520 results about "Ammonium bisulfate" patented technology

The invention discloses an efficient and clean beneficiation method of complex sulfide ore. The method includes the following steps: utilizing an activator selected from one of or some of oxalic acid, ammonium carbonate, ammonium bicarbonate, ammonium sulfate, ammonium bisulfate and ferrous sulfate as a combination; utilizing collectors including xanthate collectors, black collectors, white collectors and thionocarbamate collectors; mixing the activator, the collectors and BC; stirring; and performing flotation separation of the sulfide ore to obtain the sulfur concentrate. The inventive beneficiation method has the advantages of high discrimination property, cleanness and non-toxicity; and is suitable for the flotation separation of the complex sulfide ore, particularly the flotation separation of complex sulfide ore containing pyrrhotites and pyrites with fine dissemination size.

The invention relates to a grafted copolymerized cationic polysaccharide bioflocculant and a preparing method thereof. A product with the cationic degree (DC) of 3-63% is finally prepared through an aqueous solution polymerization technology with a present nonionic polysaccharide bioflocculant (Dx) as a raw material, one or more of dimethyl diallyl ammonium chloride (DMDAAC), methacryloxyethyltrimethyl ammonium chloride (DMC), acryloyloxyethyltrimethyl ammonium chloride (DAC), dimethylaminoethyl methacrylate (DMAEMA), dimethylaminoethyl acrylate (DMAEA) as a monomer, and one or two of ammonium persulfate/sodium bisulfate and dibenzoyl peroxide (BPO) (AIBA) as an initiator. The preparation method is simple, and is easy to control, and the product obtained in the invention has good flocculation effect and high treatment efficiency, and can be widely used in the field of treatment various sewages, the sludge dewatering field and the like.

The invention relates to a method for preparing aluminum oxide and other products by aluminum-containing materials of bauxite, alunite, nepheline, fly ash, kaolin, coal gangue and clay. The method comprises the following steps: (1) crushing and grinding an aluminum-containing material, carrying out mixing and baking for the treated aluminum-containing material and ammonium bisulfate; (2) carryingout dissolution and filtering for the baked clinker to obtain a crude ammonium aluminum sulfate solution and aluminum extracting residue; (3) carrying out an iron precipitating treatment for the ammonium aluminum sulfate solution with the concentration more than 1 g/L by adopting a jarosite method, then carrying out an iron precipitating treatment by a goethite method, carrying out an aluminum precipitating treatment for the resulting solution, carrying out calcination for the resulting aluminium hydroxide to prepare aluminum oxide; (4) carrying out an iron precipitating treatment for the ammonium aluminum sulfate solution with the concentration less than 1 g/L by adopting the goethite method, and carrying out an aluminum precipitating treatment to prepare aluminum oxide, or adopting a recrystallization method to carry out purification, adopting a reaction of the ammonium aluminum sulfate crystal and a ammonium carbonate solution to precipitate the aluminum to obtain ammonium aluminumcarbonate, carrying out calcination for the ammonium aluminum carbonate, and adopting a Bayer method to treat the calcined ammonium aluminum carbonate to prepare sandy aluminum oxide; (5) washing anddrying the aluminum extracting residue, wherein the dried aluminum extracting residue is adopted as the silicon dioxide product.

The invention provides a simple, efficient and environment-friendly method for recovering valuable metals from a positive electrode material of a waste lithium ion battery; the method comprises the following steps of performing discharging of a salt solution; performing disassembling to separate a positive plate; performing smashing on the positive plate to separate a positive electrode material and an aluminum foil; performing mixed low-temperature roasting on the positive electrode material and a roasting agent ammonium sulfate and/or ammonium bisulfate; performing leaching on the roasted material and separating to obtain carbon and a lixivium; adding a precipitant into the lixivium, and regulating the pH value by using NH<3>-containing flue gas, performing deposition on other metals except Li, and carrying out solid-liquid separation; regulating the pH value of a filtrate by using the NH3-containing flue gas, adding ammonium carbonate or ammonium bicarbonate or pumping CO<2> gas, and carrying out lithium precipitation to obtain a lithium carbonate product. The preparation process is simple, the process conditions are mild, the time required by the process is short, a large amount of acid and alkali do not need to be consumed, and the cost is low; and in addition, recovery of the valuable metals and carbon from the positive electrode material can be effectively realized, themethod is green and environment-friendly, and a large amount of solid waste and wastewater cannot be generated.

