Cooling pond water treatment system
A method of increasing operational efficiency of a power plant includes determining an average rate of accumulation of scale-forming compounds in a cooling water source, directing water from the cooling water source having a first concentration of scale forming compounds through a treatment system to produce a treated water having a lower concentration of scale-forming components than the first concentration by operating the treatment system with operating parameters selected such that a rate of removal of the scale-forming components from the water in the treatment system is greater than the average rate of accumulation of the scale-forming components, directing the treated water back into the cooling water source, and circulating water including the treated water from the cooling water source through a cooling system of the power plant.
1. A method of increasing operational efficiency of a power plant, the method comprising:
determining an average rate of accumulation of scale-forming compounds in a cooling water source;
directing water from the cooling water source having a first concentration of scale forming compounds through a treatment system to produce a treated water having a lower concentration of scale-forming components than the first concentration by operating the treatment system with operating parameters selected such that a rate of removal of the scale-forming components from the water in the treatment system is greater than the average rate of accumulation of the scale-forming components, operating the treatment system including
pretreating the water from the cooling water source in a pretreatment stage configured to produce a pretreated water,
treating the pretreated water in a membrane separation stage configured to separate the pretreated water into permeate and brine, treating the pretreated water in the membrane separation stage includes filtering the pretreated water with an ultrafiltration unit to produce a first filtered water,
backwashing the ultrafiltration unit to produce a backwash waste, and
directing the backwash waste into the cooling water source;
directing the treated water back into the cooling water source; and
circulating water including the treated water from the cooling water source through a cooling system of the power plant.
2. The method of claim 1 , wherein operating the treatment system further comprises:
biologically deactivating biological organisms in the water from the cooling water source in the pretreatment stage;
and
treating the brine in a brine recovery stage configured to separate the brine into the treated water and a reject.
3. The method of claim 2 , wherein pretreating the water from the cooling water source includes adding a biocide to the water from the cooling water source.
4. The method of claim 3 , wherein pretreating the water from the cooling water source further includes adding a pH adjustment agent to the water from the cooling water source.
5. The method of claim 4 , wherein adding the pH adjustment agent to the water from the cooling water source includes adjusting the pH of the water from the cooling water source to a pH of between 6.5 and 7.5.
6. The method of claim 3 , wherein pretreating the water from the cooling water source further includes holding the water from the cooling water source in a storage tank downstream of a point of injection of the biocide for a time sufficient to deactivate substantially all microorganisms that were present in the water from the cooling water source.
7. The method of claim 1 , wherein treating the pretreated water in the membrane separation stage further includes filtering the first filtered water in a first reverse osmosis unit to separate the first filtered water into the permeate and the brine.
8. The method of claim 7 , further comprising adding one or more of a reducing agent, an anti-scaling agent, or a pH adjustment agent to the first filtered water prior to filtering the first filtered water in the first reverse osmosis unit.
9. The method of claim 7 , wherein treating the brine in the brine recovery stage includes filtering the brine in a second reverse osmosis unit to produce the treated water and the reject.
10. The method of claim 2 , wherein treating the brine in the brine recovery stage includes filtering the brine in a reverse osmosis unit to produce the treated water and the reject.
11. The method of claim 10 , further comprising adding a biocide to the brine prior to filtering the brine in the reverse osmosis unit.
12. The method of claim 11 , further comprising holding the brine in a storage tank downstream of a point of injection of the biocide into the brine for a time sufficient to deactivate substantially all microorganisms that were present in the brine.
13. The method of claim 10 , further comprising adding one or more of a reducing agent, an anti-scaling agent, or a pH adjustment agent to the brine prior to filtering the brine in the reverse osmosis unit.
14. The method of claim 2 , wherein treating the brine in the brine recovery stage includes separating the brine into the treated water and the reject in an electrically driven separation apparatus.
15. The method of claim 14 , wherein treating the brine in a brine recovery stage includes separating the brine into the treated water and the reject in one of an electrodialysis system or an electrodialysis reversal system.
16. The method of claim 14 , further comprising adding a biocide to the brine prior to separating the brine into the treated water and the reject in the electrically driven separation apparatus.
17. The method of claim 16 , further comprising holding the brine in a storage tank downstream of a point of injection of the biocide into the brine for a time sufficient to deactivate substantially all microorganisms that were present in the brine.
18. The method of claim 14 , further comprising adding one or more of an anti-scaling agent or a pH adjustment agent to the brine prior to separating the brine into the treated water and the reject in the electrically driven separation apparatus.
19. A method of remediating water having a first concentration of scale-forming compounds from a water source, the method comprising:
pretreating the water from the water source in a pretreatment stage configured to biologically deactivate biological organisms in the water from the water source and produce a pretreated water;
treating the pretreated water in a membrane separation stage configured to separate the pretreated water into permeate and brine, treating the pretreated water in the membrane separation stage including
filtering the pretreated water with an ultrafiltration unit to produce a first filtered water,
backwashing the ultrafiltration unit to produce a backwash waste, and
directing the backwash waste into the water source;
treating the brine in a brine recovery stage configured to separate the brine into a treated water having a lower concentration of scale-forming components than the first concentration and a reject; and
directing the treated water into the water source,
the acts of pretreating the water, treating the pretreated water, and treating the brine being performed at a rate such that a rate of removal of the scale-forming components from the water is greater than the average rate of accumulation of the scale-forming components in the water source.
20. The method of claim 19 , wherein treating the pretreated water in the membrane separation stage further includes
filtering the first filtered water in a reverse osmosis unit to separate the first filtered water into the permeate and the brine.
21. The method of claim 20 , wherein treating the brine in the brine recovery stage includes separating the brine into the treated water and the reject in a second reverse osmosis unit.
22. The method of claim 20 , wherein treating the brine in the brine recovery stage includes separating the brine into the treated water and the reject in one of an electrodialysis system or an electrodialysis reversal system.