Process for the removal of metals from solution

Claim 2

A process of removing metals from an aqueous solution containing ions of at least one dissolved metal therein which is capable of forming stable cationic complexes with polyamines and which has to be removed from said solution, said process comprising the steps of: (a) adding to said solution a polyamine selected from the group consisting of ethylenediamine, propylenediamine, triaminotriethylamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine and tetra-2-aminoethylethlenediamine in order to form stable cationic complexes with the ions of said one metal, said polyamine being added in at least equimolar amount with respect to said metal; (b) contacting the solution of step (a) with a cation exchanger selected from the group consisting of synthetic and natural tectosilicates and phyllosilicates, in an amount of 3 to 30 grams of cation exchanger per gram of metal ion to be removed from solution, in order to adsorb said stable cationic metal-polyamine complexes from said aqueous solution onto said cation exchanger, and (c) separating said cation exchanger from said aqueous solution after contact.

Claim 3

The process as claimed in claim 1, wherein said at least one dissolved metal is selected from the group consisting of elements from groups III B, IV B, V B, VI B, VII B, VIII, I B, II B, III A, IV A, V A, VI A, and VII A of the Periodic System of Elements as far as comprised in periods 4,5,6 and 7 of that System and as far as being capable of forming stable cationic complexes with polyamines.

Claim 4

A process of removing metals from an aqueous solution containing ions of at least one metal dissolved therein which is capable of forming stable cationic complexes with polyamines and which has to be removed from the solution, said process comprising the steps of: (a) combining a polyamine selected from the group consisting of ethylenediamine, propylenediamine, triaminotriethylamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine and tetra-2-aminoethylethylenediamine with a cation exchanger selected from the group consisting of synthetic and natural tectosilicates and phyllosilicates in order to form a solid adsorbent, said polyamine and said cation exchanger being combined in such a mutual ratio as to ensure that at least an equimolar amount of polyamine is present with respect to said metal when the resulting solid adsorbent is added to said aqueous solution in an amount corresponding to 3-30 grams of cation exchanger per gram of metal ion to be removed from solution; (b) contacting said aqueous solution with said solid adsorbent in order to adsorb said metal ion from said solution and form stable cationic polyamine-metal complexes on said cation exchanger in said solid adsorbent, said solid adsorbent being used in an amount corresponding to 3 to 30 grams of cation exchanger per gram of metal ion to be removed from solution; and (c) separating said solid adsorbent from said aqueous solution after contact.

Claim 5

A process of removing metals from an aqueous solution containing ions of at least one metal dissolved therein which is capable of forming stable cationic complexes with polyamines and which has to be removed from the solution, said process comprising the steps of: (a) combining a polyamine selected from the group consisting of ethylenediamine, propylenediamine, triaminotriethylamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine and tetra-2-aminoethylethylenediamine with a cation exchanger selected from the group consisting of synthetic and natural tectosilicates and phyllosilicates in order to form a solid adsorbent, said polyamine and said cation exchanger being combined in such a mutual ratio as to ensure that at least an equimolar amount of polyamine is present with respect to said metal when the resulting solid adsorbent is added to said aqueous solution in an amount corresponding to 3-30 grams of cation exchanger per gram of metal ion to be removed from solution; (b) contacting said aqueous solution with said solid adsorbent in order to adsorb said metal ion from said solution and form stable cationic polyamine-metal complexes on said cation exchanger in said solid adsorbent, said solid adsorbent being used in an amount corresponding to 3 to 30 grams of cation exchanger per gram of metal ion to be removed from solution; and (c) separating said solid adsorbent from said aqueous solution after contact.

Claim 6

The process as claimed in claim 3, wherein said at least one dissolved metal is selected from the group consisting of elements from groups III B, IV B, V B, VI B, VII B, VIII, I B, II B, III A, IV A, V A, VI A, and VII A of the Periodic System of Elements as far as comprised in periods 4,5,6 and 7 of that System and as far as being capable of forming stable cationic complexes with polyamines.

Claim 7

The process as claimed in claim 3, wherein said at least one dissolved metal is selected from the group consisting of mercury, cadmium, copper, zinc, nickel and cobalt.

Claim 8

The process as claimed in claim 3, wherein said polyamine has at least 4 amino groups per molecule.

Claim 9

The process as claimed in claim 3, wherein tetraethylenepentamine is used as a polyamine and at least one of montmorillonite and bentonite is used as a cation exchanger, and said aqueous solution contains at least one of copper and mercury ions as dissolved metal ions to be removed.

Claim 10

The process as claimed in claim 3, wherein said polyamine is combined with said cation exchanger by admixing said polyamine to an aqueous slurry of said cation exchanger at a pH of about 7, separating a resulting solid adsorbent from said slurry and drying said solid adsorbent.

Claim 11

The process as claimed in claim 3, wherein said aqueous solution is a waste water derived from at least one of metal-processing and metal-plating industries.

Claim 12

The process as claimed in claim 3, wherein contact of said solid adsorbent with said aqueous solution is effected during a period of about 2 hours.

Claim 13

The process as claimed in claim 3, wherein said contact is effected batchwise.

Claim 14

The process as claimed in claim 11 wherein said at least one dissolved metal is selected from the group consisting of mercury, cadmium, copper, zinc, nickel and cobalt.

Claim 15

The process as claimed in claim 11, wherein said polyamine has at least four amino groups per molecule.

Claim 16

The process as claimed in claim 11, wherein tetraethylenepentamine is used as a polyamine and at least one of montmorillonite and bentonite is used as a cation exchanger, and said aqueous solution contains at least one of copper and mercury ions as dissolved metal ions to be removed.

Claim 17

The process as claimed in claim 11, wherein said aqueous solution is a waste water derived from at least one of metal-processing and metal-plating industries.

Claim 18

The process as claimed in claim 11, wherein said contact is effected batchwise.