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75 results about "Arsenous acid" patented technology

Arsenous acid (or arsenious acid) is the inorganic compound with the formula H₃AsO₃. It is known to occur in aqueous solutions, but it has not been isolated as a pure material, although this fact does not detract from the significance of As(OH)₃.

Method for preparing arsenic trioxide from arsenic sulfide waste

The invention provides a method for preparing arsenic trioxide from arsenic sulfide waste. The arsenic sulfide waste is soaked in a sodium hydroxide solution to extract arsenic sulfide, arsenic sulfide mixes with an excessive amount of arsenic acid, and the mixture reacts at a temperature ranging from 40 DEG C to 95 DEG C for 0.5 to 3 hours, to produce a mixture containing arsenous acid and elemental sulfur; the mixture containing arsenous acid and elemental sulfur mixes with 2 to 5 times (by mass) of water and then oxygen gas is introduced so that arsenous acid is oxidized into arsenic acid, and the reaction product is filtered to remove elemental sulfur and thus to produce an arsenic acid solution; and the arsenic acid solution is reduced by sulfur dioxide gas to arsenous acid with a lower solubility, the reaction liquid is distilled under a reduced pressure to produce a saturated solution of arsenous acid, the saturated solution of arsenous acid is cooled so that arsenous acid is crystallized and then filtered to produce a filter cake of arsenous acid, and the filter cake of arsenous acid is dried and pulverized to obtain an arsenic trioxide product. The method has a short process flow, increases the recovery rate of arsenic, avoids the production of secondary pollutants, adopts simple equipment, greatly reduces the cost of arsenic recovery and is worthy to be widely applied.
Owner:JIANGSU ZHONGKE MACHINERY

Compound technology for removing As, Sb, Bi by utilizing copper electrolyte

The invention discloses a compound technology for removing, Sb, Bi by utilizing copper electrolyte. A process for removing As by means of solvent extraction and a process of removing Sb and Bi by means of solution self-purification are combined; copper arsenite crystals are prepared by As in a back-extraction solution and is used as a high arsenic electrolytic additive; during high arsenic electrolysis, Sb and Bi in the solution can be effectively removed through As (III), and a majority of Sb and Bi in an anode plate enter anode mud. According to the compound technology, the aims of removing As, Sb and Bi can be fulfilled; meanwhile, an electro-deposition induced decoppering and dearsenification method is eliminated in the main process, and a small quantity of nickel removal liquid in the auxiliary process needs to be subjected to electro-deposition treatment. The compound technology is low in power consumption; the amount of H3As gas, black copper plates and black copper powder is obviously reduced; a dearsenification product is sold in a form of As2O3 or stacked in a form of calcium arsenate. According to the method, the operating environment is optimized, the defects that the As removal product contains a large amount of copper in the electro-deposition induced decoppering and dearsenification method and needs to be returned to a pyrogenic process system for separating copper and arsenic are overcome; the electro-deposition during the main impurity removal process is avoided, and the energy consumption is obviously reduced.
Owner:CHINA NERIN ENG

Nano zero valent iron @ molecular sieve composite material and preparation method and applications thereof

The invention relates to a nano zero valent iron @ molecular sieve composite material and a preparation method and applications thereof. The preparation method comprises following steps: preparing aniron salt solution; adding molecular sieves into the iron salt solution; mechanically stirring the iron salt solution under the protection of nitrogen so as to introduce iron ions into the molecular sieves to obtain a mixed solution (A) containing molecular sieves and iron salts; subjecting the mixed solution (A) to solid-liquid separation; after separation, mixing the solids with water to obtaina mixed reaction solution; under the protection of nitrogen and mechanical stirring, adding a solution of a reducing agent into the mixed reaction solution, keeping on stirring to obtain a mixed solution (B); subjecting the mixed solution (B) to solid-liquid separation; and finally washing and drying the obtained solids after separation to obtain the nano zero valent iron @ molecular sieve composite material. The synthesized nano zero valent iron @ molecular sieve composite material has a cation exchange function of molecular sieves and an adsorption-reduction function of nano zero valent ironand has a good effect on removing cations of heavy metals such as Pb<2+>, Cu<2+>, etc. and anions such as ions of arsenous acid.
Owner:WUHAN UNIV OF SCI & TECH

