Process for integrating treatment of and energy derivation from geothermal brine

Claim 2

A process for treating and deriving useful energy from a two-phase geothermal brine produced from a subterranean geothermal reservoir, said two-phase geothermal brine containing non-condensible gases, including hydrogen sulfide, and also containing heavy and/or transition metals in solution, the process comprising: (a) separating said non-condensible gases from said produced geothermal brine, thereby separating a substantial majority of said hydrogen sulfide from said geothermal brine; (b) flashing a portion of said separated geothermal brine to a high quality steam; (c) deriving useful energy from said high quality steam; (d) converting substantially all of said hydrogen sulfide separated from said geothermal brine with said non-condensible gases to sulfur and/or other sulfur compounds of a higher oxidized state; (e) removing a portion of said sulfur and/or other sulfur compounds of a higher oxidized state from said non-condensible gases to form an environmentally acceptable vent gas; (f) discharging at least a portion of said environmentally acceptable vent gas to the atmosphere; (g) mixing said portion of saod sulfur and/or sulfur compounds of a higher oxidized state with the geothermal brine remaining after step (b); and (h) injecting the mixture formed in step (g) into said subterranean geothermal reservoir.

Claim 3

The process defined in claim 1 wherein said produced geothermal brine further contains silica in solution and said geothermal brine is maintained at a temperature above the temperature required to maintain silica in solution.

Claim 4

The process defined in claim 1 wherein during step (d) said hydrogen sulfide is catalytically converted to sulfur dioxide.

Claim 5

The process defined in claim 1 wherein prior to separating non-condensible gases from said geothermal brine in step (a) the process further comprises the step of adding an oxidant to said two-phase geothermal brine to oxidize at least a portion of said hydrogen sulfide.

Claim 6

The process defined in claim 1 further comprising the step of, prior to step (d), contacting said separated non-condensible gases containing hydrogen sulfide with a selected scrubber liquid to remove entrained brine constituents and a minor portion of the hydrogen sulfide therefrom; and combining the scrubber liquid containing said minor portion of hydrogen sulfide and brine constituents with the mixture injected in step (h), the composition of said scrubber liquid being selected such that said minor portion of hydrogen sulfide is converted to sulfur and/or sulfur compounds of a higher oxidized state, thereby avoiding the formation of heavy and/or transition metal sulfides in the mixture injected in step (h).

Claim 7

A process for treating and deriving useful energy from a two-phase geothermal brine produced from a subterranean geothermal reservoir, containing non-condensible gases, including hydrogen sulfide, and also containing heavy and/or transition metals in solution, which comprises: (a) separating steam and said non-condensible gases from said produced geothermal brine; (b) flashing a portion of said produced geothermal brine to a high quality steam; (c) separating said high quality steam from the remaining geothermal brine; (d) deriving useful energy from said high quality steam; (e) cooling said steam and non-condensible gases separated from said produced geothermal brine in step (a), thereby condensing a portion of the steam; (f) separating said condensed portion from said non-condensible gases and uncondensed steam; (g) contacting said non-condensible gases and uncondensed steam with a scrubber liquid thereby removing deleterious brine constituents and a portion of the hydrogen sulfide from said separated non-condensible gases and uncondensed steam; (h) converting substantially all the hydrogen sulfide present in said separated non-condensible gases and uncondensed steam to sulfur dioxide, thereby forming a product gas containing sulfur dioxide; (i) removing a portion of said sulfur dioxide from said product gas while condensing substantially all of the remaining uncondensed steam, thereby forming an environmentally acceptable vent gas; (j) discharging at least a first portion of said environmentally acceptable vent gas to the atmosphere; (k) mixing said condensed portion and said scrubber liquid containing deleterious brine constituents and hydrogen sulfide; (l) contacting the mixture of (k) containing hydrogen sulfide with a stoichiometric excess of sulfur dioxide formed in (h) to produce a fluid mixture substantially free of hydrogen sulfide; (m) adding the mixture of (l) to the remaining geothermal brine of (c); and (n) injecting the mixture formed in (m) into said subterranean geothermal reservoir.

