Drilling geothermal wells with removal of H2 S

Claim 2

A process for the treatment of raw geothermal steam produced during the drilling, flow testing, or reworking of a geothermal well whereby the H 2 S gas contained in said steam is abated which comprises the steps of (A) contacting said raw steam containing entrained solids and H 2 S gas with an aqueous solution having 1 to 6 moles of ferric chelate for each mole of H 2 S in said steam, 25 to 3000 parts per million of one or more water soluble cationic polymeric catalysts, and a pH in the range of 7 to 11 whereby H 2 S is substantially completely absorbed and rapidly converted into sulfur solids and whereby a ferrous chelate solution is generated. (B) separating said ferrous chelate solution from entrained solids, and sulfur solids, (C) converting said ferrous chelate solution with an oxygen containing gas stream into a ferric chelate solution, (D) recycling said ferric chelate solution back to said contacting step for reuse.

Claim 3

The process as set forth in claim 1 wherein the mole ratio of ferric chelate to H 2 S is in the range from 2 to 4 and the pH range is 9.5 to 10.5.

Claim 4

The process as set forth in claim 1 wherein said separation step involves a residence time of said chelate solution of 0.1 to 5 hours.

Claim 5

The process as set forth in claim 1 wherein said conversion step is conducted with an oxygen containing gas at a rate to provide at least 0.5 mole of oxygen per mole of H 2 S being treated.

Claim 6

The process as set forth in claim 1 wherein said chelate is the ferric chelate of H-hydroxyethylethylenediamine triacetic acid and said polymeric catalyst is poly(dimethyl diallyl) ammonium chloride.

Claim 7

A process for the treatment of raw geothermal steam produced during the drilling, flow testing, or reworking of a geothermal well whereby the H 2 S gas contained in said steam is abated which comprises the steps of (A) contacting said raw steam containing entrained solids and H 2 S gas with an aqueous solution having 1 to 6 moles of ferric chelate for each mole of H 2 S in said steam wherein said chelate is selected from the group consisting of ethylenediaminetetraacetic acid, N-hydroxyethylethylenediaminetriacetic acid, and N-hydroxyethylaminodiacetic acid, 25 to 3000 parts per million of one or more water soluble cationic polymeric catalysts, and a pH in the range of 7 to 11 whereby H 2 S is substantially completely absorbed and converted into sulfur solids and whereby a ferrous chelate solution is generated, (B) separating said ferrous chelate solution from entrained solids, and sulfur solids, (C) converting said ferrous chelate solution with an oxygen containing gas stream into a ferric chelate solution, (D) recycling said ferric chelate solution back to said contacting step for reuse.

Claim 8

A process for the treatment of raw geothermal steam produced during the drilling, flow testing, or reworking of a geothermal well whereby the H 2 S gas contained in said steam is abated which comprises the steps of (A) contacting said raw steam containing entrained solids and H 2 S gas with an aqueous solution having 1 to 6 moles of ferric chelate for each mole of H 2 S in said steam wherein said chelate is selected from the group consisting of ethylenediaminetetraacetic acid, N-hydroxyethylethylenediaminetriacetic acid, and N-hydroxyethylaminodiacetic acid, 25 to 3000 parts per million of one or more water soluble cationic polymeric catalysts, and a pH in the range of 7 to 11 whereby H 2 S is substantially completely absorbed and converted into sulfur solids and whereby a ferrous chelate solution is generated, (B) separating said ferrous chelate solution from entrained solids, and sulfur solids, (C) converting said ferrous chelate solution with an oxygen containing gas stream into a ferric chelate solution, (D) recycling said ferric chelate solution back to said contacting step for reuse.

Claim 9

The process as set forth in claim 6 wherein the mole ratio of ferric chelate to H 2 S is in the range from 2 to 4 and the pH range is 9.5 to 10.5.

Claim 10

The process as set forth in claim 6 wherein said separation step involves a residence time of said chelate solution of 0.1 to 5 hours.

Claim 11

The process as set forth in claim 6 wherein said conversion step is conducted with an oxygen containing gas at a rate to provide at least 0.5 mole of oxygen per mole of H 2 S being treated.

Claim 12

In a process for the treatment of raw geothermal stream produced during the drilling, flow testing, or reworking of a geothermal well which includes the steps of contacting said raw steam containing H 2 S with an aqueous solution of ferric chelate having a pH in the range of 7 to 11 and having 1 to 6 moles of ferric chelate for each mole of H 2 S in said stream, separating said chelate solution from entrained solids and sulfur solids, converting said chelate solution with an oxygen containing gas into a ferric chelate solution, and recycling said ferric chelate solution back to said contacting step, the improvement which comprises adding to said chelate solution an effective amount of one or more water soluble cationic polymeric catalysts.

Claim 13

In a process for the treatment of raw geothermal stream produced during the drilling, flow testing, or reworking of a geothermal well which includes the steps of contacting said raw steam containing H 2 S with an aqueous solution of ferric chelate having a pH in the range of 7 to 11 and having 1 to 6 moles of ferric chelate for each mole of H 2 S in said stream, separating said chelate solution from entrained solids and sulfur solids, converting said chelate solution with an oxygen containing gas into a ferric chelate solution, and recycling said ferric chelate solution back to said contacting step, the improvement which comprises adding to said chelate solution an effective amount of one or more water soluble cationic polymeric catalysts.