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226 results about "Lead chloride" patented technology

Lead chloride may refer to: Lead chloride, mineral name: cotunnite. Lead chloride

Method for recovering lead from lead-containing material by matching leaching-electrowinning method

InactiveCN102206750AEasy to separateImprove the efficiency of follow-up operationsPhotography auxillary processesProcess efficiency improvementSlagLead sulfate
The invention discloses a method for recovering lead from a lead-containing material by matching a leaching-electrowinning method. The method comprises the following steps of: selectively leaching the lead from the lead-containing material at the temperature of -95DEG C by using a mixture of 0.005-0.5M ethylenediaminotetraacetateedetate and 0.05-1.0M alkali as a leaching agent, and filtering and separating to obtain a lead-containing solution; and separating out metal lead powder from the solution by using an electrowinning method, blending electrowinning waste liquor, and returning to the leaching step. By leaching lead from secondary zinc oxide soot, the grade of zinc in secondary zinc oxide and the leaching rate of subsequent leaching can be improved, and subsequent treatment is facilitated; and by leaching lead from low-grade lead slag containing lead oxide, lead sulfate or lead chloride, the leached sewage in the slag piling process never contains lead or contains little lead, environment is not affected, the waste is changed into treasure, and the lead can be recovered from the lead slag. The method has the advantages of simple flow, simple operation, low energy consumption and the like, and can be widely used for treating lead-containing secondary zinc oxide materials and low-grade lead slag.
Owner:CENT SOUTH UNIV

Method for removing sulfur from waste lead-acid storage battery gypsum mud by using magnesium chloride

The invention relates to a method for removing sulfur from waste lead-acid storage battery gypsum mud by using magnesium chloride, which is characterized by comprising the following steps of: firstly, decomposing a waste lead storage battery subjected to acid pouring to obtain the gypsum mud, and entering the next process for later treatment; then leaching the gypsum mud by using a magnesium chloride solution, converting lead sulfate in the gypsum mud into lead chloride entering into the solution, leaving other oxides of lead in leached slag, carrying out liquid-solid separation after leaching is ended, and smelting the leached slag at the low temperature to produce wet lead; cooling to crystallize a leachate to obtain solid lead chloride and crystallized mother liquor, smelting the solid lead chloride at low temperature to produce the wet lead, carrying out regeneration treatment on the crystallized mother liquor by using the crystallized mother liquor and then returning to the step of desulfurizing and leaching the gypsum mud; and finally, adding calcium chloride to the crystallized mother liquor to regenerate the magnesium chloride as a desulfurizing agent and simultaneously produce calcium sulfate as a byproduct. The invention has good desulfurizing effect, and the magnesium chloride as the desulfurizing agent has low price, is easy to regenerate and can be recycled. The invention does not have high requirement on production equipment, greatly reduces the production cost and has obvious advantages.
Owner:SHENYANG RES INST OF NONFERROUS METALS

Comprehensive recycling method of electric steel making lead and zinc-contained dust

The invention provides a comprehensive recycling method of electric steel making lead and zinc-contained dust. The comprehensive recycling method comprises the following steps: lead and zinc-contained dust is prepared as pellets for reduction roasting at high temperature; lead and zinc are reduced as simple substances for volatilization in a gas-state form; iron-contained materials are formed to molten blocks, and are separated from lead and zinc; lead and zinc-contained gas and dust are collected, and are oxidized and cooled to obtain rough oxidized lead powder and rough oxidized zinc powder; the iron-contained materials without lead and zinc are collected for quick cooling, crushing and magnetic separation to obtain iron raw materials; the rough oxidized lead powder and the rough oxidized zinc powder are put in a rotary kiln again for high-temperature sintering, and are oxidized and cooled to obtain high-purity finish oxidized lead powder and finish oxidized zinc powder; the finish oxidized lead powder and the finish oxidized zinc powder are firstly reacted with hydrochloric acid to obtain lead chloride and zinc chloride; and lead chloride and zinc chloride are reacted with sodium carbonate to finally obtain lead carbonate and zinc carbonate. The comprehensive recycling method is simple in process, high in lead and zinc recovery rate and high overall resource recycling rate.
Owner:CHONGQING UNIVERSITY OF SCIENCE AND TECHNOLOGY +1