Claim 8

A process for treating and deriving useful energy from a two-phase geothermal brine produced from a subterranean geothermal reservoir, containing non-condensible gases, including hydrogen sulfide, and also containing heavy and/or transition metals in solution, which comprises: (a) separating steam and said non-condensible gases from said produced geothermal brine; (b) flashing a portion of said produced geothermal brine to a high quality steam; (c) separating said high quality steam from the remaining geothermal brine; (d) deriving useful energy from said high quality steam; (e) cooling said steam and non-condensible gases separated from said produced geothermal brine in step (a), thereby condensing a portion of the steam; (f) separating said condensed portion from said non-condensible gases and uncondensed steam; (g) contacting said non-condensible gases and uncondensed steam with a scrubber liquid thereby removing deleterious brine constituents and a portion of the hydrogen sulfide from said separated non-condensible gases and uncondensed steam; (h) converting substantially all the hydrogen sulfide present in said separated non-condensible gases and uncondensed steam to sulfur dioxide, thereby forming a product gas containing sulfur dioxide; (i) removing a portion of said sulfur dioxide from said product gas while condensing substantially all of the remaining uncondensed steam, thereby forming an environmentally acceptable vent gas; (j) discharging at least a first portion of said environmentally acceptable vent gas to the atmosphere; (k) mixing said condensed portion and said scrubber liquid containing deleterious brine constituents and hydrogen sulfide; (l) contacting the mixture of (k) containing hydrogen sulfide with a stoichiometric excess of sulfur dioxide formed in (h) to produce a fluid mixture substantially free of hydrogen sulfide; (m) adding the mixture of (l) to the remaining geothermal brine of (c); and (n) injecting the mixture formed in (m) into said subterranean geothermal reservoir.

Claim 9

The process defined in claim 6 wherein step (d) is performed by scrubbing said high quality steam with a liquid to remove deleterious brine constituents in said high quality steam, and utilizing said scrubbed high quality steam to drive a turbine which drives an electrical generator, said scrubbed high quality steam exiting the turbine being condensed to form a high quality steam condensate.

Claim 10

The process defined in claim 7 wherein step (i) is performed by scrubbing said product gas with at least a portion of said high quality steam condensate to remove substantially all of said sulfur dioxide.

Claim 11

The process defined in claim 8 wherein at least a portion of the high quality steam condensate containing sulfur dioxide formed in step (i) is then utilized as the scrubber liquid in step (g).

Claim 12

The process defined in claim 8 wherein at least a second portion of said high quality steam condensate is utilized as the scrubber liquid in step (g) and wherein the high quality steam condensate containing sulfur dioxide formed in (i) is added to the mixture formed in step (m).

Claim 13

The process defined in claim 10 wherein step (l) is performed by adding the mixture formed in step (k) to said product gas.

Claim 14

The process defined in claim 8 wherein said produced geothermal brine further contains silica in solution and said produced geothermal brine and mixtures therewith are maintained at a temperature above the temperature required to keep silica in solution.

Claim 15

The process defined in claim 6 wherein said hydrogen sulfide is catalytically converted to sulfur dioxide.

Claim 16

The process defined in claim 6 further comprising the step of, prior to step (a), adding an oxidant to said two-phase geothermal brine to oxidize at least a portion of the hydrogen sulfide contained therein.

Claim 17

The process of claim 6 wherein prior step (h), the process further includes the steps of converting a substantial portion of the hydrogen sulfide present in said separated non-condensible gases and uncondensed steam to elemental sulfur; and separating said elemental sulfur from said separated non-condensible gases and uncondensed steam.

Claim 18

The process defined in claim 6 further including the steps of, prior to step (b), countercurrently contacting said produced geothermal brine containing non-condensible gases with a second portion of said environmentally acceptable vent gas thereby stripping residual non-condensible gases from said produced geothermal brine; and thereafter adding the gases thus stripped from said produced geothermal brine to said separated steam and non-condensible gases prior to step (e).

