline environment; in the alkaline environment, Fe<3+>, Al<3+>, and prepolymer products thereof carry out hydrolysis quickly to form Fe(OH)3 flocculus and Al(OH)3 flocculus; before the flocculus becomes big, the adsorption sites on the surface of flocculus form covalent bonds with Ti<3+>, the flocculus becomes bigger and bigger very quickly and goes on absorbing Ti<3+> in water; at the same time, Ti<3+>, Fe<3+>, Al<3+>, Zn<2+>, lead, and cadmium carry out co-precipitation reactions, and thus the heavy metal ions in water are removed.

This invention relates to extend the benefits of using hypochlorite compounds such as sodium hypochlorite to clean and disinfect articles while reducing or eliminating the side effects of treating an article with a strong oxidant material. The invention relates to a single step process involving mixing of precursor compositions of a suitable hypohalite or hypohalous acid with a solution of a reducing agent. Optionally a buffer may be present in either or both precursor compositions, such that at time of use such active hypohalous acid concentration in the resulting aqueous mixture remains at a sufficient activity level to effect one or more desired benefits against a target substrate for a desired period of time. The oxidant is substantially consumed by reaction with the reducing agent after the time needed for achieving the desired benefit has passed.

The invention discloses a gas phase oxidization-liquid phase oxidization-absorption three-section type dry-wet-process flue gas denitration process. According to the process, ozone is used as a gas-phase oxidant to oxidize one part of nitric oxide in flue gas into high-valence-state nitric oxide capable of being absorbed by slurry; any one or a mixture solution of more of hydrogen peroxide, sodium hypochlorite, sodium chlorite, sodium chlorate, sodium persulfate, potassium chlorate, potassium hypermanganate and potassium dichromate is sprayed to be used as a liquid-phase oxidant to oxidize the residual high-valence-state nitric oxide in the flue gas into the high-valence-state nitric oxide; and the flue gas enters an absorption tower and a magnesium hydroxide solution is sprayed to absorb the high-valence-state nitric oxide. Compared with the prior art, the process firstly adopts two times of oxidization of a gas phase and a liquid phase and a magnesium oxide wet process is used for absorbing so that a target of efficiently removing the nitric oxide is realized; and by virtue of the technical scheme, the use amount of the ozone is reduced, the equipment cost and operation cost are reduced and the denitration efficiency is improved and can reach more than or equal to 93%.

The invention provides a method for recycling valuable metals from lead anode slime, which comprises the following steps: preprocessing anode slime to obtain oxide anode slime, and performing chloration and leaching on 65-78 wt% of oxide anode slime, 15-20 wt% of sodium chloride and 5-20 wt% of sodium chlorate to obtain an acid leaching liquor and acid leaching residue; performing cooling crystallization on the acid leaching liquor and filtering to obtain first filter residue and a first filter liquor; hydrolyzing, insulating and filtering the first filter liquor to obtain second filter residue and a second filter liquor; recycling antimony from the second filter residue; adding iron powder into the second filter liquor and reducing and filtering to obtain a third filter liquor and third filter residue; recycling bismuth, copper and arsenic from the third residue; taking 70-95 wt% of the acid leaching residue and 5-30 wt% of a reducing agent and performing alkaline leaching to obtain alkaline leaching liquor and alkaline leaching residue; recycling tellurium from the alkaline leaching liquor; and performing pyrogenic process smelting on the alkaline leaching residue to recycle gold and silver. The method solves the technical problems that in the prior art, antimony is difficult to leach, and the recovery rate of valuable metals such as copper, bismuth, antimony, tellurium and the like is low.

The invention relates to the technical field of circuit board printing, particularly a low-acidity acidic etching regenerant and an acidic etching mother liquor thereof. The regenerant provided by the invention comprises the following components in percentage by weight: 10-12% of sodium chlorate, 15-17% of sodium chloride, 0.15-1.17% of ammonium chloride, 0.5-0.7% of urea, 1-1.5% of additive and 70-74% of water. The invention can perform the acidic etching under low acid equivalent, thereby ensuring the smoothness of the production, improving the working environment and prolonging the equipment life.

The invention relates to an electrochemical method which produces sodium chloride and alkaline hydrogen peroxide simultaneously. The method can improve the use efficiency of the two poles of the electricity, and lower the production cost. The method adopts an electrolytic tank consisting of an anode, a cation exchange membrane, an anion exchange membrane and a cathode, wherein, the electrodes combine with the membranes in sequence to form an anode chamber, an intermediate chamber and a cathode chamber; sodium chloride solution and sodium chlorate solution are circulated to the anode chamber, sodium hydroxide solution and air is circulated to the cathode chamber and sodium hydroxide solution is circulated to the intermediate chamber; after direct current circulating among the electrodes, chlorine is produced in the anode while the oxygen in the cathode deoxidizes and produces hydrogen peroxide and the concentration of the sodium hydroxide solution in the intermediate chamber is increased; the anolyte flowing out of the anode chamber flows into an external heated reaction tank, and chlorine is transferred into sodium chlorate; the anolyte is circulated back to the anode chamber of the electrolytic tank; a part of the concentrated sodium hydroxide solution which flows out of the intermediate chamber can be used for adjusting the pH value of the anolyte without using extra sodium hydroxide, thereby lowering the running cost.

The invention provides an environmental-friendly coal-saving agent for a cement shaft kiln, comprising the following raw materials by weight portion: 3-7 portions of a coal combusting low-temperature modifying agent, 2-6 portions of a compound sulphur-fixing agent, 0.5-0.96 portion of a combusting inductive agent, 3-7 portions of a raising agent, 56-96 portions of a combusting poising agent, and 5-15 portions of a highly-efficient sulphur-fixing agent. The coal combusting low-temperature modifying agent can be potassium permanganate, potassium chlorate, potassium perchlorate, sodium chlorate, sodium nitrate and the like; the compound sulphur-fixing agent can be sodium carbonate, calcium oxide and the like; the raising agent can be waste liquor of paper mill containing Na or/and Ca sulphonate and the like; and the combusting poising agent can be a chemical waste reducing substance containing sodium chloride and the like. The method solves the problems of environmental pollution and resource waste in the prior art, uses compatibility of multiple chemical raw material of 6-10 percent and chemical waste to prepare the coal-saving agent with small dosage and fast effect to be added to the production of the cement shaft kiln in trace quantity, and has the advantages of resource conservation by using waste, coal conservation and consumption reduction, and reduction of dust and SO2 discharge and environmental pollution.

The invention discloses a method for extracting nickel and molybdenum from nickel-molybdenum ore, comprising the following steps of: (a) in the presence of an oxidizing agent, leaching the finely-ground nickel-molybdenum ore from an acid solution and filtering to obtain a leachate, wherein the oxidizing agent is sodium chlorate or potassium chlorate; (b) adding a first alkaline compound in the leachate, adjusting the pH value of the leachate to be 1.5-3.5 and filtering to respectively obtain a precipitation and a supernate; (c) adding a second alkaline compound in the supernate, adjusting thepH value of the supernate to be 5-7 and filtering to obtain a nickel-containing compound; and (d) leaching the precipitation in an alkali liquor, filtering to obtain a molybdenum-containing leachate,and extracting and re-extracting the molybdenum-containing leachate to obtain a molybdenum-containing compound. By using the method, the sodium chlorate or potassium chlorate is used as the oxidizingagent, the higher leaching rate of the nickel and molybdenum and the higher recovery rate of the nickel and molybdenum can be obtained.