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81 results about "Sulfur Acids" patented technology

Inorganic or organic acids that contain sulfur as an integral part of the molecule.

Method for producing iron pellet with sulfur acid residue containing large contents of impurities and enriching valuable metal

The invention discloses a method for producing iron pellets with sulfur acid residue containing large contents of impurities and enriching valuable metal. The method comprises the following steps: reducing and calcining under a moderate temperature, preparing the iron pellets, chlorinating and calcining under a high temperature, reducing the temperature of the iron pellets while recycling heat energy, collecting dust in flue gas and purifying the flue gas, adding a reducing agent of which the weight is 6 to 9 percent that of the sulfur acid residue on the condition that the kiln head temperature ranges from 750 to 900 DEG C, the kiln tail temperature ranges from 350 to 500 DEG C, and the reducing and calcining step lasts for 70 to 100 min; calcining sand in a high temperature on the condition that 3 to 5 percent of ferrous chloride, 2 to 3 percent of adhesive, and 2 to 3 percent of lignite and/or coke powder are added; pelletizing; carrying out the high-temperature chlorinating and calcining step after dry pre-heating; and recycling heat energy, collecting dust, and purifying the flue gas to achieve the emission standard. According to the invention, two sections of a rotary kiln are adopted for fulfilling the reducing and calcining step and the high-temperature chlorinating and calcining step respectively, wherein a large quantity of arsenic is extracted, part of zinc is reduced and volatilized, the chlorination calcining ensures the reduction and the volatilization of residual arsenic, zinc, tin, lead and copper are chlorinated and volatilized, and sulphur is oxidized into sulfur dioxide and enters the flue gas, so as to obtain qualified the iron pellets. The method has the advantages that the iron recovery rate is 92 to 95; the arsenic extraction rate is larger than 95 percent; the desulfuration rate is equal to or larger than 90 percent; the volatilization rates of the lead, tin and zinc are 60 to 70 percent; and the volatilization rate of copper is about 30 percent.
Owner:个旧市富祥工贸有限责任公司

Technique for using dry discharging carbide slag to completely substitute natural calcareous raw material for producing cement chamotte

ActiveCN101265041ASolve the problem of environmental pollution that is difficult to deal withSolve pollutionCement productionCycloneSlag
The invention discloses a method for producing cement clinkers from dried carbide slag completely instead of natural limy materials, which relates to the field of building materials. Firstly, three auxiliary materials (including sand rock, coal ash and sulfur acid residue) are compounded, pulverized and sieved, and the fine powder is fed into a dryer. Then, the carbide slag with a water content less than or equal to 12% is fed into the dryer, and undergoes intensive heat exchange with the hot flue gas at the charge side, realizing complete drying and mixture. The crude material powder is fed into first-stage, second-stage and third-stage cyclone cylinders to undergo multiple suspension heat exchange with the hot flue gas, and then enter a rotary kiln for calcination. The hot flue gas inside the klin undergoes the heat exchange in a pipeline calciner and a wind pipe and then reversely flows into the third-stage, second-stage and first-stage third-stage cyclone cylinders, the dryer, a cyclone dust collector, a system fan and an airbox pulse bag-shaped dust collector sequentially, and the purified gas is discharged into the external atmosphere. The coal powder jets into the calciner at the charge side for further combustion, and the crude material powder undergoes decomposition reactions: Ca(OH)2-H2O+CaO. The clinker burned in the rotary kiln is cooled by a grate cooler and then delivered to a clinker storage room. In the invention, the waste carbide slag is completely dried by using the exhaust gas at the discharge side, and the heat consumption for clinker combustion is reduced by about 25%, thereby realizing energy conservation and exhaust reduction.
Owner:新疆凯盛建材设计研究院(有限公司)

Photocatalytic oxidation flue gas desulfurization and denitration system of coal-fired power plant

The invention relates to a photocatalytic oxidation flue gas desulfurization and denitration system of a coal-fired power plant, which belongs to the cross field of energy source engineering and environmental engineering, and is applied to simultaneous flue gas desulfurization and denitration of the coal-fired power plant. The process route of the system comprises the following steps of: preparing oxygen with more than 90% of purity by using an oxygenator, and introducing the prepared oxygen into a photo-catalyzing reaction tower for fully reacting to produce an oxidizing material as a main component; simultaneously introducing the oxidizing material and flue gas (after dust extraction) into an oxidizing reaction tower, oxidizing SO2 in the flue gas by the oxidizing material into a final product SO3, and oxidizing NO and NO2 by the oxidizing material into a final product NO3; absorbing SO3 and NO3 in the flue gas after oxidizing reaction when passing through an absorption tower; and completing the simultaneous flue gas desulfurization and denitration process. During desorbing, the obtained by-product, namely nitrate-sulfur acid is collected by a storage tank and is an industrial chemical with wide uses. The system simultaneously realizes desulfurization and denitration in one set of device (complete equipment) and has high removal efficiency and no secondary pollution.
Owner:武汉慧邦环境工程技术有限公司

