Salt production from wastewater
Many processes generate wastewater streams rich in sulfate and chloride. These salt components are traditionally not recovered and are discharged to the environment. The invention recovers pure water for recycle/reuse and simultaneously generates valuable pure salts of NaCl and Na2SO 4 for beneficial reuse, eliminating the waste stream. Process consists of the sequential crystallization of salt products with an intermediate purification step in which a chemical reactant is added to elevate levels of purity. The process is configured to simultaneously achieve zero liquid discharge.
1. A method for salt production from a wastewater stream, comprising:
a) providing a wastewater stream comprising sulfate ions and chloride ions;
b) pretreating the wastewater stream with at least one unit operation selected from the group consisting of hardness removal, silica reduction, alkalinity reduction, total organic carbon reduction, and pH adjustment;
c) feeding the wastewater stream to a first stage crystallizer, thereby precipitating and growing sodium sulfate crystals in a first mother liquor;
d) separating the sodium sulfate crystals from the first mother liquor;
e) collecting the first mother liquor and sending it to a chemical reaction vessel;
f) dosing a reactive chemical to the chemical reaction vessel to remove sulfate ion from solution in the wastewater stream as a precipitated solid and removing the precipitated solid to produce a purified sodium chloride brine, wherein the reactive chemical is selected from the group consisting of Ca(NO 3 ) 2 and Ca(OH) 2 ;
g) sending the purified sodium chloride brine into a second stage crystallizer, thereby precipitating and growing sodium chloride crystals in a second mother liquor; and
h) separating the sodium chloride crystals from the second mother liquor.
2. A method for salt production from a wastewater stream, comprising:
a) providing a wastewater stream comprising sulfate ions and chloride ions;
b) pretreating the wastewater stream with at least one unit operation selected from the group consisting of hardness removal, silica reduction, alkalinity reduction, total organic carbon reduction, and pH adjustment;
c) feeding the wastewater stream to a first stage crystallizer, thereby precipitating and growing sodium sulfate crystals in a first mother liquor;
d) separating the sodium sulfate crystals from the first mother liquor;
e) collecting the first mother liquor and sending it to a chemical reaction vessel;
f) dosing a reactive chemical to the chemical reaction vessel to remove sulfate ion from solution in the wastewater stream as a precipitated solid and removing the precipitated solid to produce a purified sodium chloride brine;
g) sending the purified sodium chloride brine into a second stage crystallizer, thereby precipitating and growing sodium chloride crystals in a second mother liquor;
h) separating the sodium chloride crystals from the second mother liquor; and
i) removing a purge stream from the second stage crystallizer to enhance salt purity.
3. The method of claim 2 , wherein the wastewater stream is a coal to gas wastewater stream.
4. The method of claim 1 , further comprising concentrating the wastewater stream prior to at least one of the pretreatment step and the step of sending the wastewater stream to the chemical reaction vessel.
5. The method of claim 4 , wherein the concentration step includes at least one process selected from the group consisting of membrane concentration and thermal evaporation.
6. The method of claim 1 , wherein said separating steps are conducted by dewatering in a centrifuge.
7. The method of claim 2 , wherein said reactive chemical is selected from the group consisting of CaCl 2 , Ca(NO 3 ) 2 , and Ca(OH) 2 .
8. The method of claim 3 , further comprising recycling water from the second mother liquor into a coal gasification process.
9. The method of claim 2 , further comprising washing and/or drying the sodium sulfate salt, thereby enhancing its purity.
10. The method of claim 2 , further comprising washing and/or drying the sodium chloride salt, thereby enhancing its purity.
11. The method of claim 2 , further comprising processing the purge stream in a processor selected from the group consisting of a mixed-salt crystallizer and a dryer.
12. The method of claim 8 , wherein the coal gasification process and method for salt production operate as a zero liquid discharge system with respect to water.
13. The method of claim 1 , wherein the pretreatment step is a hardness removal step, and wherein the hardness removal step produces a regeneration waste stream from an ion exchanger.
14. The method of claim 13 , wherein the regeneration waste stream comprises CaCl 2 , and wherein said CaCl 2 is recycled as a reactive chemical.
15. The method of claim 1 , comprising evaporating water in the first stage crystallizer with at least one of mechanical vapor compression, steam driven, multiple effect evaporation, and thermo-compressor driven evaporation.
16. The method of claim 5 , wherein the concentrating of the wastewater stream includes nanofiltration that rejects more than 90% of the sulfate ion from the wastewater stream.
17. A method for salt production from a wastewater stream, comprising:
a) providing a wastewater stream comprising sulfate ions and chloride ions;
b) pretreating the wastewater stream;
c) sending the wastewater stream to a chemical reaction vessel;
d) dosing a reactive chemical to the chemical reaction vessel to remove sulfate ion from solution in the wastewater stream as a precipitated solid and removing the precipitated solid to produce a purified sodium chloride brine;
e) sending the purified sodium chloride brine into a crystallizer, thereby precipitating and growing sodium chloride crystals in a mother liquor;
f) separating the sodium chloride crystals from the mother liquor; and
g) removing a purge stream from the crystallizer to enhance salt purity.
18. The method of claim 17 , further comprising concentrating the wastewater stream prior to at least one of the pretreatment step and the step of sending the wastewater stream to the chemical reaction vessel, wherein the concentrating of the wastewater stream includes at least one process selected from the group consisting of membrane concentration and thermal evaporation.
19. The method of claim 18 , wherein the step of pretreating the wastewater stream includes using a nanofiltration that rejects more than 90% of the sulfate ion from the wastewater stream.
20. The method of claim 17 , comprising evaporating water in the crystallizer with at least one of mechanical vapor compression, steam driven, multiple effect evaporation, and thermo-compressor driven evaporation.