Method for comprehensively recovering valuable metals from copper anode sludge silver separating slag

The invention relates to a copper anode sludge silver separating slag reutilization technique, particularly a method for comprehensively recovering valuable metals from copper anode sludge silver separating slag. The method comprises the following steps: carrying out hot acid leaching on silver separating slag, filtering to obtain a hot acid leaching solution containing silver and barium and hot acid leaching slag containing tin and lead; diluting the hot acid leaching solution with water, filtering to obtain a precipitate, dissolving the precipitate with nitric acid, and filtering to obtain a barium sulfate precipitate and a silver nitrate solution; reducing the solution to obtain silver powder; leaching the hot acid leaching slag with acidic chlorine salt, filtering to obtain a chlorine salt leaching solution and chlorine salt leaching slag; cooling the chlorine salt leaching solution to crystallize and precipitate lead chloride; and carrying out alkali fusion, water immersion and evaporation crystallization on the chlorine salt leaching slag to obtain sodium stannate. The method can effectively recover all the valuable metals with higher content in the silver separating slag, and the recovery rates of the lead, silver, tin and barium are respectively up to higher than 97%, 92%, 90% and 95%. The method has the characteristics of simple technique, no emission of three wastes, high metal recovery rate and the like, and is suitable for large-scale industrial production.
Owner:JIANGXI UNIV OF SCI & TECH

Processing method for waste liquid from stripping tin scolding

The invention provides a processing method for waste liquid from stripping tin scolding, which comprises the following steps: in the waste liquid from stripping tin scolding, adding a chlorate for reacting, then filtering the solution, washing the filter residue by a concentrated ammonia liquor for dissolving the silver chloride sediment, recovering silver by a washing lotion to acquire pure lead chloride, extracting a filtrate by an extractant to obtain ferric iron, wherein a strip liquor is a ferric trichloride solution which can be prepared to a tin stripping liquid, adding sulfate for depositing lead and silver, wherein the reacted filter residue is a mixed sediment of lead sulphate and silver sulfate, washing by the concentrated ammonia liquor, reducing to obtain a silver powder and lead sulphate; filtering and depositing lead and silver, depositing tin and iron, filtering to obtain the sediment and dissolving by alkali, and then electrolyzing to obtain tin, electrolyzing the residual filtrate to recovery copper, and depositing palladium in the solution to obtain the sediment for recovering palladium. The processing method has reasonable and useful process flow, and performs comprehensive recovery and utilization on valuable metal in the waste liquid from stripping tin scolding, the resource waste is reduced, and the environmental pollution is reduced.
Owner:JIANGXI GREEN ECO MFG RESOURCE CYCLE

Method for extracting heavy metals from secondary flying ash generated during burning wastes

The invention discloses a method for extracting heavy metals from secondary flying ash generated during burning wastes, which comprises the following steps of: adding secondary flying ash generated during burning wastes into water under the condition that the ratio of the secondary flying ash to the water is 1:2-3; stirring and washing with water at 60-80 DEG C for 30-90 minutes; naturally precipitating for 2-4 hours, and separating supernatant liquid from residues; adding an isometric concentrated hydrochloric acid solution into the residues, stirring, refluxing and extracting at 60-80 DEG C for 30 minutes, and centrifugally separating solids from liquid to obtain extraction liquid and residual solid residues; evaporating the supernatant liquid at 100 DEG C to obtain mixed solid powder of CuCl2 and ZnCl2, and condensing the evaporated water vapor for recycling; carrying out vacuum evaporation on the extraction liquid at 60-80 DEG C to obtain PbCl2 powder, and simultaneously, recovering the hydrochloric acid; and adding lime of which the weight concentration is 10% into the residual solid residues for stirring uniformly to form inert solid wastes. In the invention, copper chloride and zinc chloride are separated by heating and water washing firstly, and lead chloride is obtained by adding the concentrated hydrochloric acid for heating, refluxing and extracting secondly, thereby realizing the purpose of recovering heavy metals.
Owner:刘阳生 +1