Low-sulfur discharging and sulfur recycling process of intermediate concentration acid gas

The invention provides a low-sulfur discharging and sulfur recycling process of intermediate concentration acid gas. A purpose of desulphurizing low-concentration acid gas with H2S content of 5 to 20 percent can be achieved by treating the low-sulfur acid gas by virtue of a direct oxidation reactor, a selective oxidation reactor and two adsorption desulphurization towers which can be connected in series and parallel; the direct oxidation reactor is filled with a TiO2 sulfur recycling catalyst, the selective oxidation reactor is filled with a H2S selective oxidation catalyst, catalysts in the direct oxidation reactor and selective oxidation reactor are packed in multiple layers, an air inlet and a cooling coil pipe are respectively arranged between two layers, and the adsorption desulphurization tower is filled with a thermally-renewable catalytic oxidation adsorption desulphurization agent; by selecting the appropriate catalyst and desulphurization agent and precisely controlling the process condition of each step, the total sulfur contained in the process discharged gas is that SO2 content is less than or equal to 10mg / m<3>. By virtue of thermal regeneration, the service life of the catalytic oxidation adsorption desulphurization agent is greatly prolonged, and the desulphurization amount of the catalytic oxidation adsorption desulphurization agent is greatly increased. The process has the advantages of low sulfur emission, high sulfur recycling rate (approximate to 100 percent), long service life and large desulphurization amount of the desulphurization agent, fewer replacement times, less expense, good desulphurization agent removal and scrapping condition, safety and the like.
Owner:山东迅达化工集团有限公司

Rejection processing technology for gas production wastewater in sulfur acid containing gas field

The invention discloses a rejection processing technology for gas production wastewater in sulfur acid containing gas field. The rejection processing technology for gas production wastewater in sulfur acid containing gas field comprises the following steps: enabling the sulfur acid containing gas field gas production wastewater to be successively subjected to suspension and oil removal processing, aeration sulfur removal, chemical oxidation sulfur removal, coagulation and flocculation processing, settlement, sterilization, double-medium filter filtering, fiber bundle filter filtering, ultrafiltration, and corrosion and scale inhibition. The invention also provides a corrosion and scale inhibition agent which comprises hydroxyethylidene diphosphonic acid, sodium sulfonate and benzotriazole. The gas production wastewater rejection processing technology is simple in flow, relatively low in operation cost and simple in management, and is capable of effectively processing sulfur acid containing gas field gas production wastewater, and discharged water reaches A3 standard in Recommended Index for the Injection Water Quality for Clastic Reservoir in People's Republic of China petroleum and Natural Gas Industry Standards SY/T5329/94.
Owner:SHANGHAI EMPEROR OF CLEANING HI TECH

Method for recycling copper from acid waste etching solution

The invention discloses a method for recycling copper from an acid waste etching solution. The method is characterized by comprising the following steps that firstly, an organic phase and the acid waste etching solution are subjected to 1-5 levels of extraction according to the volume ratio of 1-30:1, and copper is extracted; secondly, the load organic phase obtained in the first step and purified water are subjected to 1-5 levels of washing according to the volume ratio of 0.1-10:1; thirdly, the load organic phase washed in the second step and a copper sulphate solution including sulfur acid of 130-250 g/L and copper ions of 1-50 g/L are subjected to 1-3 levels of back extraction according to the volume ratio of 1-10:1, the organic phase obtained through back extraction is returned to the first step to be repeatedly used, and a water phase is a copper sulphate solution; fourthly, metal stainless steel 304 or stainless steel 316 or metal titanium is used as a cathode, the copper sulphate solution obtained in the third step is electroplated under the current density of 50-400 A/m<2>, electroplated copper is obtained, and the copper sulphate solution obtained after the copper is electroplated is returned to the third step to be repeatedly used. According to the method for recycling copper from the acid waste etching solution, the copper can be separated selectively from the acid waste etching solution, the technology is simple, and the separation effect is good.
Owner:陈飙

