Saline wastewater treatment system using solar-assisted heat pump
US-2024083794-A1 · Mar 14, 2024 · US
US9725341B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9725341-B2 |
| Application number | US-201213468784-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 10, 2012 |
| Priority date | May 10, 2011 |
| Publication date | Aug 8, 2017 |
| Grant date | Aug 8, 2017 |
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Methods for removing one or more contaminants from an aqueous stream comprising: adding one or more hydraulic binders and one or more promoters to the aqueous stream, and separating the contaminants from the aqueous stream are provided. The methods may be used for removing contaminants that are arsenic-based, selenium-based, cadmium-based, zinc-based, mercury-based, iron-based, chromium-based and/or phosphate-based.
Opening claim text (preview).
We claim: 1. A method for removing one or more contaminants from an aqueous stream comprising: a) adding one or more hydraulic binders and one or more nucleophilic promoters to the aqueous stream; b) allowing the one or more hydraulic binders, the one or more promoters and the one or more contaminants to interact to form solidified contaminants; and c) separating the solidified contaminants from the aqueous stream; wherein the one or more nucleophilic promoters are selected from the group consisting of elemental sulfur, nitriles, organophosphines, and ethers; and wherein the one or more hydraulic binders are added to the aqueous stream in the form of a powder mixture; wherein the aqueous stream is selected from the group consisting of drinking water, ground water, well water, surface water, agricultural waters, wastewater from mining processes, geothermal fluids, water from mining processes associated with smelting, mine dewatering, tailing impoundment treatment, flotation, autoclave, acid mine drainage, wastewater from flue gas, desulfurization units, runoff from wet fly ash ponds, and groundwater streams; and wherein the dosage of the one or more hydraulic binders added to the aqueous stream is about 10 ppm to about 50,000 ppm. 2. The method of claim 1 , wherein the one or more contaminants are selected from the group consisting of mercury, cadmium, zinc, manganese, lead, copper, chromium, molybdenum, gallium, indium, thallium, other metal contaminants, including the various oxidation states of these metals and compounds comprising these metals. 3. The method of claim 1 , wherein the one or more contaminants are selected from the group consisting of antimony, arsenic, selenium, phosphates, other non-metallic contaminants, and compounds comprising arsenic, selenium, phosphates, including the various oxidation states of these non-metals and compounds comprising these non-metals. 4. The method of claim 1 , wherein the one or more contaminants comprise arsenic-based, selenium-based, cadmium-based, zinc-based, mercury-based, iron-based, chromium-based and/or phosphate-based contaminants. 5. The method of claim 1 , wherein the one or more hydraulic binders are selected from the group consisting of hydraulic lime, naturally occurring cements, pozzolana cements, gypsum cements, phosphate cements, high alumina cements, slag cements, cement kiln dust, silica cements, high alkalinity cements, Portland cements and combinations thereof. 6. The method of claim 1 , wherein the one or more nucleophilic promoters is elemental sulfur. 7. The method of claim 1 , wherein the aqueous stream is selected from wastewater from flue gas, desulfurization units, runoff from wet fly ash ponds, and groundwater streams. 8. The method of claim 1 , wherein the separation step is accomplished by gravity settling, filtration, or another mechanical separation method. 9. The method of claim 1 , wherein the method further comprises stirring or agitating the aqueous stream after the one or more hydraulic binders and one or more nucleophilic promoters have been added. 10. The method of claim 1 , wherein the one or more hydraulic binders and one or more nucleophilic promoters are premixed before being added to the aqueous stream. 11. The method of claim 10 , wherein the one or more hydraulic binders and one or more nucleophilic promoters are added as a dry blend. 12. The method of claim 10 , wherein the one or more hydraulic binders and one or more nucleophilic promoters are added as a dispersion. 13. The method of claim 1 , wherein the method further comprises adding a flocculant. 14. The method of claim 1 , wherein the aqueous stream is selected from the group consisting of wastewater from mining processes, water from mining processes associated with smelting, mine dewatering, tailing impoundment treatment, and acid mine drainage. 15. The method of claim 1 , wherein the one or more contaminants are removed from the aqueous stream to below about 2.0 ppb. 16. The method of claim 1 , wherein the aqueous stream is not contaminated sludge.
Iron or iron compound · CPC title
Chromium or chromium compounds, e.g. chromates · CPC title
Processes for the treatment of water whereby the filtration technique is of importance (C02F1/44 takes precedence; construction of filters in general B01D24/00 - B01D41/00) · CPC title
Selenium compounds · CPC title
Sludge treatment by fixation or solidification · CPC title
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