Method for preparing lead chloride and calcium sulfate from lead plasters of waste lead accumulators by wet process

The invention discloses a method for preparing lead chloride and calcium sulfate from lead plasters of waste lead accumulators by a wet process. The lead plasters of the waste lead accumulators are taken as a raw material, and the method comprises the following steps of: leaching the lead plasters in an HCl-NaCl system; cooling the leach solution to separate out crystals; and separating, washing and drying. The method is characterized in that: a sulfur resource is recovered from cooling crystallization filtrate, and the cooling crystallization filtrate is in a closed cycle; the cooling crystallization filtrate is added with calcium chloride to form a calcium sulfate precipitate; the calcium sulfate precipitate is separated, washed and dried to form a calcium sulfate product; and the filtrate is used for preparing saturated NaCl solution which returns to the leaching process. Through the method, the lead chloride is obtained, and the industrial gypsum with the purity of over 97 percent is also obtained, so the sulfur resource is recycled, the cooling crystallization filtrate is circularly used, the lead recovery rate is over 96 percent after four times of circulation, and the waste of the lead resource and the lead pollution are avoided.
Owner:HEFEI UNIV OF TECH +1

Manufacturing method for perovskite solar cell with compound electronic transmission layer structure

The invention provides a manufacturing method for a perovskite solar cell with a compound electronic transmission layer structure. The method is characterized by comprising the following steps: (1) spin-coating a SnO2 compact layer on a conductive glass layer and then putting into a muffle furnace for burning for 1h at 180 DEG C; (2) dissolving iodine methylamine and lead chloride at mole ratio of (5:1)-(1:1) into N,N-dimethyl formamide, forming a solution, using a gluing machine for depositing the solution on the SnO2 compact layer, controlling the temperature at 70-150 DEG C and crystallizing, thereby acquiring a methylamine lead iodine polycrystalline film; (3) uniformly coating the organic solution of a hole-transport material onto the methylamine lead iodine polycrystalline film, thereby forming a hole-transport material layer; (4) adopting an evaporation method for evaporating a silver electrode layer on the hole-transport material layer. The cell produced according to the method provided by the invention has higher photovoltaic conversion efficiency; the compounding technique is simpler; the prepared SnO2 compound electronic transmission material is performed under lower temperature below 180 DEG C; the energy consumption of the cell is reduced; the cost is saved.
Owner:NINGBO UNIV

Preparation method of color-adjustable small-size Mn: CsPbCl3 nanocrystal

The invention discloses a preparation method of a color-adjustable small-size Mn: CsPbCl3 nanocrystal and belongs to the technical field of semiconductor nanomaterial preparation. The preparation method comprises weighing lead chloride, oleic acid, oleylamine and octadecene, putting the materials into a three-necked flask, carrying out vacuum-pumping at 120 DEG C, adding trioetylphosphine into thematerials in the nitrogen gas protective atmosphere at 150 DEG C to obtain a mixed solution, cooling the mixed solution to the room temperature, pouring a cesium oleate solution into the mixed solution for a reaction at the room temperature for 1h to obtain a CsPbCl3 nanocrystal seed, preparing lead bismuth chloride perovskite with different sizes from the CsPbCl3 nanocrystal seed, carrying out purification, adding a manganese salt into the perovskite, and carrying out grinding to obtain Mn: CsPbCl3 nanocrystals in different colors. The preparation method can adjust the amaranth of the Mn: CsPbCl3 nanocrystal to red color. The color-adjustable small-size Mn: CsPbCl3 nanocrystal has the controllable size and high fluorescence efficiency. The preparation method has simple processes, utilizes easily available raw materials, realizes large-scale synthesis and has a wide product application prospect.
Owner:JILIN UNIV

Method for separating copper from lead matte and comprehensively utilizing lead matte

