Removing sulphur-based contaminants and nitrogen-based contaminants from water streams

Abstract

A small-scale system for removing hydrogen sulfide and ammonia from a wastewater stream includes a sulfur recovery stage, an ammonia recovery stage, and a separation stage. Sulfur species are oxidized and converted into solid sulfur and solid sulfur species by exposure to a combination of chelated iron and oxidizer. The solid sulfur and solid sulfur species are removed by filtration to yield a sulfur-free stream to which oxidizer is added and electromagnetic radiation is inputted to break the N—H bonds of the ammonia into amine radicals. The combination of additional oxidizer and electromagnetic radiation promotes the creation of water and nitrogen gas.

Claims

1. A method comprising: converting sulfur species that are present in a wastewater stream into at least one of solid sulfur and solid sulfur species, comprising the steps of: introducing chelated iron to the wastewater stream; and introducing an oxidizer to the wastewater stream; removing at least one of solid sulfur and solid sulfur species from the wastewater stream, thereby creating a sulfur-free stream; emitting electromagnetic radiation into the sulfur-free stream; and introducing additional oxidizer to the sulfur-free stream.

2. The method of claim 1 comprising the further step of separating the sulfur-free stream into phases.

3. The method of claim 2 comprising removing nitrogen gas in a separated gaseous phase.

4. The method of claim 3 comprising removing iron precipitate in a separated solid phase.

5. The method of claim 3 comprising removing elemental sulfur in a separated solid phase.

6. The method of claim 5 comprising removing sweet water in a separated aqueous phase.

7. The method of claim 1 wherein emitting electromagnetic radiation into the sulfur-free stream comprises emitting microwave radiation into the sulfur-free stream.

8. The method of claim 1 wherein emitting electromagnetic radiation into the sulfur-free stream comprises emitting ultraviolet radiation into the sulfur-free stream.

9. The method of claim 1 wherein introducing chelated iron to the wastewater stream comprises introducing one or more of ferric salts, ferrous salts, ferric chelants, and ferrous chelants.

10. The method of claim 1 wherein introducing chelated iron to the wastewater stream comprises introducing Alanine, n,n-bid, (carboxymethyl) iron complex.

11. A method comprising: converting sulfur species that are present in a wastewater stream into at least one of solid sulfur and solid sulfur species via oxidation, comprising the steps of: introducing chelated iron to the wastewater stream; and introducing an oxidizer to the wastewater stream; removing the at least one of solid sulfur and solid sulfur species from the wastewater stream, thereby creating a sulfur-free stream; emitting electromagnetic radiation into the sulfur-free stream; introducing additional oxidizer to the sulfur-free stream; separating the sulfur-free stream into phases; and separating the sweet water as an aqueous phase.

12. The method of claim 11 wherein emitting electromagnetic radiation comprises emitting microwave radiation.

13. The method of claim 11 wherein emitting electromagnetic radiation comprises emitting ultraviolet radiation.

14. The method of claim 11 wherein introducing chelated iron to the wastewater stream comprises introducing one or more of ferric salts, ferrous salts, ferric chelants, and ferrous chelants.

15. The method of claim 11 wherein introducing chelated iron to the wastewater stream comprises introducing Alanine, n,n-bid, (carboxymethyl) iron complex.

Description

BRIEF DESCRIPTION OF THE FIGURES

(1) FIG. 1 illustrates a process for removal of contaminants from wastewater streams associated with oil and gas wells.

(2) FIG. 2 illustrates an apparatus for removal of contaminants from wastewater streams associated with oil and gas wells.

DETAILED DESCRIPTION

(3) FIG. 1 illustrates a process for removing contaminants such as hydrogen sulfide and ammonia from a sour water stream 100 that has been separated from a product stream 101 from a raw natural gas or crude oil well 99. Although the process is described and illustrated in the context of oil and gas production, wastewater that contains sulfur-based and hydrogen-based contaminants from a wide variety of sources other than sour water from oil and gas wells could be treated. For example, and without limitation, the process might be used to treat leachate from landfills and discharge wastewater from meat production facilities. Consequently, the invention should not be viewed as limited to treatment of sour water from oil and gas production. The process for removing the contaminants from a wastewater stream includes three stages: sulfur recovery 102; ammonia recovery 104; and separation 106. The order in which steps are performed at each stage may be rearranged, and some steps may be implemented partially or wholly concurrently.

(4) The sulfur recovery stage 102 includes various steps for treating hydrogen sulfide by separating and recovering sulfur from the sour water stream 100. Step 108 is converting sulfur species that are present in the sour water stream into solid sulfur, which may include elemental sulfur, sulfur species, or both. The converted stream is separated into solid and aqueous phases and the separated converted solids are removed in step 115, such as by filtering, which results in recovery of solid sulfur 128 in the form of elemental sulfur, sulfur species, or both from the sour water stream. The remaining aqueous phase is a sulfur-free stream 116, where “sulfur-free” means that the aqueous phase of the stream has a sufficiently low concentration of sulfur that the ammonia removal stage 104 is not inhibited. For context, and without limitation, the sulfur-free stream 116 may contain 30 parts per million or less of sulfur, by weight, in the aqueous phase.