Arsenic sulfide waste residue recycling treatment method and device thereof

The invention discloses an arsenic sulfide waste residue recycling treatment method, which comprises the following steps: performing alkaline leaching to obtain sulfo-arsenite or sulfo-arsenate solution, filtering to remove waste residues through a filter, to obtain alkaline leachate, then performing oxidation desulfurization, so as to oxidize sulfo-arsenite or sulfo-arsenate into sulfo-arsenite or arsenate ions, then filtering and separating elemental sulfur through another filter to obtain arsenite or arsenate solution, recovering acid-base from the arsenite or arsenate solution by utilizing a bipolar membrane device, returning base solution for alkaline leaching and acid solution for crystalization and preparation of As2O3 or As2O5, performing electrodialysis or reverse osmosis concentration on residual liquor in a bipolar membrane salt chamber, returning concentrated liquor as inflowing water of the salt chamber of the bipolar membrane device, and draining or recovering fresh water. According to the arsenic sulfide waste residue recycling treatment method, the problems that for the traditional arsenic sulfide waste residue treatment method, consumption is large, the content of arsenic in effluent water does not reach the standard, the recycling rate is low, the technological process is complicated, secondary pollution exists and the like can be solved, the content of arsenic in effluent water reaches the standard, the recycling rate of As and S is high, the advantages of low consumption, low running cost, simple technological process and the like can be achieved.
Owner:BEIJING CYCLE COLUMBUS ENVIRONMENTAL SCI & TECH

Energy saving process and system for comprehensively recycling waste acid of sulfuric acid purification

The invention discloses an energy saving process for comprehensively recycling waste acid of sulfuric acid purification. The energy saving process comprises the following steps: high-temperature flue gas is fed into a first-stage washing tower; acidic liquor at the bottom of a tower is pumped to an acid discharging spraying head in a gas inlet pipeline of the first-stage washing tower, and the acidic liquor is in contact with the high-temperature flue gas reversely to absorb SO3 in the flue gas; the flue gas washed by the acidic liquor is cooled and then enters a subsequent conventional purification process for continuous cooling, and condensed diluted acid generated in the subsequent cooling process is returned into the first-stage washing tower to keep the SO3 and water in the tower balanced; heavy metal dust and arsenic elements in the flue gas form sulfate and arsenious acid after being washed by the acidic liquor; a compressed air aeration device oxidizes the arsenious acid in the acidic liquor into arsenic acid; the acidic liquor containing the arsenic acid and the heavy metal acid salt is conveyed into a cooling and thickening tower; concentrated acid from the cooling and thickening tower is filtered by a slag filter to filter out heavy metal sulfate slag; filtrate enters an SO2 reducing tank, and high-concentration SO2 gas is fed into the tank, so that the arsenic acid is reduced into arsenious acid precipitates which can be slightly dissolved in the sulfuric acid; the acidic liquor containing the arsenious acid precipitates is subjected to solid-liquid separation to obtain an arsenious acid filter cake.
Owner:中铝环保节能集团有限公司

Method for separating and recovering arsenic from metallurgical material acid leaching liquid

A method for separating and recovering arsenic from a metallurgical material acid leaching liquid comprises the following steps: selectively adsorbing arsenic by adopting antimony or/and bismuth oxide and hydrate thereof as an adsorbent in order to remove arsenic, and filtering to obtain an arsenic removed liquid and a supported adsorbent; recovering valuable metals from the arsenic removed liquid, adding a sodium carbonate or/and sodium hydroxide solution to the supported adsorbent, carrying out stirring desorbing regeneration, and filtering to obtain a regenerated adsorbent and a desorption liquid; and returning the regenerated adsorbent to the arsenic adsorbing removal process for cycle use, carrying out cooling crystallization on the desorption liquid to precipitate disodium hydrogen arsenate crystals, and returning a disodium hydrogen arsenate crystallization mother liquor to the above supported adsorbent desorption process for cycle use. Obtained disodium hydrogen arsenate can be dried to obtain a product, and the product can be directly sold in the market, or can be used as an arsenous acid production raw material in order to realize recycling of As in the acid leaching liquid. The method has the advantages of simple process, simple operation, low production cost, good arsenic removal effect, no side effects on recovery of the valuable metal from the liquid, and thorough elimination of pollution of the arsenic removal process of the metallurgical material acid leaching liquid to environment.
Owner:CENT SOUTH UNIV

