PROCESS FOR REMOVAL OF IRON CYANIDE COMPLEX

Abstract: A process for removal of iron cyanide complex or complexes from a solution. The process is characterized by contact of the solution containing the complex or complexes with a specific polysulphide, e.g., ammonium polysulphide at a temperature of from about 110 °C to about 180 °C.

Description: The invention relates to a process for the removal of iron cyanide complex or complexes from an aqueous solution. The presence of cyanide complexes in various industrial streams, such as process or effluent streams, poses significant problems of removal or disposal. In particular, these materials may interfere with further process steps, and environmental restrictions severely limit their waste effluent concentrations. With regard to waste treatment, their long term stability renders them unsuitable for standard biological waste procedures. With regard to waste effluent disposal, their toxicity or the toxicity of their derivatives or decomposition products renders them unsuitable for discharge to the environment. Accordingly, a method or process for removal of these undesirable species from aqueous solutions could have significant economic importance. It is therefore an object of the invention to provide such a removal process. Therefore, the invention is characterized by the steps of heating a solution containing said complex or complexes in a contact or conversion zone with ammonium polysulphide or sodium polysulphide, or a mixture thereof, at a temperature of from 110 °C to 180 °C, and producing a mixture having a reduced concentration of iron cyanide complex or complexes. In an advantageous embodiment the process of the invention is carried out in a closed system or vessel. As used herein, the term "iron cyanide complex" or "iron cyanide complexes" refers to either of or both the ferrocyanide ion, [Fe II (CN)₆]⁻⁴, and the ferricyanide ion, [Fe III (CN)₆]⁻³. The reactions, in the case of ammonium polysulphide, may be shown, as follows: wherein (M) is a metal ion or ions, or NH₄⁺, and × is 3, 4 or 5, and y is 4, 2 and 4/3 respectively, or wherein (M) is a metal ion or ions or NH₄⁺, and × is 3, 4, or 5, while y is 4, 2 and 4/3, respectively, and Z is (M) will be any available metal ions or ammonium ion in solution providing the appropriate charge balance, suitable metal ions including the ions of Na, K, Li, Ca, Mg, Al, Sn, etc. The invention may be practised with any suitable aqueous solution containing the iron cyanide complex or complexes. In general, any aqueous solution containing the iron cyanide complex or complexes, and which does not contain substantial concentrations of other components which react with or interfere substantially with the polysulphide(s) employed, may be used, as will be understood by those skilled in the art. Thus, the solutions treated may contain a variety of non-interfering components, such as soot and carbon, and other types of streams may be treated. However, the streams treated according to the invention can have reduced levels of or be free or substantially free of easily reactable cyanide materials, e.g., free cyanide, undissociated (HCN), and dissociated (CN⁻), referred to collectively as free cyanide species. While any or all of these components may be present to a limited extent, the polysulphide will react preferentially therewith, thus reducing the efficiency of the process. The solutions may contain materials that enhance polysulphide formation. The concentrations of the iron cyanide complex or complexes in the solutions treated are not critical, and may range from detectable or minimal impurity amounts, e.g., less than about 1 ppm by weight, to the solubility limits of the complex or complexes. Generally, the concentrations will range from about 1 to about 200 ppm, advantageously 10 to 50 ppm, all by weight. As indicated, the conversion temperatures will range from about 110 °C to about 180 °C, advantageously from about 120 °C to about 150 °C. The low temperatures of conversion, which result from the use of polysulphide to remove cyanide from the complex or complexes, represent a real energy advantage of the invention. The process of the invention may be carried out batchwise or continuously, but is advantageously carried out continuously. In such case, make-up ammonium or polysulphide (or a mixture thereof) is continuously supplied to the contact or conversion zone, and a portion or "bleed" of solution is removed from the contact zone. Whether batch or continuous, the contacting and conversion are carried out for a time sufficient to convert at least the bulk of the cyanide complex or complexes present, or to reduce the concentration of the cyanide complex or complexes to the level desired. This time may vary with the concentrations and actual temperatures employed. Obviously, longer or shorter residence times may be employed than those suggested hereinafter, it not being intended by the specification of appropriate residence times to limit the invention. In the case of a batch operation, a suitable total reaction or residence time, assuming a well stirred system, may range from a few minutes to several hours, for example about 10 minutes to about one hour. In the case of a continuous operation, the contacting and conversion are carried out in such manner that a given portion of solution in passing through the reaction zone has an average residence time as indicated, supra. Turbulent flow reactors may be utilized, or a well stirred vessel is also suitable. As noted, the system can be closed. Pressures in the conversion zone are not critical, and may range from below atmospheric to 100 atmospheres or more. Advantageously pressures will range from atmospheric to 5 or 10 atmospheres. Either ammonium polysulphide or sodium polysulphide, or a mixture thereof, may be used, although the use of ammonium polysulphide is considered advantageous. The polysulphide will advantageously be supplied as a solution, although the polysulphide may be generated in situ in the mixture or solution in the conversion or contact zone by reaction of suitable precursors. The polysulphide solution will advantageously have a pH of from about 8 to 10, more advantageously from 8.5 to 9.5. The pH of the aqueous solutions treated may be widely variable, but will advantageously range from 7 to 11, more advantageously 8.5 to 9.5, and may be adjusted to this range, if desired. Concentrations of the polysulphide are not critical, but solution will range from 0.01 to 1, advantageously 0.1 to 0.5 moles per litre. The polysulphide solution may be added to the aqueous solution containing iron cyanide complex or complexes prior to entry into the hydrolysis zone. In general, the polysulphide solution will contain at least a stoichiometric amount of the polysulphide sulphur with respect to the iron cyanide complex or complexes, and advantageously up to 3 or 4 times the stoichiometric amount. Elemental sulphur may be supplied in the contact or hydrolysis zone to maintain this concentration. It is an advantage of the invention that the products of the conversion may be sent to biotreatment. The invention will now be explained in more detail with reference to the following Examples. Example I Fifty (50) millilitres of an aqueous slurry of flyash particulates (pH 7.5) containing 15 ppm by weight of iron cyanide complex was heated for 15 minutes at 170 °C in a closed vessel with an amount of ammonium polysulphide which was in stoichiometric excess with respect to the iron cyanide complex. Analysis of the product mixture indicated that thiocyanate ion was produced, but detectable amounts of the complex were not observed. Example II In a similar experiment, in the absence of the polysulphide, only approximately 50 per cent of the iron cyanide complex was converted by the heating. The product of the conversion was ammonium formate.

Claims: A process for the removal of iron cyanide complex or complexes from an aqueous solution characterized by the steps of heating a solution containing said complex or complexes in a contact or conversion zone with ammonium polysulphide or sodium polysulphide, or a mixture thereof, at a temperature of from 110 °C to 180 °C, and producing a mixture having a reduced concentration of iron cyanide complex or complexes. The process as claimed in claim 1 characterized by the steps of adding ammonium or sodium polysulphide, or a mixture thereof, to the solution containing said complex or complexes, and heating the resultant mixture. The process as claimed in claim 1 characterized in that the solution is at least substantially free of free cyanide species. The process as claimed in claim 1 characterized in that the ammonium polysulphide, sodium polysulphide, or mixture thereof is supplied to the contact or conversion zone as a solution.

Inventors: BAKER, DANIEL CLARK
Applicants: SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
Application year: 1986
Main classification: C02F1
IPC codes: C02F1, C02F9