Highly-ordered single-piece copper-based porous material and preparation method thereof

The invention provides a highly-ordered single-piece copper-based porous material and a preparation method thereof and relates to a single-piece copper-based porous material. The preparation method comprises the following steps: preparing the raw materials of the single-piece copper-based porous material according to the atom ratios of Cu50Fe[50-x]Cox, Cu50Fe[50-x]Nix and Cu50Fe[50-x]Mnx, wherein x is 1-20at.%; smelting prepared alloys, starting a magnetic stirring button, and cooling after uniformly smelting; cutting a smelted Cu-Fe-X system alloy into slices by adopting a line cutting machine, carrying out thermal treatment after polishing, and quenching, wherein X is Co, Ni or Mn; pretreating a sample subjected to thermal treatment in a hydrochloric acid solution and then placing in an electrochemical workstation for electrochemical corrosion, wherein the alloy is connected with a positive electrode of a power supply, pure copper is connected with a negative electrode, and a sulfur acid solution is used as an electrolyte and placed in an electrochemical device; and cleaning the alloy subjected to electrochemical corrosion, and blow-drying so as to obtain a product. The single-piece copper-based porous material has the advantages of high order degree and controllable pore diameter size and distribution.
Owner:XIAMEN UNIV

Cement clinker produced by using various industrial waste residues

The invention relates to cement clinker produced by using various industrial waste residues, which is characterized in that: metal magnesium reducing slag, lime mud or calcium carbide mud or dicyandiamide slag, mountain flour, fly ash or coal gangue and sulfur acid residue are compounded and optimally mixed to produce a raw material; and the raw material is calcined by a calcining process to produce the cement clinker. The cement clinker is characterized in that: various industrial waste residues are comprehensively used to produce the cement clinker, a large amount of waste residues are used, a large amount of natural resources and energy is saved, and standard coal consumption is saved by more than 20 percent in the calcining process of the waste residues which are compounded and optimally mixed, the emission of CO2 and other harmful gases in a large amount is reduced at the same time, the calcining speed of the clinker is increased, and the energy-saving, emission-reducing, consumption-reducing and environmental-protection effects are obvious; and experiments prove that single-machine output and production efficiency are improved and that after 28 days, the pressure strength of the clinker is improved by more than 5MPa compared with that of the clinker produced by the traditional method.
Owner:宁夏建筑材料研究院(有限公司)

Process for preparing strong acid and strong alkali by separating cobalt smelting wastewater

The invention discloses a process for preparing strong acid and strong alkali by separating cobalt smelting wastewater. The process is characterized by comprising the following steps: S1, filtration by microfiltration: using a microfiltration system to treat cobalt smelting wastewater to remove a lot of suspended soils and particles and controlling the SS value being less than 1 to obtain microfiltration contributing water; S2, nanofiltration separation: feeding the treated microfiltration contributing water to a nanofiltration system to separate two types of salt to obtain nanofiltration concentrated water and nanofiltration contributing water, wherein the nanofiltration concentrated water is sodium sulfate and the nanofiltration contributing water is sodium chloride; S3, nanofiltration concentrated water treatment: feeding the nanofiltration concentrated water into a bipolar membrane system to be treated to prepare sodium hydroxide and sulfur acid; and S4, nanofiltration contributing water treatment: feeding the nanofiltration contributing water into the bipolar membrane system to be treated to obtain sodium hydroxide and hydrochloric acid. The process for preparing strong acid and strong alkali by separating cobalt smelting wastewater disclosed by the invention abandons high cost caused by evaporation, so that salt in the wastewater can be recycled in the process, and zero discharge of wastewater is achieved.
Owner:XIAMEN STARMEM TECH

Copper-covered circuit board etching technology

The invention relates to a copper-covered circuit board etching technology which is low in cost and high in etching precision. The copper-covered circuit board etching technology comprises the steps that a copper-covered board after development of a front working procedure is washed through RO water to neutral, polishing is carried out on the copper-covered plate after water washing by using a needle brushing type scrubbing machine, and micro-etching liquid is evenly sprayed on the surface of the copper-covered plate, wherein the micro-etching liquid is a water solution containing sulfur acid and hydrogen peroxide; the copper-covered plate after the micro-etching is washed into the neutral through the RO water again; the copper-covered plate after the washing is immerged into etching liquid for 1-2min, and then the copper-covered plate is washed to neutral by using the RO water again. Compared with the prior art, micro copper wire bridging connection problems cannot emerge on etched circuit boards, production cost is low, special etching liquid does not need to be prepared, micro etching process is carried out on the copper-covered plate by adopting the mode of combining physic micro etching of a pin type plate brushing machine and chemical micro etching, the precision of etching process is improved greatly, and etched micro copper wires with the wire width less than 0.2mm are neat in edge.
Owner:CHONGQING HANGLING PCB

