Process for removal and recovery of mercury from liquids

Claim 2

A process for the recovery of metallic mercury from a mercury-containing liquid having a pH of about 5 or higher to produce a purified liquid having a mercury content of less than 50 parts per billion which comprises: (a) contacting particles of metallic silver with said liquid to dissolve said mercury in said metallic silver to form a silver amalgam and a purified liquid, (b) separating said purified liquid from said silver amalgam, (c) heating said silver amalgam with a heated gas to vaporize mercury from said silver amalgam to produce mercury vapors and particles of metallic silver, said heated gas containing said mercury vapors, (d) cooling said heated gas to condense said mercury vapors to metallic mercury, and (e) recovering said metallic mercury.

Claim 3

The process of claim 1 in which said particles of metallic silver are silver powder or silver granules.

Claim 4

The process of claim 1 in which said particles of metallic silver comprise silver coated particles of ceramic materials selected from the group consisting of glass, bricks, refractories, porcelain and abrasives.

Claim 5

The process of claim 2 or 3 in which said mercury-containing liquid is selected from the group consisting of solutions of alkali metal hydroxides, alkaline earth metal hydroxides, alkali metal alkoxides, alkaline earth metal alkoxides, and alkali metal hydrosulfites.

Claim 6

The process of claim 3 in which said particles of metallic silver are glass particles coated with metallic silver.

Claim 7

The process of claim 3 in which said liquid has a pH of from about 6.5 or higher.

Claim 8

The process of claim 6 in which said silver coated particles are admixed with silver powder or silver granules.

Claim 9

The process of claim 7 in which said ceramic material is brick.

Claim 10

The process of claim 8 in which said particles have a silver content of from about 0.5 to about 90 percent by weight of silver.

Claim 11

The process of claim 9 in which said heated gas is nitrogen at a temperature of from about 100° to about 400° C.

Claim 12

The process of claim 10 in which said particles have a size of from about 27,000 to about 30 microns.

Claim 13

The process of claim 11 in which said particles form the packing of a separation column.

Claim 14

The process of claim 12 in which said particles are contacted with said liquid at a space velocity in the range of from about 0.5 to about 100 per hour.

Claim 15

The process of claim 13 in which said liquid is a solution of an alkali metal alkoxide produced by the reaction of an alkali metal amalgam with an alcohol.

Claim 16

The process of claim 14 in which said liquid is a solution of sodium methylate.

Claim 17

The process of claim 13 in which said heated gas containing mercury vapors is cooled to a temperature below 100° C. to condense said mercury vapors to form metallic mercury.

Claim 18

The process of claim 13 in which said liquid is water.

Claim 19

A process for the recovery of metallic mercury from a solution of an alkali metal alkoxide to produce a purified solution having a mercury content of less than 50 parts per billion which comprises: (a) contacting particles of metallic silver contained in a separation unit with said liquid to dissolve said mercury in said silver to form a silver amalgam and a purified solution of an alkali metal alkoxide, (b) separating said purified solution from said silver amalgam, (c) heating said silver amalgam with a heated gas to vaporize mercury from said silver amalgam to produce mercury vapors and particles of metallic silver, said heated gas containing said mercury vapors, (d) cooling said heated gas to condense said mercury vapors to metallic mercury, and (e) recovering said metallic mercury.

Claim 20

A process for the recovery of metallic mercury from a solution of an alkali metal alkoxide to produce a purified solution having a mercury content of less than 50 parts per billion which comprises: (a) contacting particles of metallic silver contained in a separation unit with said liquid to dissolve said mercury in said silver to form a silver amalgam and a purified solution of an alkali metal alkoxide, (b) separating said purified solution from said silver amalgam, (c) heating said silver amalgam with a heated gas to vaporize mercury from said silver amalgam to produce mercury vapors and particles of metallic silver, said heated gas containing said mercury vapors, (d) cooling said heated gas to condense said mercury vapors to metallic mercury, and (e) recovering said metallic mercury.

Claim 21

The process of claim 18 in which said particles of metallic silver are silver powder or silver granules.

Claim 22

The process of claim 18 in which said particles of metallic silver comprise silver coated particles of ceramic materials selected from the group consisting of glass, bricks, refractories, porcelain and abrasives.

Claim 23

The process of claim 20 in which said silver coated particles are admixed with silver powder or silver granules.

Claim 24

The process of claim 21 in which said ceramic material is brick.

Claim 25

The process of claim 22 in which said particles have a silver content of from about 5 to about 60 percent by weight of silver.

Claim 26

The process of claim 23 in which said heated gas is nitrogen at a temperature of from about 200° to about 300° C.

Claim 27

The process of claim 24 in which said particles have a size of from about 11,000 to about 150 microns.

Claim 28

The process of claim 25 in which said particles are contacted with said alkali metal methylate solution at a space velocity of from about 1 to about 60 per hour.

Claim 29

The process of claim 26 in which said alkali metal alkoxide is sodium methylate.