# US 5,705,078 A · Oxidative removal of aqueous cyanide by manganese(IV)-containing oxides

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- Number: US 5,705,078 A
- Document ID: US5705078A
- Status: Granted
- Kind: A
- Application number: 08/707,985
- Filed: 1996-08-23
- Granted: 1998-01-06
- Earliest claimed: 1996-08-23
- Assignees: Uop LLC
- Inventors: Paul R. Kurek; Tom N. Kalnes; Gregory John Lewis
- Web page: https://patentgrep.com/patent/US5705078A

## CPC

- C02F 1/74: with air (aeration of stretches of water C02F7/00)
- C02F 1/725: {by catalytic oxidation}
- C02F 1/722: {Oxidation by peroxides}
- C02F 1/78: with ozone {(C02F1/4672 takes precedence)}
- C02F 2101/18: Cyanides
- Y10S 210/904: -CN containing
- C02F: TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE (separation in general B01D; special arrangements on waterborne vessels of installations for treating water, waste water or sewage, e.g. for producing fresh water, B63J; adding materials to water to prevent corrosion C23F; treating radioactively-contaminated liquids G21F9/04; regeneration of reactants for recirculation into processes, see the relevant places for the processes)
- Y10S: TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS

## Abstract

Manganese(IV)-containing oxides are effective catalysts for oxidation of water-soluble cyanide over a wide pH range (0.5-12) and temperature (15.degree.-250.degree. C.). Oxygen is the preferred oxidizing agent at partial pressures between about 0.2 and 5 atmospheres (2.9-75 psi, 20-517 kPa). Electrolytically deposited MnO.sub.2 is one preferred form of the catalyst. Another preferred manganese(IV)-containing oxide is the group of cation-stabilized manganese(IV)-containing oxides illustrated by cryptomelane. Yet another preferred form of manganese(IV)-containing oxide is a group of crystalline manganese phosphate compositions having an extended network and an empirical composition on an anhydrous basis expressed by an empirical formula of: (A.sup.a+).sub.v (Mn.sup.b+)(M.sup.c+).sub.x P.sub.y O.sub.z where A is a templating agent selected from the group consisting of alkali metals, alkaline earth metals, hydronium ion, ammonium ion, organoammonium ions, and mixtures thereof, "a" represents a weighted average valence of A and varies from 1.0 to 2.0, "v" is the mole ratio of A to Mn and varies from about 0.1 to about 5, "b" is the average valence of Mn and has a value of greater than 3 to about 4, M is a metal selected from the group consisting of Al, Fe.sup.3+, Ca, Sn.sup.4+, Ti, Sb.sup.5+, and mixtures thereof, "x" is the mole ratio of M to Mn and varies from 0 to about 3.0, "c" is the weighted average valence of M and varies from about 1.0 to about 5.0, "y" is the mole ratio of P to Mn and varies from about 0.10 to about 5.0 and "z" is the mole ratio of O to Mn and has a value determined by the equation z=1/2(a.times.v+b+x.times.c+5.times.y).

## Claims

### Claim 1

A process of reducing the concentration of cyanide-containing compounds dissolved in an aqueous stream comprising contacting a stream containing at least one dissolved cyanide-containing compound with an oxidizing agent selected from the group consisting of oxygen, ozone, and hydrogen peroxide in the presence of a catalytically effective amount of a crystalline manganese phosphate composition at oxidation conditions, wherein said oxidizing conditions include a temperature between about 15.degree. and about 250.degree. C., said crystalline manganese phosphate composition having an extended network and an empirical composition on an anhydrous basis expressed by an empirical formula of:
(A.sup.a+).sub.v (Mn.sup.b+)(M.sup.c+).sub.x P.sub.y O.sub.z
where A is a templating agent selected from the group consisting of alkali metals, alkaline earth metals, hydronium ion, ammonium ion, organoammonium ions, and mixtures thereof, "a" represents a weighted average valence of A and varies from 1.0 to 2.0, "v" is the mole ratio of A to Mn and varies from about 0.1 to about 5, "b" is the average valence of Mn and has a value of greater than 3 to about 4, M is a metal selected from the group consisting of Al, Fe.sup.3+, Ga, Sn.sup.4+, Ti, Sb.sup.5+, and mixtures thereof, "x" is the mole ratio of M to Mn and varies from 0 to about 3.0, "c" is the weighted average valence of M and varies from about 1.0 to about 5.0, "y" is the mole ratio of P to Mn and varies from about 0.10 to about 5.0 and "z" is the mole ratio of O to Mn and has a value determined by the equation
z=1/2(a.times.v+b+x.times.c+5.times.y).

### Claim 2 (depends on 1)

The process of claim 1 where the cyanide-containing compound dissolved in said stream is an inorganic cyanide, an organic nitrile, or any combination thereof.

### Claim 3 (depends on 2)

The process of claim 2 where the organic nitrile is selected from the group consisting of acrylonitrile, acetonitrile, propionitrile, and 4-cyanopyridine.

### Claim 4 (depends on 1)

The process of claim 1 where and said oxidation conditions include a pH between about 0.5 and about 12.

### Claim 5 (depends on 4)

The process of claim 4 where the pH is between about 2 and about 10.

### Claim 6 (depends on 1)

The process of claim 1 where the oxidizing agent is oxygen.

### Claim 7 (depends on 6)

The process of claim 6 where the oxygen partial pressure is between about 0.2 and about 5 atmospheres.

### Claim 8 (depends on 1)

The process of claim 1 where the cyanide concentration is reduced by at least 90 percent.

### Claim 9 (depends on 8)

The process of claim 8 where the cyanide concentration is reduced by at least 95 percent.

### Claim 10 (depends on 9)

The process of claim 9 where the cyanide concentration is reduced by at least 98 percent.

### Claim 11 (depends on 10)

The process of claim 10 where the cyanide concentration is reduced by at least 99.5 percent.