The method of comprehensively utilizing phosphate fertilizer by-product includes utilizing ammonium fluoride solution of 3-14% concentration to absorb side product fluorine containing tail gas ammonium fluorosilicate solution; adding iron scrap or iron salt to fluorosilicic acid as one other by-product to eliminate phosphorus; adding liquid ammonia, ammonia water or ammonium bicarbonate; filtering, washing, and eliminating silica precipitate; returning ammonium fluoride solution to phosphate fertilizer absorbing system, concentration and drying to obtain ammonium hydrogen fluoride; reacting solid ammonium hydrogen fluoride and sulfuric acid at high temperature to obtain HF gas, absorbing HF gas to obtain hydrofluoric acid, purification and condensation to obtain anhydrous HF; and mixing the mixture of ammonium sulfate and ammonium bisulfate with ammonium bicarbonate or ammonia in a mixer, curing and crushing to ammonium sulfate fertilizer.

A method for sequestering carbon dioxide (CO₂) that includes generating ammonia from an ammonium salt to make a basic ammoniated aqueous solution and using the solution to remove at least a portion of CO₂ from a CO₂-bearing gas and precipitate the removed CO₂ as bicarbonate. The aqueous solution is recycled. Various valuable byproducts, including sodium bicarbonate, sodium carbonate, ammonium bicarbonate, and hydrochloric acid, are produced. Ammonia is generated by reacting an ammonium salt with either acidic or basic materials. Non-limiting examples of suitable ammonium salt include ammonium chloride, ammonium sulfate, ammonium bisulfate, and ammonia nitrate, those of the acidic material include ammonium bisulfate and sulfuric acid, and those of the basic material include calcium oxide, limestone, dolomite, cement kiln dust, calcium-rich fly ash, steel and iron slag, and silicate rocks or mining wastes that are rich in serpentine, olivine or wollastonite.

A quaternary ammonium salt ionic liquid of the present invention and its preparation and application methods belong to quaternary ammonium compounds, and its molecular composition is N, N, N-trimethyl-N-sulfobutyl-ammonium bisulfate, and its molecular formula is [HSO3-b -N(CH3)3]HSO4, the structural formula is as follows: the quaternary ammonium salt ionic liquid of the present invention is non-corrosive equipment and environment-friendly, and the quaternary ammonium salt ionic liquid catalyst of the present invention is used for nitrobenzene catalytic hydrogenation to synthesize p-amino The phenol reaction is a liquid phase method, the reaction temperature is 60-130° C., and the PAP yield reaches 19.5-88%.

The invention discloses a method for determining N-methylamino ammate in production of acesulfame. The method mainly comprises the steps of: (1) selecting an analytical chromatographic condition, an ODS column (4.6mm*25cm) or other equivalent chromatographic columns, wherein the wavelength is 250nm, the flow velocity is 1ml/min, the column temperature is 25 DEG C, and the sample amount is 20mu l; (2) preparing tetrabutylammonium hydrogen sulfate solution from deionized water until the molar concentration is 1.0-2.0mmol/L, and preparing a mobile phase from the prepared tetrabutylammonium hydrogen sulfate solution and chromatographic grade methanol according to the volume ratio of 60 to 40; (3) diluting the sample to be tested by an organic solvent according to the volume ratio until the concentration is 0.5-2.0%, so as to prepare a test solution; (4) absorbing the test solution by a microinjector, injecting into an efficient liquid chromatograph, and analyzing by an area external standard method; and (5) recording the content of the N-methylamino ammate in the sample to be tested. By adopting the method disclosed by the invention, the content of the N-methylamino ammate can be accurately and rapidly determined.

The invention discloses a method for online elimination of ammonium bisulfate clogging of air pre-heaters of a coal-fired boiler of a thermal power plant. A unit load regulation low-load period is used, according to a reversibility principle of an ammonium bisulfate deposition process, an operation regulation method is put forward, so that one air pre-heater on one single side is isolated from air, a small quantity of high-temperature flue gas is fed, the overall part temperature of each air pre-heater is gradually increased, liquid ammonium bisulfate attached to heat-transfer elements is gasified, and clogging is eliminated. At present, load regulation is frequently performed on coal-fired units in China, and long low-load operation periods exist at night frequently, so that the units can use the load regulation low-load period frequently to perform alternating ammonium bisulfate clogging elimination on air pre-heaters, resistance of the air pre-heaters is reduced, high-pressure water washing after shutdown is avoided, and economic losses are reduced.

