METHODS OF SEAWATER SOFTENING FOR DESALINATION AND MINERAL EXTRACTION
Disclosed are methods for seawater softening for the desalination plants (thermal and membrane) by using the carbon mineralization (CM) technique. Disclosed are several process flow diagrams in which the carbon mineralization is integrated at the upstream and/or downstream of the thermal and membrane desalination processes. By using these methods, the released CO2 from industrial factories, seawater feed minerals solutes shall be removed to improve the performance of the desalination plants. Most importantly, valuable products such as Ca/Mg carbonates and BaSO4, which are being used in building rocks, concrete, cement, paints, plastic, etc., can be produced.
1 . A method of sea water softening comprising:
adding buffer solution (NaOH) to sea water to elevate its alkalinity up to pH 10,
mixing flue gas with sucked non-condensable gases from thermal desalination unit,
bubbling in a reactor to produce carbonates and sulfates by precipitation,
washing the precipitate, and
filtering and drying the precipitate to yield valuable mineral product,
wherein processed filtered saline water, free from most of divalent ions, is directed to a thermal desalination unit for producing fresh water and brine,
wherein rejected brine from the desalination unit is partially recycled as feedstock, and at least a portion is blow down and at least a portion is utilized in brine crystallizer to achieve zero liquid discharge.
2 . The method of claim 1 , wherein the carbonates produced are at least one of CaCO3, MgCO3, Na2CO3, BaCO3.
3 . The method of claim 1 , the crystallizer is a mechanical vapor compression system.
4 . The method of claim 1 , wherein the crystallizer is BaCl2.
5 . The method of claim 1 , wherein the first step is precipitating the sulfates through chemical precipitation.
6 . A method of sea water softening comprising:
adding buffer solution (NaOH) to sea water to elevate its alkalinity up to pH 10,
mixing flue gas with sucked non-condensable gases from thermal desalination unit,
bubbling in a reactor to produce carbonates and sulfates by precipitation,
washing the precipitate, and
filtering and drying the precipitate to yield valuable mineral product,
wherein processed filtered saline water, free from most of divalent ions, is directed to membrane-based desalination unit (Reverse Osmosis) for producing fresh water and brine,
wherein the rejected brine from desalination unit is partially recycled as feedstock, and at least a portion is blow down and at least a portion is utilized in brine crystallizer to achieve zero liquid discharge.
7 . The method of claim 6 , wherein the carbonates produced are at least one of CaCO3, MgCO3, Na2CO3, BaCO3.
8 . The method of claim 6 , wherein the crystallizer is a mechanical vapor compression system.
9 . The method of claim 6 , wherein the crystallizer is BaCl2.
10 . The method of claim 6 , wherein the feed water should be filtered first to remove sediments, marine life, and solids.
11 . The method of claim 1 , wherein the method is performed at a top brine temperature at or above 65 degrees Celsius.
12 . The method of claim 1 , wherein the flue gas originates from at least one of exhaust of diesel engines, industrial plants, and desalination plants.
13 . The method of claim 6 , wherein the flue gas originates from at least one of exhaust of diesel engines, industrial plants, and desalination plants.
14 . The method of claim 1 , wherein the sulfate precipitated is BaSO4.
15 . The method of claim 6 , wherein the sulfate precipitated is BaSO4.
16 . The method of claim 6 , wherein a reduction of specific energy consumption equal to or greater than 27%.