Resource treatment method for smelting flue gas washing wastewater

The invention discloses a resource treatment method for smelting flue gas washing wastewater. According to the method, smelting flue gas washing wastewater is subjected to resourceful treatment through the steps of reduction neutralization deacidification, step-by-step adsorption defluorination and dechlorination, neutralization purification and impurity removal and the like; the sulfuric acid inthe wastewater is neutralized with lime to obtain calcium sulfate containing less than 0.1% of As; the fluorine and the chlorine in the wastewater are separated and recovered in the form of sodium fluoride and sodium chloride solids respectively after adsorbing and enriching, the arsenic in the purification slag is recovered in the form of metallic arsenic or arsenious acid, and the valuable metals in the wastewater are enriched in the neutralization purification slag to facilitate comprehensive recovery; and the neutralized and purified liquid returns to smelting flue gas washing so as to berecycled. The method provided by the invention has the advantages of good treatment effect, high comprehensive utilization rate, zero wastewater discharge, no secondary pollution and the like, and issuitable for industrial application of smelting flue gas washing wastewater treatment.
Owner:CENT SOUTH UNIV +1

Method for removing arsenic in calcium-rich high-arsenic groundwater by using biochar

The invention discloses a method for removing arsenic in calcium-rich high-arsenic groundwater by using biochar, belonging to the field of arsenic pollution treatment for groundwater. The method comprises the following steps: adding biochar into alkaline calcium-rich high-arsenic groundwater, and carrying out a stirring reaction for at least 4 hours to remove arsenic dissolved in the groundwater,wherein the concentration of arsenic contained in the groundwater is 0.1-10 mg/L, and the concentration of calcium ions is 20-2000 mg/L. According to the invention, the specific calcium-rich high-arsenic groundwater is used as the object in which arsenic is to be removed; oxidizing active groups on the surface of the biochar are employed to oxidize low-valent arsenite in the groundwater into high-valent arsenate, and the generated arsenate reacts with the calcium ions and biochar to formation an arsenic-calcium-biochar precipitate; so the characteristic that the groundwater is rich in calciumand is alkaline is fully utilized, oxidation and adsorption means are organically combined to achieve the purpose of integrated removal of arsenic from the groundwater, and the method can effectivelysolve the common problems of low efficiency, high operating cost, complicated operation and the like in conventional methods for removing arsenic in groundwater.
Owner:HUAZHONG UNIV OF SCI & TECH

Method for measuring concentrations of four arsenic compounds in granulocytes by using HPLC (High Performance Liquid Chromatography)-ICP (Inductively Coupled Plasma)-MS method and application

The invention relates to a method for measuring the concentrations of four arsenic compounds in granulocytes by using an HPLC (High Performance Liquid Chromatography)-ICP (Inductively Coupled Plasma)-MS method and an application, and belongs to the technical field of blood sample detection. In order to solve the problem that the existing method cannot accurately measure the concentrations of fourdifferent arsenic compounds AsIII, AsV, DAV and MMVA in granulocytes, the invention provides a method for measuring the concentrations of four arsenic compounds in granulocytes by using the HPLC-ICP-MS method. The method comprises the steps of determining a detection condition, preparing a standard solution, drawing a standard curve, collecting and processing a granulocyte sample, performing sample detection and data processing. According to the method for measuring the concentrations of four arsenic compounds in granulocytes by using the HPLC-ICP-MS method and the application, each arsenic compound in granulocytes can be effectively extracted and accurately quantified. When the method is applied to the detection of the concentrations of four arsenic compounds in peripheral blood granulocytes of a patient suffering from APL (Acute Promyelocytic Leukemia, the metabolism and distribution characteristics of each arsenic form can be clarified, a technical basis is provided for revealing ofthe action mechanism of arsenic acid and reduction of toxic reactions, and when the method is used for assisting clinics, personalized medicine and targeted therapy are implemented.
Owner:HARBIN MEDICAL UNIVERSITY