(5) To convert the sulfur species in step 109, a chelated iron reagent is introduced to the sour water stream in step 110. The pH of the sour water stream is strongly influenced by the presence of ammonia, a strong base, and the reagent should be effective at the pH of the sour water stream. Reagents may include one or more of ferric salts, ferrous salts, ferric chelants, ferrous chelants, and Fe-MGDA (ferric/ferrous methylglycinediacetate), e.g. Alanine, n,n-bid, (carboxymethyl) iron complex (CAS 547763-83-7). Step 112 includes addition of one or more oxidizers to the sour water stream. A wide variety of oxidizers may be used, including but not limited to one or more of chlorine, hypochlorous acid, hypochlorite, chlorine dioxide, chlorite, perchlorate, inorganic peroxides, permanganates, sodium, oxygen, and ozone. In some implementations, oxygen and/or peroxides are used as the oxidizer and the oxygen is provided by ambient air. The hydrogen sulfide in the sour water stream is oxidized into elemental sulfur, sulfur species, or both by exposure to the combination of chelated iron and oxidizer. The stream is then separated into a solid phase and an aqueous phase in step 114 and the solids are removed in step 115 as described above.

(6) The ammonia recovery stage 104 may include various steps for separating and recovering ammonia from the sulfur-free stream 116. Step 118 is introducing electromagnetic radiation. The electromagnetic radiation may be introduced in the form of UV (Ultraviolet) light, microwave radiation, or both. The electromagnetic radiation breaks the N—H bonds of the ammonia in the sulfur-free stream into amine radicals. Step 119 is introducing one or more oxidizers. A wide variety of oxidizers may be used, including but not limited to one or more of chlorine, hypochlorous acid, hypochlorite, chlorine dioxide, chlorite, perchlorate, inorganic peroxides, permanganates, sodium, oxygen, and ozone. The oxidizer or oxidizers may be, but are not necessarily, from the same source as the oxidizers described in step 114, i.e. more of the same oxidizer or oxidizers may be added. In some implementations, hypochlorite is used in the presence of a catalyst and the electromagnetic radiation to oxidize the ammonia to amines and then to nitrogen gas. Thus, the combination of oxidizers and electromagnetic radiation promote the creation of water and nitrogen gas.

(7) In the separation stage 106 the output stream from the ammonia recovery stage is separated into phases as indicated in step 120. More specifically, the stream is separated into one or more of the following distinct phases: aqueous phase, oil phase, gaseous phase, and solid phase. The aqueous phase is sweet water 122 that is sulfur-free and ammonia-free in accordance with government regulatory standards. The gaseous phase includes nitrogen gas 124 in the form of gaseous nitrogen and nitrogen species that are easily removed by processes further downstream. The other phases may include iron precipitate 126 and sulfur 128 in the form of elemental sulfur, sulfur species, or both.

(8) FIG. 2 illustrates an apparatus for removal of contaminants from sour water streams associated with oil and gas wells. The apparatus includes a hydrogen sulfide abatement container 200, an ammonia abatement container 202, and a separation unit 204. Sour water 206, chelated iron 208, and oxidizer 210 are introduced to the hydrogen abatement container 200. The hydrogen sulfide in the sour water stream is oxidized into elemental sulfur, sulfur species, or both by exposure to the chelated iron and oxidizer. An agitator may be used to facilitate exposure of the sour water to the chelated iron and oxidizer. A filter 212 may be used to separate the solid phase 213 from the aqueous phase 215. The separated solid phase includes the sulfur 128 (elemental and/or sulfur species). The remaining aqueous phase 215 is a sulfur-free stream.

(9) Additional oxidizer 210 is introduced to the sulfur-free stream 116, and the resulting stream is introduced to the ammonia abatement container 202. The ammonia abatement container includes at least one electromagnetic radiation source 216. The electromagnetic radiation source, which may generate UV and/or microwave radiation, may include one or more of a sodium vapor lamp, a mercury vapor lamp, a metal arc lamp, a vacuum tube, a solid state UV source, a light-emitting diode, a metal halide lamp, and a solid state microwave source. The electromagnetic radiation breaks the N—H bonds of the ammonia into amine radicals while the oxidizer promotes the creation of water and nitrogen gas.

(10) The resulting stream is provided to a separation unit 204, which separates the stream into one or more of an aqueous phase, oil phase, gaseous phase, and solid phase. The aqueous phase is sweet water 122 that is sulfur-free and ammonia-free in accordance with government regulatory standards. The gaseous phase may include nitrogen gas 124 (including gaseous nitrogen species and/or nitrogen species that are easily removed by processes further downstream). The other phases may include iron precipitate 126 and elemental sulfur 128.

(11) Several features, aspects, embodiments, and implementations have been described. Nevertheless, it will be understood that a wide variety of modifications and combinations may be made without departing from the scope of the inventive concepts described herein. Accordingly, those modifications and combinations are within the scope of the following claims.