Process for the removal of organic contaminants from soils and sedimenta

Claim 2

A process for the decontamination of materials including solids contaminated with organic contaminants, the process comprising the steps of:

Claim 3

(a) separating the material into a solid fraction;

Claim 4

(a) separating the material into a solid fraction;

Claim 5

(b) leaching the solid fraction with a liquid consisting essentially of a hydrophilic leaching solvent and up to 30% water to obtain contaminated leaching solvent and a mixture of decontaminated solid fraction and leaching solvent, and wherein the hydrophilic solvent is completely miscible in water and has a boiling point in the range of 40° C. to 95° C. at atmospheric pressure; and

Claim 6

(b) leaching the solid fraction with a liquid consisting essentially of a hydrophilic leaching solvent and up to 30% water to obtain contaminated leaching solvent and a mixture of decontaminated solid fraction and leaching solvent, and wherein the hydrophilic solvent is completely miscible in water and has a boiling point in the range of 40° C. to 95° C. at atmospheric pressure; and

Claim 7

(c) stripping contaminants from the contaminated leaching solvent with a hydrophobic stripping solvent and water to concentrate the contaminants, and wherein the hydrophobic solvent has a density of less than 0.9 g/ml, and the hydrophobic solvent is such that a partition coefficient of the contaminants between the hydrophobic and the hydrophilic solvent is equal to or greater than 3 for the entire range of the ratio of water to hydrophilic solvent.

Claim 8

(c) stripping contaminants from the contaminated leaching solvent with a hydrophobic stripping solvent and water to concentrate the contaminants, and wherein the hydrophobic solvent has a density of less than 0.9 g/ml, and the hydrophobic solvent is such that a partition coefficient of the contaminants between the hydrophobic and the hydrophilic solvent is equal to or greater than 3 for the entire range of the ratio of water to hydrophilic solvent.

Claim 9

The process according to claim 1, further comprising: (d) stripping the leaching solvent from the mixture produced in step (b) to produce decontaminated solid fraction; and (e) recycling leaching solvent from the stripped leaching solvent of step (d) and step (c) into the leaching step (b).

Claim 10

The process according to claim 1, further comprising: (f) separating the contaminants from the contaminated stripping solvent of step (c) to produce decontaminated stripping solvent; and (g) recycling the decontaminated stripping solvent of step (f) to the stripping step (c).

Claim 11

The process according to claim 1, wherein the step (b) of leaching comprises multistage countercurrent leaching.

Claim 12

The process according to claim 1, wherein the hydrophilic solvent comprises a solvent selected from the group consisting of acetone, methanol, ethanol, and isopropanol.

Claim 13

The process according to claim 5, wherein the hydrophobic solvent includes one selected from the group consisting of the methane series with 6 to 16 carbon atoms per molecule, kerosene and toluene.

Claim 14

The process according to claim 1, wherein the step (c) of stripping comprises contacting the contaminated leaching solvent in a liquid-liquid extractor with the stripping solvent and an aqueous solution of potassium sulfate.

Claim 15

The process according to claim 1, wherein step (a) comprises separating the material into a solid fraction and a liquid fraction with residual contaminant and further comprising: (h) adsorbing residual contaminant from the liquid fraction from step (a) onto decontaminated solid fraction to produce decontaminated liquid fraction and contaminated solid fraction.

Claim 16

The process according to claim 8, comprising: adding the contaminated solid fraction from step (h) to the solid fraction to be leached in step (b).

Claim 17

The process according to claim 8, further comprising: using a portion of the decontaminated solid fraction from step (b) to constitute the decontaminated solid fraction in step (h).

Claim 18

The process according to claim 8, wherein the step (a) of separating comprises physically separating the liquid and solid fractions.

Claim 19

The process according to claim 11, wherein the step of physically separating comprises one of filtering and/or centrifuging.

