发明名称 Method for Producing Nanometer Lithopone from Electrolytic Zinc Acid Leaching Residue
摘要 Disclosed is a method for producing nanometer lithopone from electrolytic zinc acid leaching residue. The method comprises specific steps of: leaching, purifying, carrying out a metathetical reaction, washing, smashing and the like. Through these steps, zinc is selectively leached out by an ammonia-ammonium sulfate process; and iron and arsenic are removed by ammonium persulfate, heavy metal elements such as nickel, copper, lead, cadmium and the like are removed by sulfurization method and zinc powder replacement method; and a metathetical reaction is carried out to obtain an nZnS—BaSO4 crystalline filter cake, the crystalline filter cake is dried and smashed to obtain a nanometer lithopone product. The zinc in the acid leaching residue can be recycled effectively by this method. The ammonia leaching method is used as the technical means of effectively treating the acid leaching residue, the obtained lithopone product is good in quality, and sulfate radicals needed in the production are provided by the acid leaching residue itself, so that the resource utilization of the acid leaching residue is implemented; and in addition, the production cost is low, and the operation is simple.
申请公布号 US2015218338(A1) 申请公布日期 2015.08.06
申请号 US201214430550 申请日期 2012.09.25
申请人 SICHUAN JUHONG TECHNOLOGY CO., LTD. 发明人 Chen Shangquan;Li Shichun;Li Xiaohong
分类号 C08K3/30 主分类号 C08K3/30
代理机构 代理人
主权项 1. A method for producing nanometer lithopone from electrolytic zinc acid leaching residue comprising: 1) leaching, wherein the electrolytic zinc acid leaching residue is leached out by an ammonia-ammonium sulfate solution, the ammonia concentration is 5.5˜7.0 mol/L and the ammonium sulfate concentration is 0˜1 mol/L (regulating the sulfate concentration according to the type of product) in said ammonia-ammonium sulfate solution, the leaching temperature is 20˜50° C., and the leaching time is 3 h˜9 h; 2) purifying, including adding ammonium persulfate to said final leached solution to remove iron by oxidation method one time, and adding activated carbon to said leaching liquid to remove arsenic by adsorbing of the arsenic and iron precipitation, adding polyacrylamide flocculating agent before filtration separation, and then adding alkali sulfide to the solution of after oxidation to remove impurity, and then separating the solution to obtain filtrate, then replacing the heavy metal elements such as nickel, copper, lead, cadmium and the like in the filtrate by using zinc powder, obtaining the zinc sulfate ammonia complex refining liquid; 3) processing metathetical reaction, including dissolving sulfide in distilled water to get clear and transparent metathesis solution, adding non-ionic surfactant and mixing evenly, and then adding to said zinc sulfate ammonia complex refining liquid for metathetical reaction, obtaining lithopone emulsion, separating said emulsion by method of filtration to obtain ammonia solution and nZnS—BaSO4 crystalline filter cake, wherein said ammonia solution returns to the step of leaching after adjusting the ammonia concentration to said concentration; 4) washing and smashing, including washing said nZnS—BaSO4 crystalline filter cake by distilled water or ethanol, then separating by method of filtration, and then drying and smashing, and obtaining the nanometer lithopone product.
地址 Sichuan CN