A polishing composition for a memory hard disk, which comprises the following components (a) to (d):(a) from 0.1 to 50 wt %, based on the total amount of the polishing composition, of at least one abrasive selected from the group consisting of silicon dioxide, aluminum oxide, cerium oxide, zirconium oxide, titanium oxide, silicon nitride and manganese dioxide,(b) from 0.001 to 10 wt %, based on the total amount of the polishing composition, of at least one iron salt selected from the group consisting of iron nitrate, iron sulfate, ammonium iron sulfate, iron perchlorate, iron chloride, iron citrate, ammonium iron titrate, iron oxalate, ammonium iron oxalate and an iron chelate complex salt of ethylenediaminetetraacetic acid,(c) from 0.01 to 30 wt %, based on the total amount of the polishing composition, of at least one peroxydisulfate salt selected from the group consisting of ammonium peroxydisulfate, potassium peroxydisulfate and sodium peroxydisulfate, and(d) water.

The invention belongs to the technical field of controlling atmospheric pollutants exhausted by coal-fired boilers, and particularly relates to an SNCR-SCR combined denitration system and method based on ammonia nitrogen molar ratio detection and regulation. The system comprises an ammonia-containing storage tank, an air preheater, an SNCR reaction zone, an SCR reaction zone, a first detection system, a second detection system, a third detection system and a control system, wherein the SNCR reaction zone is arranged in a boiler furnace, the SCR reaction zone is arranged in a boiler flue, and the first detection system, the second detection system and the third detection system are connected with the control system. The combined denitration system can achieve full-load denitration operation, is high in denitration efficiency and solves the problem of corrosion and deposition of ammonium bisulfate in follow-up equipment.

At present, a regenerative Junker-type air preheater is used for heating boiler-supplied air in most of large coal-fired power generating sets in China, and ammonium bisulfate results in scaling and corrosion on the surface of heat transfer elements at the medium/low temperature end of the air preheater, thereby threatening the safe and stable operation of the air preheater directly. The invention relates to a method for the optimized regulation of an SCR (Selective Catalyst Reduction) flue gas denitration system in a coal-fired power plant, which comprises the following steps of: (1) jetting ammonia into a denitration reactor; (2) measuring the concentrations, the speeds and the temperature distribution of NO and O2 at an inlet of the denitration reactor; (3) measuring the concentration distribution of NO and O2 at an outlet of the denitration reactor; (4) calculating the unevenness Cv of the concentration distribution of NO at the outlet of the denitration reactor; and (5) comparing the obtained Cv with C%. The method effectively reduces ammonia escape, prevents ammonium bisulfate from scaling and corrosion on the surface of the heat transfer elements of the air preheater, and ensures the safe and stable operation of the air preheater.

A method for comprehensive utilization of laterite nickel ore comprises the following steps: (1) pulverizing laterite nickel ore, grinding, mixing with ammonium bisulfate, and roasting; (2) dissolving and filtering the roasted clinker to obtain a filtrate, depositing iron by an ihleite method, and depositing iron by a goethite method; (3) performing nickel deposition of the filtrate obtained after iron deposition by sodium sulfide, preparing a nickel sulfide product; (4) performing magnesium deposition of the filtrate obtained after nickel deposition by sodium hydroxide to obtain magnesium hydroxide; (5) washing, drying and calcining magnesium hydroxide to prepare a magnesium oxide product; (6) using the roasted clinker dissolved slag as a microsilica fume product directly, wherein the main component of the slag is silica; (7) calcining ammonium jarosite to obtain an iron oxide product.

The invention relates to an anti-sulfur film type low-temperature denitration catalyst and a preparation method thereof. The catalyst uses honeycomb ceramic as a carrier, (Mn-Ce-Ox) composite oxides as active ingredients and (Ni-Co-Cu-Sb-Nb-Ox) composite oxides as catalytic assistants, and a surface layer is covered by an anti-corrosion, wearproof, hydrophobic and breathable anti-sulfur functional film. The anti-sulfur functional film can effectively prevent matters such as ammonium bisulfate from contacting the active site of the catalyst, slow down deposition of poisons on the surface of the catalyst, prevent impact of dust in flue gas on the catalyst, effectively solve the problem that the low-temperature SCR catalyst easily causes poisoning, and prolong the service life of the low-temperature catalyst. The denitration rate of the catalyst achieves more than 90 percent at the temperature 140-200 DEG C. The anti-sulfur film type low-temperature denitration catalyst and the preparation method thereof have great significance in industrialized application of the low-temperature SCR denitration catalyst and promotion of an SCR denitration technology in China.