Claim 20

A process for the decontamination of a mixture of sediment and water containing a contaminant including organic PCBs, the process comprising the steps of: (a) separating the mixture into a solid fraction including water and a liquid fraction including residual contaminant; (b) leaching the solid fraction with a liquid consisting essentially of a hydrophilic solvent and up to 30% water to obtain a contaminated mixture of solvent and water and a decontaminated mixture of sediment, solvent and water, and wherein the hydrophilic solvent is completely miscible in water and has a boiling point in the range of 40° C. to 95° C. at atmospheric pressure; (c) stripping contaminant from the contaminated mixture of step (b) with a hydrophobic solvent and water to produce contaminated hydrophobic solvent in which the contaminant is concentrated and a decontaminated mixture of hydrophilic solvent and water, and wherein the hydrophobic solvent has a density of less than 0.9 g 1/ml, and the hydrophobic solvent is such that a partition cofficient of the contaminant between the hydrophobic and the hydrophhilic solvent is equal to or greater than 3 for the entire range of the ratio of water to hydrophilic solvent; and (d) adsorbing the residual contaminant from the liquid fraction onto decontaminated sediment to produce decontaminated water and contaminated sediment.

Claim 21

A process for the decontamination of a mixture of sediment and water containing a contaminant including organic PCBs, the process comprising the steps of: (a) separating the mixture into a solid fraction including water and a liquid fraction including residual contaminant; (b) leaching the solid fraction with a liquid consisting essentially of a hydrophilic solvent and up to 30% water to obtain a contaminated mixture of solvent and water and a decontaminated mixture of sediment, solvent and water, and wherein the hydrophilic solvent is completely miscible in water and has a boiling point in the range of 40° C. to 95° C. at atmospheric pressure; (c) stripping contaminant from the contaminated mixture of step (b) with a hydrophobic solvent and water to produce contaminated hydrophobic solvent in which the contaminant is concentrated and a decontaminated mixture of hydrophilic solvent and water, and wherein the hydrophobic solvent has a density of less than 0.9 g 1/ml, and the hydrophobic solvent is such that a partition cofficient of the contaminant between the hydrophobic and the hydrophhilic solvent is equal to or greater than 3 for the entire range of the ratio of water to hydrophilic solvent; and (d) adsorbing the residual contaminant from the liquid fraction onto decontaminated sediment to produce decontaminated water and contaminated sediment.

Claim 22

The process according to claim 13, further comprising: (a) stripping the hydrophilic solvent and water from the decontaminated mixture produced in step (b) to produce decontaminated sediment; (f) separating hydrophilic solvent from water in the stripped hydrophilic solvent and water of step (e) and step (c); and (g) recycling the separated hydrophilic solvent from step (f) into the leaching step (b).

Claim 23

The process according to claim 7, further comprising: (h) adding the contaminated sediment from step (d) to the solid fraction to be leached in step (b); (i) using a portion of the decontaminated sediment from step (b) to constitute the decontaminated sediment in step (d); and (j) using the water obtained in step (f) for the water in step (c).

Claim 24

The process according to claim 15, further comprising: (k) separating the contaminant from the contaminated hydrophobic solvent of step (c) to produce decontaminated hydrophobic solvent; and (i) recycling the decontaminated hydrophobic solvent of step (k) to the stripping step (c).

Claim 25

The process according to claim 16, wherein the step (a) of separating comprises physically separating the liquid and solid fraction.

Claim 26

The process according to claim 17, wherein the step of physically separating comprises one of filtering and centrifuging.

Claim 27

The process according to claim 13, wherein the step (b) of leaching comprises multistage countercurrent leaching.

Claim 28

The process according to claim 19, wherein the hydrophilic solvent comprises one selected from the group consisting of acetone, methyl ethyl ketone, methanol, ethyl alcohol, isopropanol.

Claim 29

The process according to claim 20, wherein the hydrophobic solvent comprises one selected from the group consisting of the methane series with 6 to 16 carbon atoms per molecule, kerosene and toluene.

Claim 30

The process according to claim 13, wherein the step (c) of stripping comprises contacting the contaminated hydrophilic solvent in a liquid-liquid extractor with the hydrophobic solvent, and water or an aqueous solution of a mineral salt.