Claim 19

A process for treating and deriving useful energy from a two-phase geothermal brine produced from a subterranean geothermal reservoir, containing non-condensible gases, including hydrogen sulfide, and also containing heavy and/or transition metals in solution, which comprises: (a) separating steam and said non-condensible gases from said produced geothermal brine; (b) flashing a portion of said produced geothermal brine to a high quality steam; (c) separating said high quality steam from the remaining geothermal brine; (d) deriving useful energy from said high quality steam; (e) cooling said steam and non-condensible gases separated from said produced geothermal brine in step (a) thereby condensing a portion of the steam; (f) separating said condensed portion from said non-condensible gases and uncondensed steam; (g) contacting said non-condensible gases and uncondensed steam with a scrubber liquid thereby removing deleterious brine constituents and a portion of the hydrogen sulfide from said separated non-condensible gases and uncondensed steam; (h) mixing said condensed portion and said scrubber liquid containing deleterious brine constituents and said portion of the hydrogen sulfide; (i) separating substantially all of said portion of hydrogen sulfide form the mixture formed in step (h) to form a liquid mixture having trace amounts of hydrogen sulfide; (j) adding said portion of hydrogen sulfide to the separated non-condensible gases and uncondensed steam from step (g) to form a feed gas; (k) converting substantially all the hydrogen sulfide present in said feed gas to sulfur dioxide, thereby forming a product gas containing sulfur dioxide and uncondensed steam; (l) removing substantially all of said sulfur dioxide from said product gas, while condensing substantially all of said uncondensed steam, thereby forming an environmentally acceptable vent gas; (m) discharging at least a portion of said environmentally acceptable vent gas to the atmosphere; (n) contacting the liquid mixture from step (i) with a stoichiometric excess of the sulfur dioxide formed in (k) to form a fluid mixture substantially free of hydrogen sulfide; (o) adding the fluid mixture formed in step (n) to the remaining geothermal brine of step (c); and (p) injecting the mixture formed in step (o) into said subterranean geothermal reservoir.

Claim 20

A process for treating and deriving useful energy from a two-phase geothermal brine produced from a subterranean geothermal reservoir, containing non-condensible gases, including hydrogen sulfide, and also containing heavy and/or transition metals in solution, which comprises: (a) separating steam and said non-condensible gases from said produced geothermal brine; (b) flashing a portion of said produced geothermal brine to a high quality steam; (c) separating said high quality steam from the remaining geothermal brine; (d) deriving useful energy from said high quality steam; (e) cooling said steam and non-condensible gases separated from said produced geothermal brine in step (a) thereby condensing a portion of the steam; (f) separating said condensed portion from said non-condensible gases and uncondensed steam; (g) contacting said non-condensible gases and uncondensed steam with a scrubber liquid thereby removing deleterious brine constituents and a portion of the hydrogen sulfide from said separated non-condensible gases and uncondensed steam; (h) mixing said condensed portion and said scrubber liquid containing deleterious brine constituents and said portion of the hydrogen sulfide; (i) separating substantially all of said portion of hydrogen sulfide form the mixture formed in step (h) to form a liquid mixture having trace amounts of hydrogen sulfide; (j) adding said portion of hydrogen sulfide to the separated non-condensible gases and uncondensed steam from step (g) to form a feed gas; (k) converting substantially all the hydrogen sulfide present in said feed gas to sulfur dioxide, thereby forming a product gas containing sulfur dioxide and uncondensed steam; (l) removing substantially all of said sulfur dioxide from said product gas, while condensing substantially all of said uncondensed steam, thereby forming an environmentally acceptable vent gas; (m) discharging at least a portion of said environmentally acceptable vent gas to the atmosphere; (n) contacting the liquid mixture from step (i) with a stoichiometric excess of the sulfur dioxide formed in (k) to form a fluid mixture substantially free of hydrogen sulfide; (o) adding the fluid mixture formed in step (n) to the remaining geothermal brine of step (c); and (p) injecting the mixture formed in step (o) into said subterranean geothermal reservoir.

Claim 21

The process defined in claim 17 wherein step (d) is performed by scrubbing said high quality steam with a liquid to remove deleterious brine constituents entrained in said high quality steam, and utilizing said scrubbed high quality steam to operate a turbine which drives an electrical generator, said scrubbed high quality steam being condensed to form a high quality steam condensate.

Claim 22

The process defined in claim 18 wherein step (l) is performed by scrubbing said product gas with at least a first portion of said high quality steam condensate to remove substantially all of said sulfur dioxide.

Claim 23

The process defined in claim 19 wherein a second portion of said condensed high quality steam is utilized as the scrubber liquid in step (g) and wherein the high quality steam condensate containing sulfur dioxide formed in (l) is added to the mixture formed in step (o).