The invention relates to a method for recycling the waste sulfuric acid of the second separation during the production process of the industrial sulfanilamide. The invention method is the novel process of first recycling the organic matter and second treating the waste sulfuric acid, and hydrochloric acid and ammonium hydrogen sulfate or ammonium sulfate with wide application by the treatment of the waste sulfuric acid. The invention not only reduces the environmental pollution and but also decreases the production cost of the industrial sulfanilamide, and has the good environmental protection benefit, the social benefit and the enormous economic benefit.

The invention belongs to a method for producing plant fertilizers, more particularly to a method for producing a solid-state Ca/Mg/Ti/Fe/S/N/Si compound fertilizer from water-quenched blast furnace slag. The invention is characterized in that: the raw materials include titanium oxide-containing water-quenched blast furnace slag, ammonium sulfate, ammonium hydrogen sulfate, ammonium pyrosulfate and ammonium persulfate; the method comprises the following steps: ball-milling Ti-containing water-quenched blast furnace slag to obtain powder of particle size of 60-160 micrometers, mixing the furnace slag powder with 3-20 times of one substance selected from ammonium sulfate, ammonium hydrogen sulfate, ammonium pyrosulfate, ammonium persulfate, or a mixture thereof, heating the resulting mixture up to 200-500 DEG C and maintaining the temperature for 10-65 min, and crushing clinkers to small pieces of 4-12 mm diameter. The invention utilizes Ti-containing water-quenched blast furnace slag and other raw materials to produce plant fertilizers, and thereby realizes environmental protection, Ti resource utilization and nutrient supplementation to plants.

The invention relates to an SCR (selective catalytic reduction) denitration catalyst, in particular to an SCR (selective catalytic reduction) denitration catalyst for accelerating ammonium hydrogen sulfate decomposition by low-temperature flue gas, a preparation method and an application. The SCR denitration catalyst takes composite oxides formed by titanic oxides and transition metal oxides as carriers, vanadium oxides as active components and tungsten oxides as co-catalysts, the molar ratio of transition metal elements to titanium elements in the catalyst is (0.1-0.5):1, and the transition metal oxides include one or more of MnO2, Fe2O3, CeO2, ZrO2, Al2O3, SnO2, Nb2O5 and Sb2O5. An appropriate quantity of transition metal oxides are added into the catalyst, the SCR denitration catalyst for accelerating low-temperature decomposition of ammonium hydrogen sulfate is prepared, and the catalyst accelerates the ammonium hydrogen sulfate to decompose at the temperature lower than 350 DEG C.

The invention relates to a method for extracting aluminium oxide from pulverized fuel ash. The method comprises the following steps of: finely grinding the pulverized fuel ash, and then carrying out deferrization treatment; carrying out pyrolysis on ammonium sulphate to prepare ammonium bisulfate and ammonia gas; dissolving out a solid generated after sintering, and then obtaining a solution containing ammonium aluminum sulfate; crystallizing the solution containing the ammonium aluminum sulfate to obtain solid ammonium aluminum sulfate; dissolving the solid ammonium aluminum sulfate and thenpreparing the dissolved solid ammonium aluminum sulfate into a solution reacting with the ammonia gas or ammonia water to generate trihydrate alumina or ammonium sulfate; and roasting the trihydrate alumina to obtain the aluminium oxide. By using the method for extracting aluminium oxide from pulverized fuel ash in the invention, ammonium bisulfate is prepared and the ammonia gas is coproduced, thus, the reaction between the ammonium sulfate and the pulverized fuel ash is convenient to control; and the method is simple, few in side products and easy to realize industrial application.

The invention relates to a catalyst used for synthesis of p-aminophenol by catalytic hydrogenation of nitrobenzene, a preparation method and an application method, belonging to catalyst containing both platinum and organic compound field. The catalyst is a supported and bi-functional catalyst, and comprises room temperature ionic liquid of N, N, N-trimethyl-N-sulfobutyl-ammonium bisulfate which is one component of the active components, active metal Pt which is the other component of the active components, and silica gel carrier; wherein, the loading of the room temperature ionic liquid of N, N, N-trimethyl-N-sulfobutyl-ammonium bisulfate is 5 to 50%, while the loading of the active metal Pt is 0.01 to 1.5%. The invention has the advantages that: as a highly active heterogeneous catalyst, the catalyst overcomes the shortcomings that the homogeneous catalyst in prior art can not be used repeatedly, the reaction conditions of the heterogeneous catalyst in prior art are severe and the activity is low, and the problems that the equipment is liable to corrosion and the discharge of wastewater pollutes environment are solved.