Preparation method of Fe (III)-containing magnetic nano material

The invention discloses a preparation method of a Fe (III)-containing magnetic nano material, relates to a preparation method of an iron-containing magnetic nano material, and aims at solving the problems that in an existing preparation method of an iron-containing magnetic nano material for adsorbing arsenic, the reaction temperature is high, energy consumption is high, and the reaction conditions are complex. The preparation method comprises the steps that 1, magnetic particles are prepared; 2, blending is performed to obtain the Fe (III)-containing magnetic nano material. The invention further discloses application of the Fe (III)-containing magnetic nano material, and the Fe (III)-containing magnetic nano material is used for adsorbing arsenous acid ions by serving as an adsorbing agent. The preparation method has the advantages that energy consumption is low, and the reaction can be performed under stirring at room temperature; environmental friendliness is achieved, cheap metal salts FeCl3.6H2O and FeCl2.4H2O and sodium carboxymethylcellulose are used as reagents, deionized water is taken as solvent, and no template or other toxic reagent needs to be added; the yield is high, and large-scale preparation can be achieved. The preparation method is mainly used for preparing the Fe (III)-containing magnetic nano material.
Owner:NORTHEAST INST OF GEOGRAPHY & AGRIECOLOGY C A S

Method for preparing arsenic trioxide from arsenic sulfide waste

The invention provides a method for preparing arsenic trioxide from arsenic sulfide waste. The arsenic sulfide waste is soaked in a sodium hydroxide solution to extract arsenic sulfide, arsenic sulfide mixes with an excessive amount of arsenic acid, and the mixture reacts at a temperature ranging from 40 DEG C to 95 DEG C for 0.5 to 3 hours, to produce a mixture containing arsenous acid and elemental sulfur; the mixture containing arsenous acid and elemental sulfur mixes with 2 to 5 times (by mass) of water and then oxygen gas is introduced so that arsenous acid is oxidized into arsenic acid,and the reaction product is filtered to remove elemental sulfur and thus to produce an arsenic acid solution; and the arsenic acid solution is reduced by sulfur dioxide gas to arsenous acid with a lower solubility, the reaction liquid is distilled under a reduced pressure to produce a saturated solution of arsenous acid, the saturated solution of arsenous acid is cooled so that arsenous acid is crystallized and then filtered to produce a filter cake of arsenous acid, and the filter cake of arsenous acid is dried and pulverized to obtain an arsenic trioxide product. The method has a short process flow, increases the recovery rate of arsenic, avoids the production of secondary pollutants, adopts simple equipment, greatly reduces the cost of arsenic recovery and is worthy to be widely applied.
Owner:JIANGSU ZHONGKE MACHINERY

Method for recycling copper from arsenic-containing copper slag

The invention relates to a method for recycling copper from arsenic-containing copper slag. The method sequentially comprises the following steps that (a) the copper slag is mixed with strong base pieces and put into a ball mill, ball milling is conducted for 0.5-2 hours, and a ball milled mixture is obtained; (b) the ball milled mixture is put into a calcination kiln, a mixed gas of oxygen and nitrogen is fed into the calcinations kiln, calcination is conducted for 0.5-2 hours at the temperature of 600-750 DEG C, and a calcination product is obtained; (c) the calcination product is poured into a 40-80 DEG C strong alkaline solution and soaked for 0.5-1 hour, and a filtrate and filter residues are obtained through filtration; and (d) the filter residues are inserted into a cathode and an anode for electrolysis after being putting into a sulfuric acid solution for dissolution, and copper ions are deposited and precipitated on the cathode, calcium chloride and 1-ethyl-3-methylimidazolium chloride salts are added into the filtrate until no precipitation occurs, and filtration is conducted after stirring. A mixture of the calcium chloride and the 1-ethyl-3-methylimidazolium chloride salts is added into an arsenic-containing solution, and arsenous acid radicals in the solution are completely precipitated through mutual cooperation of calcium ions and 1-ethyl-3-methylimidazolium ions, so that the environmental pollution caused by the arsenous acid radicals is avoided.
Owner:YANCHENG TONGJI NEW MATERIAL TECH CO LTD
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