首页> 外国专利> PROCEDURE FOR THE ELABORATION OF A MATERIAL AND ENERGETIC RESERVE OF SOFT ACIDS ATTACKED BY THE ENERGETICS OF TITANIUM DIHYDROXIDE AFTER THE SULPHATE METHOD.

PROCEDURE FOR THE ELABORATION OF A MATERIAL AND ENERGETIC RESERVE OF SOFT ACIDS ATTACKED BY THE ENERGETICS OF TITANIUM DIHYDROXIDE AFTER THE SULPHATE METHOD.

机译:硫酸盐法后,将二羟基氢氧化钛的能量所侵蚀的软酸的物质和能量储备进行细化的程序。

摘要

The invention relates to a process for energy- and material-saving treatment of the diluted acid which is obtained in the manufacture of titanium dioxide and contains 20 to 24 % by weight of H2SO4 and dissolved metal sulphates. This acid is directly contacted in circulation with hot, unpurified calcination off-gases and preconcentrated to a concentration of 26 to 29 % by weight of H2SO4 and the concentration of this acid is kept constant by adding further diluted acid and unpurified calcination off-gases into the circulation. A residue then precipitates which essentially contains titanium dioxide as well as calcium sulphate and a little silica. After previous addition of anhydrite seeds, as necessary, to the preconcentrated acid, the residue is separated off, preferably in a membrane filter press, freed of the major part of the calcium sulphate by washing with water and recycled into the titanium dioxide manufacturing process. In the case of relatively iron-rich diluted acids, for example those originating from ilmenite, a mixture of water-containing metal sulphates, which is called "green salt" and contains predominantly iron(II) sulphate heptahydrate, is precipitated by cooling crystallisation from the preconcentrated acid separated from the residue, and separated off. This step is unnecessary in the case of acids containing less iron. The acid is then concentrated up to 60 to 71 % by weight of H2SO4, metal sulphates ("filter salt") precipitating which are likewise separated off. The acid is recycled to the raw material digestion, and the filter salt can be thermally cracked, the cracking gases being processed to give high-percentage sulphuric acid. Alternatively, the filter salt can be neutralised. During the preconcentration and further concentration, at least 80 % by weight of the calcium sulphate originally present in the diluted acid can be precipitated and separated off.
机译:本发明涉及一种用于在二氧化钛的生产中获得的稀酸的节能和材料处理的方法,所述稀酸包含20至24重量%的H 2 SO 4和溶解的金属硫酸盐。使该酸与未纯化的高温煅烧废气直接循环接触,并预先浓缩至H2SO4的浓度为26%至29%(重量),并通过向其中添加进一步的稀酸和未纯化的煅烧废气使该酸的浓度保持恒定。流通。然后沉淀出残余物,其基本上包含二氧化钛以及硫酸钙和少量二氧化硅。在必要时将预先准备好的硬石膏种子添加到预浓缩的酸中之后,优选在膜压滤机中将残留物分离出来,通过用水洗涤将大部分硫酸钙除去,然后循环到二氧化钛生产过程中。在相对富铁的稀酸的情况下,例如那些来自钛铁矿的稀酸,一种含水的金属硫酸盐的混合物被称为“绿色盐”,主要含有七水合硫酸铁(II),通过冷却结晶从中沉淀出来。从残余物中分离出预浓缩的酸,并分离出来。对于含铁量较少的酸,此步骤是不必要的。然后将酸浓缩至高达60-71重量%的H 2 SO 4,沉淀出同样被分离出的金属硫酸盐(“滤盐”)。酸被循环到原料消化中,滤盐可以进行热裂化,处理裂化气体得到高含量的硫酸。或者,可以将滤盐中和。在预浓缩和进一步浓缩期间,最初存在于稀酸中的硫酸钙的至少80重量%可以沉淀并分离出来。

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