Treatment of a solution containing iron salts

Details Treatment of a solution containing iron salts Treatment of a solution containing iron salts

1999-11-15

2001-06-12

Smith, Duane (Department: 1724)

Liquid purification or separation

Processes

Making an insoluble substance or accreting suspended...

C210S713000, C210S714000, C210S722000, C210S758000, C423S050000, C423S052000, C423S140000, C423S146000

Reexamination Certificate

active

06245240

ABSTRACT:

This invention relates to treatment of a mixture of iron and manganese salts so as to reduce the manganese content thereof and in particular to the treatment of iron salts produced in the production of titanium dioxide by the sulphate process.
In the sulphate process for the production of titanium dioxide, titaniferous raw material such as ilmenite is digested with sulphuric acid to form a solid mass which is treated with water and filtered to provide a solution containing mainly titanium sulphate, ferrous sulphate and ferric sulphate. The ferric ions are reduced to ferrous ions by the addition of iron, and the solution is cooled under vacuum to crystallise out the ferrous sulphate (commonly known as copperas) leaving a solution of titanium sulphate from which titanium dioxide may be precipitated by hydrolysis. Alternatively, the titanium dioxide may be precipitated first and the copperas crystallised out from the waste solution.
Clearly, the quantity of copperas relative to the quantity of titanium dioxide produced depends on the ratio of iron to titanium in the raw material. Typical figures are circa 1:1 for ilmenite (massive), 0.71:1 for ilmenite (sand) and 0.15:1 for ilmenite (slag). In any case, it will be appreciated that copperas is produced in substantial amounts for which a use must be found as there are environmental problems involved in its disposal.
One use of copperas is as the base material from which a coagulant for treatment of water may be prepared. In one conventional method, the ferrous sulphate is oxidised to ferric sulphate by being dissolved in a mixture of sulphuric acid and nitric acid. On addition to water containing colloidal particles, the ferric sulphate hydrolyses to form an insoluble hydroxide which interacts with the colloidal particles causing them to coagulate. The coagulated particles can then be removed by settlement and/or filtration.
A further use of the by-product is for the production of iron oxide. However, the soluble manganese is not oxidised by the conventional methods. Although it is known that soluble manganese can be oxidised to insoluble manganese dioxide by the addition of a further oxidising agent such as peroxide or potassium permanganate, the manganese dioxide so produced is in very finely divided colloidal form which is difficult and expensive to remove, particularly on a commercial scale and hence the final ferric sulphate product still has sufficient manganese content to make it unacceptable for the above uses.
According to one aspect of the invention, there is provided a method of treating a solution containing iron salt(s) contaminated with soluble manganese salt(s) comprising adding to the solution an oxidising agent capable of converting said manganese salt(s) to manganese dioxide, characterised by the addition of manganese dioxide as seeding agent, whereby any colloidal manganese dioxide is deposited on said seed particles, and by the separation of the manganese dioxide particles from the solution containing iron salt(s).
According to a preferred feature, the seeding agent is added before the additional oxidising agent. The seed particles desirably have an average particle size of at least 10 &mgr;m, but the preferred size is 30-50 &mgr;m.
In accordance with a further preferred feature, the seed particles are produced by reacting ferrous sulphate and potassium permanganate.
In order to reduce costs, the manganese dioxide particles separated from one batch of treated ferric sulphate solution can be recycled and used as the seed particles for a further batch of solution.
Treatment of copperas by the conventional method does not necessarily convert all the ferrous sulphate to ferric sulphate. Normally, this is disadvantageous. However, in accordance with a further preferred aspect of the invention, this residual ferrous sulphate can, by the addition of potassium permanganate, be used to produce the manganese dioxide seed particles. Of course, if too little ferrous sulphate is present to produce the required amount of seed particles, further ferrous sulphate may be added.
The oxidised agent may be any of the well known agents such as ozone, a peroxide, or a persulphate. Preferably, however, the oxidising agent is potassium permanganate which is added continuously over a period in the form of a saturated solution.
The method is effective when carried out at reflux temperature. However, it may be carried out at a temperature of 70 to 80° C., i.e. the temperature at which the copperas is dissolved in the sulphuric
itric acids, so that the liquor can be taken straight from the reactor without any additional heating requirement.
The invention will be more readily understood from the following examples.


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