Process for the removal of sulfate and metals from aqueous solutions

Claim 2

A process for reducing the concentration of water soluble ionic selenium species, sulfate ions and ionic heavy metal species in an aqueous solution containing the same comprising: providing an aqueous solution containing said water soluble ionic selenium species, sulfate ions and ionic heavy metal species, said aqueous solution having a pH of at least about 6.0; providing a porous matrix containing a population of bacteria comprising at least one anaerobic bacteria of the genus Clostridium and at least one anaerobic bacteria selected from the group consisting of bacteria of the genera Desulfovibrio and Desulfotomaculum, said bacteria being capable of matabolically reducing said ionic selenium species to water insoluble metallic selenium and said sulfate ions to hydrogen sulfide, respectively, said matrix being under anaerobic conditions; and passing said aqueous solution through said porous matrix in the presence of nutrients and at predetermined temperatures, said nutrients and said temperatures providing for the growth and steady state population density of said bacteria, to contact the ionic selenium species and the sulfate ions in said aqueous solution with the bacteria contained in the porous matrix whereby said bacteria metabolically reduce at least a portion of the ionic selenium species to water insoluble metallic selenium and at least a portion of the sulfate ions to hydrogen sulfide which, in turn, reacts with at least a portion of the water soluble ionic heavy metal species to form water insoluble heavy metal species, said water insoluble metallic selenium and water insoluble heavy metal species being substantially retained on the porous matrix, and to produce an aqueous effluent having a reduced concentration of said water soluble ionic selenium species, sulfate ion and ionic heavy metal species.

Claim 3

The process of claim 1 wherein the ionic selenium species in said aqueous solution are in the +IV and +VI oxidation states.

Claim 4

The process of claim 1 wherein the metal components in the water soluble ionic heavy metal species in said aqueous solution are capable of reacting with hydrogen sulfide to form water insoluble heavy metal species.

Claim 5

The process of claim 1 wherein the pH of the aqueous solution containing said ionic selenium species, sulfate ions and ionic heavy metal species ranges from about 6.0 to 11.0.

Claim 6

The process of claim 1 wherein said water insoluble metallic selenium, retained on the porous matrix, is encapsulated or substantially encapsulated within the cellular structure of the Clostridium bacteria contained on said matrix.

Claim 7

The process of claim 1 wherein said aqueous solution is continuously passed through said porous matrix at a rate up to about 820 liters of the aqueous solution per square meter of the porous matrix per day.

Claim 8

The process of claim 6 wherein the passing of said aqueous solution through said porous matrix containing said bacteria is carried out in the presence of at least one nutrient comprising an organic carbon source and in the presence of at least one trace nutrient.

Claim 9

The process of claim 7 wherein said nutrient, comprising an organic carbon source, is at least one material selected from the group consisting of cellulose, hemicellulose, pectic substances, inulin, chitin, lignin, hydrocarbons, starches, sugars, proteins, amino acids, organic acids, derivatives of said materials and biological and municipal waste water sludges.

Claim 10

The process of claim 8 wherein the passing of said aqueous solution through said porous matrix containing said bacteria in the presence of said nutrient is carried out at a temperature ranging from about 0° C. to about 65° C.

Claim 11

The process of claim 6 further comprising continuously separating from said porous matrix an aqueous effluent containing a significiantly reduced concentrations of said water soluble ionic selenium species, sulfate ions and ionic heavy metal species.

Claim 12

The process of claim 1 further comprising separating and recovering said water insoluble metallic selenium and water insoluble heavy metal species from said porous matrix.

Claim 13

A continuous process for reducing the concentration of water soluble ionic selenium species, sulfate ions and ionic heavy metal species in an aqueous solution containing the same comprising: providing an aqueous solution containing water soluble ionic selenium species in the +IV and +VI oxidation states, sulfate ions and water soluble ionic heavy metal species, said water soluble ionic heavy metal species being capable of reacting with hydrogen sulfide to form water insoluble heavy metal species, said aqueous waste solution having a pH ranging from about 6 to about 11; providing a porous matrix containing populations of at least one Clostridium bacteria and at least one Desulfovibrio bacteria, said bacteria being capable of metabolically reducing said water soluble ionic selenium species to water insoluble metallic selenium and said sulfate ions to hydrogen sulfide, respectively, said matrix being under anaerobic conditions; continuously passing said aqueous waste solution through said porous matrix at a rate up to about 820 liters of the aqueous waste solution per square meter of the porous matrix per day, in the presence of at least one nutrient comprising an organic carbon source and selected from the group consisting of cellulose, hemicellulose, pectic substances, inulin, chitin, hydrocarbons, starches, sugars, proteins, amino acids, organic acids biological and municipal sludges waste water and in the presence of at least one trace nutrient and at a temperature ranging from about 0° C. to about 65° C., said nutrient and said temperature providing for the growth and steady state population density of the bacteria in said matrix, to contact said selenium species with said Clostridium bacteria and thereby metabolically reduce said selenium species to water insoluble selenium metal and to contact said sulfate ions with said Desulfovibrio bacteria and thereby metabolically reduce at least a portion of said sulfate ions to hydrogen sulfide which reacts with at least a portion of the water soluble heavy metal ionic species to form water insoluble heavy metal species, said water insoluble selenium metal being substantially encapsulated in said Clostridium bacteria, said encapsulated selenium metal and water insoluble heavy metal species being substantially retained on the porous matrix; and continuously separating from said porous matrix an aqueous effluent containing a reduced concentration of said water soluble ionic selenium species and water soluble ionic heavy metal species.