The invention relates to a method for separating copper from lead matte and comprehensively utilizing lead matte, and belongs to the field of wet metallurgy of non-ferrous metals. The process is characterized by adding hydrogen peroxide under a hydrochloric acid system for oxidization leaching. The method is as follows: ball-milling lead matte blocks until grain size is lower than 100 meshes, and feeding the ball-milled lead matte into a leaching slot for carrying out oxidization leaching, wherein HCl concentration is controlled to 1mol/L-6mol/L, concentration of hydrogen peroxide is controlled to 0.5mol/L-3.5mol/L, a liquid-solid ratio is controlled to (3-10):1, a temperature is controlled to 60-90 DEG C and reaction time is controlled to 1-2 hours. Under a hydrochloric acid condition, hydrogen peroxide is utilized and used as an oxidant for leaching sulfide; in the oxidization leaching process, sulfur in the lead matte is oxidized into elemental sulfur or sulfate radical, copper is oxidized to enter liquor in the form of ion, and lead is left in slag with gold and sliver in the form of lead chloride or lead sulfate. After the leaching process is completed, solid-liquid separation is carried out to realize preliminary separation of copper and lead. Copper-rich leachate can replace deposited copper by adding scrap iron, and leaching residue is returned to a pyrogenic process lead refining system for recycling valuable elements such as lead, sliver, elemental sulfur, and the like.
Owner:CHENZHOU CITY JINGUI SILVER IND CO LTD

Ion liquid catalyst for synthesizing diethyl carbonate by urea alcoholysis and preparation method thereof

The invention provides a process for synthesizing diethyl carbonate by urea alcoholysis through an ion liquid catalyst. The catalyst is imidazole metal salts ion liquid. The method comprises the steps of adding absolute ethyl alcohol, urea and the catalyst into a high-pressure reaction kettle, wherein the agitation speed is 700-1000 r/min, the mol ratio of the absolute ethyl alcohol to the urea ranges from 5: 1 to 15: 1; the reaction temperature is 160-230 DEG C, the reaction time is 4-10 hours and the use amount of the ion liquid catalyst is 1-10% of the mass of raw materials; cooling to room temperature and separating to obtain a product; enabling 1-methylimidazole and n-chlorobutane (in a mol ratio of 1: 1) to react to synthesize an intermediate chlorinated 1-butyl-3-methylimidazole (BMIMCl); and further enabling the BMIMCl to react with a metal chloride to obtain a product. The added metal chloride is Lewis acid of zinc chloride, magnesium chloride, aluminum chloride, lead chloride, calcium chloride and the like, and is prepared by adding one or more of the Lewis acid to react according to a certain ratio. The method has the advantages of green environmental friendliness, high repeated utilization rate, simple process, no corrosion, selectivity of close to 100%, high yield (which is close to 30% to the greatest extent) and the like.
Owner:JIANGNAN UNIV

Process for separating lead and bismuth from high bismuth lead alloy

The invention discloses a process for separating lead and bismuth from a high bismuth lead alloy; and the process uses an alloy formed by casting high bismuth lead anode mud as an anode; and the alloy is fed in an anode bag for pulse chlorination electrolysis in a hydrochloric acid-chlorine salt system. Insoluble matters of the anode fall into the anode bag to form anode mud during electrolyzing; lead is dissolved in solution in a lead-chlorine complex form; and bismuth is separated out from a cathode in a rough bismuth powder form. The anode mud, lead chloride complex solution and rough bismuth powder are respectively obtained after electrolysis. The lead chloride solution is cooled for crystallization to obtain lead chloride; and crystallization mother liquor is returned to prepare electrolyte. The oxidation leaching is performed on the rough bismuth powder by adopting methane sulfonic acid to respectively obtain leaching liquid and leaching slag enriched with antimony and silver. The leaching liquid is replaced and purified for pulse electrodeposition to obtain electric bismuth; and electrodeposition back liquid is returned to leaching of the rough bismuth powder. The process can perform classified extraction on lead and bismuth in the high bismuth lead alloy; silver is enriched; the closed cycle of the technological process is realized; and the process has the advantages of simple technological process, high yield of valuable elements, cleanness and environmental protection.
Owner:YIYANG SHENGLI CHEM IND
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