Claim 24

The process defined in claim 20 wherein step (n) is performed by adding the liquid mixture formed in step (i) to said product gas.

Claim 25

The process defined in claim 19 wherein said produced geothermal brine further contains silica in solution and said produced geothermal brine and mixtures therewith are maintained at a temperature above the temperature required to keep silica in solution.

Claim 26

The process of claim 17 wherein said hydrogen sulfide is catalytically converted to sulfur dioxide in step (k).

Claim 27

The process of claim 17 further comprising the step of, prior to step (a), adding an oxidant to said two-phase geothermal brine to oxidize at least a portion of the hydrogen sulfide contained therein.

Claim 28

The process of claim 17 wherein the separation of step (a) is performed in two gas-liquid separators connected in series for brine flow therethrough.

Claim 29

A process for treating and deriving useful energy from a two-phase geothermal brine produced from a subterranean geothermal reservoir, containing non-condensible gases, including hydrogen sulfide and carbon dioxide, and also containing heavy and/or transition metals in solution, which comprises: (a) separating steam and said non-condensible gases from said produced geothermal brine; (b) flashing a portion of said produced geothermal brine to a high quality steam; (c) separating said high quality steam from the produced geothermal brine; (d) deriving useful energy from said high quality steam; (e) cooling said steam and non-condensible gases separated from said produced geothermal brine in step (a) thereby condensing a portion of the steam; (f) separating said condensed portion from said non-condensible gases and uncondensed steam; (g) contacting said non-condensible gases and uncondensed steam with a scrubber liquid thereby removing deleterious brine constituents and a portion of the hydrogen sulfide from said separated non-condensible gases and uncondensed steam; (h) catalytically converting substantially all the hydrogen sulfide present in said separated non-condensible gases and uncondensed steam to sulfur dioxide, thereby forming a product gas containing sulfur dioxide and carbon dioxide; (i) mixing said condensed portion and said scrubber liquid containing deleterious brine constituents to form a liquid mixture containing hydrogen sulfide; (j) adding the liquid mixture formed in step (i) to a selected portion of said product gas having a stiochiometric excess of sulfur dioxide; (k) adding the mixture formed in step (j) to the remaining produced geothermal brine from step (c); (l) injecting the mixture formed in step (k) into said subterranean geothermal reservoir, said portion of said product gas being selected to provide a sufficient carbon dioxide partial pressure in the injected mixture to substantially eliminate carbonate scaling during injection thereof.

Claim 30

A process for treating and deriving useful energy from a two-phase geothermal brine produced from a subterranean geothermal reservoir, containing non-condensible gases, including hydrogen sulfide and carbon dioxide, and also containing heavy and/or transition metals in solution, which comprises: (a) separating steam and said non-condensible gases from said produced geothermal brine; (b) flashing a portion of said produced geothermal brine to a high quality steam; (c) separating said high quality steam from the produced geothermal brine; (d) deriving useful energy from said high quality steam; (e) cooling said steam and non-condensible gases separated from said produced geothermal brine in step (a) thereby condensing a portion of the steam; (f) separating said condensed portion from said non-condensible gases and uncondensed steam; (g) contacting said non-condensible gases and uncondensed steam with a scrubber liquid thereby removing deleterious brine constituents and a portion of the hydrogen sulfide from said separated non-condensible gases and uncondensed steam; (h) catalytically converting substantially all the hydrogen sulfide present in said separated non-condensible gases and uncondensed steam to sulfur dioxide, thereby forming a product gas containing sulfur dioxide and carbon dioxide; (i) mixing said condensed portion and said scrubber liquid containing deleterious brine constituents to form a liquid mixture containing hydrogen sulfide; (j) adding the liquid mixture formed in step (i) to a selected portion of said product gas having a stiochiometric excess of sulfur dioxide; (k) adding the mixture formed in step (j) to the remaining produced geothermal brine from step (c); (l) injecting the mixture formed in step (k) into said subterranean geothermal reservoir, said portion of said product gas being selected to provide a sufficient carbon dioxide partial pressure in the injected mixture to substantially eliminate carbonate scaling during injection thereof.

Claim 31

The process defined in claim 26 wherein said produced geothermal brine further contains silica in solution and said produced geothermal brine and mixtures therewith are maintained at a temperature above the temperature required to maintain silica in solution.