Claim 14

A continuous process for reducing the concentration of water soluble ionic selenium species, sulfate ions and ionic heavy metal species in an aqueous solution containing the same comprising: providing an aqueous solution containing water soluble ionic selenium species in the +IV and +VI oxidation states, sulfate ions and water soluble ionic heavy metal species, said water soluble ionic heavy metal species being capable of reacting with hydrogen sulfide to form water insoluble heavy metal species, said aqueous waste solution having a pH ranging from about 6 to about 11; providing a porous matrix containing populations of at least one Clostridium bacteria and at least one Desulfovibrio bacteria, said bacteria being capable of metabolically reducing said water soluble ionic selenium species to water insoluble metallic selenium and said sulfate ions to hydrogen sulfide, respectively, said matrix being under anaerobic conditions; continuously passing said aqueous waste solution through said porous matrix at a rate up to about 820 liters of the aqueous waste solution per square meter of the porous matrix per day, in the presence of at least one nutrient comprising an organic carbon source and selected from the group consisting of cellulose, hemicellulose, pectic substances, inulin, chitin, hydrocarbons, starches, sugars, proteins, amino acids, organic acids biological and municipal sludges waste water and in the presence of at least one trace nutrient and at a temperature ranging from about 0° C. to about 65° C., said nutrient and said temperature providing for the growth and steady state population density of the bacteria in said matrix, to contact said selenium species with said Clostridium bacteria and thereby metabolically reduce said selenium species to water insoluble selenium metal and to contact said sulfate ions with said Desulfovibrio bacteria and thereby metabolically reduce at least a portion of said sulfate ions to hydrogen sulfide which reacts with at least a portion of the water soluble heavy metal ionic species to form water insoluble heavy metal species, said water insoluble selenium metal being substantially encapsulated in said Clostridium bacteria, said encapsulated selenium metal and water insoluble heavy metal species being substantially retained on the porous matrix; and continuously separating from said porous matrix an aqueous effluent containing a reduced concentration of said water soluble ionic selenium species and water soluble ionic heavy metal species.

Claim 15

The process of claim 12 further comprising separating and recovering said water insoluble metallic selenium and said water insoluble heavy metal species from said porous matrix.

Claim 16

The process of claim 12 wherein said aqueous solution is a mine discharge water.

Claim 17

The process of claim 14 wherein the pH of said mine discharge water ranges from about 7.0 to about 10.0.

Claim 18

The process of claim 12 wherein heavy metal components of the ionic heavy metal species in said discharge water are comprised of at least one metal, in an ionic state, selected from the group consisting of metals of Group IB, IIB, IVB, VA, VIB, VIII and the Actinide Series of the Periodic Table for Elements.

Claim 19

The process of claim 12 wherein said porous matrix is comprised of at least a porous soil, said soil containing naturally occurring populations of Clostridium and Desulfovibrio bacteria, said soil being contained in a treatment zone under anaerobic conditions.

Claim 20

The process of claim 17 wherein said aqueous solution is continuously passed through said porous matrix, contained in said treatment zone under anaerobic conditions, at a rate of flow ranging from about 86.0 to about 270 liters of aqueous solution per square meter of the porous matrix per day and where the passing of said aqueous solution through said porous matrix is carried out at a temperature ranging from about 0° C. to about 35° C. and preferably at a temperature ranging from about 12° C. to about 35° C.

Claim 21

The process of claim 18 wherein the passing of said aqueous solution through said porous matrix in said treatment zone is carried out in the presence of at least one nutrient comprising an organic carbon source and selected from the group consisting of sucrose, glucose, starch, lignin and municipal waste water sludges.