Method for recovering acid making waste heat

The invention discloses a method for recovering acid making waste heat of sulfur acid making or smelting acid making. The method comprises the following steps of: recovering partial heat carried by SO3 gas discharged from a first-section outlet, a second-section outlet and a third-section outlet of a converter in the production process of making acid; recovering heat generated by high temperature of a dry absorption system; and transferring partial heat carried by acid of a dry absorption heat recovering system to boiler water feed by using a heat exchanger on a boil water feed channel of an outlet of a reacting furnace. The scheme uses heat absorbed by dry absorption high temperature to preheat the boiler water feed of an outlet of a sulfur burner and converts the partial heat into medium pressure overheat steam. Therefore, the method can save investment, reduces requirements for soft water quality, and improves generating efficiency above all. The method appropriately modifies a heat recovering system of a converting system at the same time. The method saves a coal economizer, increases a superheater and is additionally provided with an air preheater. For smelting fume acid making, the method can provide a high temperature absorption system on the dry absorption part, and the generated heat can preheat the boiler water feed in the smelting part.
Owner:陈祥明

Application method of fine desulfurization in sulfuric acid exhaust absorption

The invention discloses an application method of fine desulfurization in sulfuric acid exhaust absorption, and relates to a technical scheme of the application of fine desulfurization in sulfuric acid exhaust absorption, in particular to a method for discharging SO2 exhaust. The method comprises the following steps of: A, introducing sulfur-containing exhaust into an absorption tower; and B, spraying ammonium sulfite-ammonium hydrogen sulfite solution serving as a fine desulfurization solution with the pH value of 5.6 to 6.1 from the top of the tower to absorb SO2 and SO3 in the sulfur-containing exhaust, and regulating the gas-liquid ratio to be (350-370): 1, wherein according to the concentration of aqueous ammonia in step B, the absorption mother solution refluxes to a mother solution circulating tank from the bottom of the absorption tower, and 10.3 to 10.6 mass percent of diluted aqueous ammonia is added, so that the ratio of (NH4)2SO3 to NH4HSO3 in the absorption solution is unchanged in an optimal range of the ammonium sulfite-ammonium hydrogen sulfite solution serving as the fine desulfurization solution; and the temperature of the mother solution in step B is between 25 and 30 DEG C. After the sulfur-containing exhaust is treated, the conversion rate of a sulfur acid device is more than or equal to 99.5 percent, and 60mg / Nm<3> of SO2 exhaust is discharged; and by substituting the expensive imported accelerant for the cheap domestic accelerant, the national emission standard can also be achieved, and the cost is reduced.
Owner:云南云天化云峰化工有限公司

Comprehensive treatment method for sulfur dioxide exhaust gas

InactiveCN109485072ASolve the problem of impurities brought in by storage oxidationReduce the impactDispersed particle separationAlkali metal sulfite preparationSulfite saltSodium sulfite
The invention belongs to the technical field of sulfur dioxide exhaust gas treatment and in particular relates to a comprehensive treatment method for sulfur dioxide exhaust gas. The invention solvesthe technical problem that the sulfur dioxide content is high after sulfur dioxide exhaust gas treatment. The invention provides the comprehensive treatment method for sulfur dioxide exhaust gas. Themethod comprises the following steps: a, collecting sulfur dioxide exhaust gas of a sulfur acid plant, dedusting the sulfur dioxide exhaust gas and conveying the same to an adsorption tower, and absorbing the same with a 10-17% by mass of caustic soda solution to obtain a sodium sulfite solution and exhaust gas absorbed by alkali liquor; and b, introducing exhaust chlorine into the exhaust gas absorbed by the alkali liquor, absorbing the mixed gas with 10-17% by mass caustic soda solution, wherein the absorption end point is that the effective alkali content is smaller than 1%; and absorbing to obtain a sodium hypochlorite solution and residual exhaust gas, the content of sulfur dioxide of which is smaller than 50 ppm. By treating the sulfur dioxide exhaust gas by means of the method, thecontent of sulfur dioxide in the treated residual exhaust gas is smaller than 50 ppm.
Owner:PANZHIHUA STEEL ENTERPRISES XINYU CHEM
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