A chemical mechanical polishing aqueous dispersion according to the invention includes (A) 0.1 to 4 mass % of colloidal silica having an average particle diameter of 10 to 100 nm, and (B) 0.1 to 3 mass % of at least one ammonium salt selected from ammonium phosphate, diammonium phosphate, and ammonium hydrogen sulfate, the chemical mechanical polishing aqueous dispersion having a mass ratio (A)/(B) of the component (A) to the component (B) of 1 to 3 and a pH of 4 to 5 and being able to simultaneously polish at least two films that form a polishing target surface and are selected from a polysilicon film, a silicon nitride film, and a silicon oxide film.

The invention discloses a formaldehyde scavenging agent. The formaldehyde scavenging agent is prepared from, by weight percent, 5%-15% of a high-molecular polymer, 1%-5% of silicon dioxide, 1%-10% of ammonium chloride, 4%-12% of ammonium bisulfate, 1%-7% of urea, 3%-8% of a cyanamide compound, 1%-5% of 1-hydroxyethylidene-1,1-diphosphonic acid, 3%-6% of plant extract and the balance water. The formaldehyde scavenging agent can scavenge formaldehyde thoroughly and protect human health and is low in cost.

A process for preparing the aluminium oxide nanoparticles from the industrial waste (used Al catalyst or rejected A-alloy) includes grinding, reacting on fused ammonium hydrogen sulfate or its solution, filtering, thermal concentrating, recrystallzing to obtain ammonium aluminium sulfate crystals, preparing its solution, dripping it in the solution of ammonium dicarbonate containing polyethanediol to generate alkaline ammonium aluminium carbonate, drying, and burning.

The invention provides an air pre-heater. A temperature increase sector plate is arranged at the position, close to a secondary air side, on a smoke side. The included angle alpha between the temperature increase sector plate and a sector plate closest to the temperature increase sector plate ranges from 7 degrees to 8 degrees. The center angle beta of each separation bin is equal to the included angle alpha. The center angle gamma of the temperature increase sector plate ranges from 9 degrees to 10 degrees. The separation bin between the temperature increase sector plate and the sector plate closest to the temperature increase sector plate is a circulation smoke separation bin. One side of a smoke inlet above the smoke side is communicated with a bypass flue. The bypass flue is sequentially connected with a dust remover, a temperature increase smoke induced draft fan and a temperature increase smoke inlet again, and the temperature increase smoke inlet is communicated with the circulation smoke separation bin. Compared with the prior art, high-temperature smoke is guided to the cold end of the air pre-heater, and when the temperature of the cold end is above 147 DEG C, ammonium bisulfate is scaled and gasified again, and the clogging prevention effect is achieved. Through the action of the temperature increase smoke induced draft fan, positive-pressure smoke flow is formed between the smoke side and an air side, pressure of the positive-pressure smoke flow and pressure of positive-pressure air flow of secondary air restrain mutually, and the air leakage problem is effectively solved.

The invention provides a preparation method of 4-chlorophenylhydrazine hydrochloride. The preparation method of the 4-chlorophenylhydrazine hydrochloride includes a diazotization reaction, a reduction reaction and an acidizing reaction. The diazotization reaction includes throwing 4-chlorophenylhydrazine to water; dropping hydrochloric acid to enable the 4-chlorophenylhydrazine hydrochloride to dissolve completely; and dropwise adding a sodium nitrite aqueous solution to obtain a chlorination diazonium parachloroaniline aqueous solution. The reduction reaction includes dropwise adding the chlorination diazonium parachloroaniline aqueous solution to an ammonium sulfite aqueous solution and obtaining diazonium parachloroaniline disulfonate. The acidizing reaction includes dropping the hydrochloric acid to the diazonium parachloroaniline disulfonate; filtering; washing; discharging; stoving; and obtaining a 4-chlorophenylhydrazine hydrochloride end product. The preparation method of the 4-chlorophenylhydrazine hydrochloride is easy to operate by using the sodium nitrite aqueous solution as a reducing agent; and the product seeds out late and side reactions are reduced due to the fact that ammonium chloride and ammonium bisulfate generated in the acidizing reaction have high solubility in the water; and furthermore product quality and product yields are improved effectively due to the fact that the product is incompact in crystallization, good in flow-ability and easy to discharge and wash.