Method and system for treating wastewater
Treating brine to produce distilled water and dried NaCl. The brine enters a crystallization plant and is heated. Once heated, the brine is circulated to an evaporator. The evaporator increases the concentration of NaCl in the brine to a point about the super saturation level. Once above the super saturation level, NaCl crystals are formed. The larger crystals are circulated to a centrifuge for drying and the smaller crystals are recirculated through the evaporator for continued growth. The NaCl crystals are dried in the centrifuge.
1. A method for treating wastewater comprising:
receiving wastewater;
screening the received wastewater, said screening comprising:
determining a concentration of total dissolved solids (“TDS”) in the received wastewater is greater than 150,000 mg/L;
pretreating the screened wastewater, based on the screening, to produce a pretreated wastewater suitable for crystallization/evaporation;
feeding the pretreated wastewater into an evaporation/crystallization unit to produce a distilled water, a concentrated brine comprising CaCl 2 ), and a salt slurry comprising NaCl crystals;
purifying a first portion of the distilled water to produce a purified water therefrom, said purifying comprising:
denitrifying nitrogen compounds in the first portion of the distilled water under anaerobic conditions to produce a denitrified distilled water therefrom;
nitrifying additional nitrogen compounds in the denitrified distilled water under aerobic conditions to produce a nitrified distilled water therefrom; and
introducing the nitrified distilled water to a membrane bioreactor comprising a membrane to remove contaminants therefrom and to thereby arrive at a purified water from the membrane bioreactor; and
converting the purified water into a de-wasted water comprising a chemical oxygen demand (“COD”) of less than or equal to 15 mg/L, a methanol concentration of less than or equal to 3.5 mg/L, a nitrite-nitrate nitrogen concentration of less than or equal to 2 mg/L, substantially no oil, a sodium concentration of less than or equal to 25 mg/L, a TDS concentration of less than or equal to 500 mg/L, and a total suspended solids (“TSS”) concentration of less than or equal to 45 mg/L,
wherein said converting comprises introducing the purified water to at least one of the group consisting of: an ion exchange system and a reverse osmosis system.
2. The method of claim 1 , further comprising:
introducing the salt slurry to a centrifuge;
washing the salt slurry with a second portion of the distilled water; and
dewatering the washed salt slurry in the centrifuge to generate a NaCl product comprising NaCl and a centrate/filtrate.
3. The method of claim 2 , further comprising separating the NaCl product from the centrate/filtrate.
4. The method of claim 3 , further comprising routing back to the evaporation/crystallization unit the centrate/filtrate remaining after the NaCl product has been separated.
5. The method of claim 4 , further comprising mixing the centrate/filtrate with the pretreated wastewater as the pretreated wastewater is fed to the evaporation/crystallization unit.
6. The method of claim 1 , wherein the evaporation/crystallization unit produces a vapor comprising water droplets, and further comprising routing the vapor from the evaporation/crystallization unit through a demister to remove the water droplets from the vapor.
7. The method of claim 6 , further comprising compressing the vapor to produce a compressed vapor.
8. The method of claim 1 , wherein the step of screening the received wastewater further comprises determining a concentration of methanol in the received wastewater is greater than 500 mg/L, and the method further comprises:
removing methanol from the screened wastewater, prior to said pretreating the screened wastewater.
9. The method of claim 8 , wherein the step of removing methanol comprises processing the screened wastewater in a rectification column.
10. The method of claim 1 , wherein the step of screening the received wastewater further comprises determining that the received wastewater is not substantially free of oil, and the method further comprises:
removing oil from the screened wastewater, prior to said pretreating the screened wastewater.
11. The method of claim 1 , further comprising:
introducing the concentrated brine to a second stage thermal mechanical evaporation/crystallization unit to generate a high-purity CaCl 2 product.
12. The method of claim 11 further comprising removing lithium from the concentrated brine before introducing the concentrated brine to the second stage thermal mechanical evaporation/crystallization unit.
13. The method of claim 12 , wherein the second stage thermal mechanical evaporation/crystallization unit further generates solid crystals comprising one or more of: barium chloride crystals and additional sodium chloride crystals.