High efficiency ion exchange system for removing contaminants from water
View Patent ↗The disclosed invention is a fixed bed ion exchange water purification system. It employs a combination of electronically controlled process steps and specific systems configurations to duplicate the effects of moving resin beds from one operating position to another as is required in moving bed ion exchange water purification systems. The invention combines features of single fixed bed ion exchange systems with those of a moving bed system. The invention applies to the treatment of water having typical industrial and drinking water concentrations of various ions.
1. A process for continuously removing nitrate ion contaminant from nitrate ion-contaminated water comprising:
with a controller, feeding said contaminated water through a first manifold to individually-valved first headers each directly adjacent to a first opening into each of a first subset of a plurality of immobile vessels, each containing between said first opening and a second opening an ion exchange resin bed capable of binding nitrate contaminant from the contaminated water and yielding reduced nitrate level water and a nitrate-contaminated resin bed,
with a controller, removing reduced nitrate level water through the second opening from each of the vessels in the first subset, and passing said reduced nitrate level water through a second individually-valved header directly adjacent to the second opening and through a second manifold to a reduced nitrate level water discharge;
with a controller, feeding regenerant solution to an individually-valved header directly adjacent to a first or second opening on one or more additional vessels making up a second subset of the plurality each such vessel containing a nitrate-contaminated resin bed,
with a controller, passing the regenerant solution over the nitrate-contaminated resin bed so that the regenerant displaces the nitrate contaminants off of the nitrate-contaminated resin bed to yield a regenerated resin bed and spent regenerant solution which is removed from the other opening on the vessel and through another individually-valved header directly adjacent to this opening,
with a controller, feeding rinse water to an individually-valved header directly adjacent to a first or second opening on one or more additional vessels making up a third subset of the plurality each such vessel containing a regenerated resin bed, and
with a controller, passing the rinse water over the regenerated resin bed to yield a rinsed, regenerated resin bed and used rinse water which is removed from the other opening on the vessel and through the individually-valved header directly adjacent to this opening.
2. The process of claim 1 further comprising the step of with a controller, periodically redirecting the valves to the individually-valved headers connected to one or more of the first subset of vessels to halt the flow of contaminated and reduced nitrate level water to said one or more of the first subset of vessels and to start the flow of regenerant solution and spent regenerant solution, thereby placing said one or more vessels from the first subset into the second subset of vessels.
3. The process of claim 2 further comprising the step of with a controller, periodically redirecting the valves to the individually-valved headers connected to one or more of the second subset of vessels to halt the flow of regenerant solution and spent regenerant solution and to start the flow of rinse water and used rinse water, thereby placing said one or more vessels from the second subset into the third subset of vessels.
4. The process of claim 3 further comprising the step of with a controller, periodically redirecting the valves to the individually valved headers connected to one or more of the third subset of vessels to halt the flow of rinse water and used rinse water and start the flow of contaminated and reduced nitrate level water, thereby placing said one or more vessels from the third subset into the first subset of vessels.
5. The process of claim 4 wherein the immobile vessels are vertically oriented with their first openings above the resin beds and their second openings below the resin beds such that the flows of water and regenerant solution are downflow through the vessels and the flow of rinse water is upflow.
6. The process of claim 5 wherein the plurality of vessels is at least ten vessels and wherein the first subset of vessels is at least about one half of the plurality of vessels.
7. The process of claim 6 wherein the regenerant solution is a brine solution.
8. The process of claim 1 further comprising the step of with a controller, periodically redirecting the valves to the individually-valved headers connected to one or more of the second subset of vessels to halt the flow of regenerant solution and spent regenerant solution and to start the flow of rinse water and used rinse water, thereby placing said one or more vessels from the second subset into the third subset of vessels.
9. The process of claim 1 further comprising the step of with a controller, periodically redirecting the valves to the individually-valved headers connected to one or more of the third subset of vessels to halt the flow of rinse water and used rinse water and start the flow of nitrate ion-contaminated and said reduced nitrate level water, thereby placing said one or more vessels from the third subset into the first subset of vessels.
10. A process for continuously removing nitrate contaminant from nitrate-contaminated water comprising:
a) with a controller continuously feeding nitrate contaminated water through a first manifold to individually-valved first headers each directly adjacent to a first opening into each of a first subset of a plurality of immobile vessels, each containing between said first opening and a second opening an ion exchange resin bed capable of binding nitrate contaminant from the nitrate contaminated water and yielding reduced nitrate level water and a nitrate contaminated resin bed, the vessels in said first subset having been in service for varying periods of time and thus having varying degrees of nitrate contamination of their resin beds,
b) with a controller continuously removing reduced nitrate level water through the second opening from each of the vessels in the first subset, and passing said reduced nitrate level water through a second individually-valved header directly adjacent to the second opening and through a second manifold to a reduced nitrate level water discharge,
c) with a controller periodically halting the feeding of step a) and the removing of step b) to and from the vessel in the first subset of vessels having the most highly nitrate contaminated resin bed thereby withdrawing that vessel from purification service,
d) with a controller feeding regenerant solution to an individually-valved header directly adjacent to an opening on the vessel withdrawn from service in step c) and passing the regenerant solution over the nitrate-contaminated resin bed so that the regenerant displaces the nitrate contaminants off of the nitrate-contaminated resin bed to yield a regenerated resin bed and spent regenerant solution,
e) with a controller removing spent regenerant solution from another opening on the vessel and through an individually-valved header directly adjacent to this opening,
f) with a controller halting the feeding of step d) and the removing of step e) once a desired degree of regeneration has been attained thereby withdrawing that vessel from regeneration service,
g) with a controller feeding rinse water to an individually-valved header directly adjacent to an opening on the vessel withdrawn from service in step f) and passing the rinse water over the regenerated resin bed so that the rinse water displaces regenerant solution from the regenerated resin bed to yield a rinsed regenerated resin bed and used rinse water,
h) with a controller removing used rinse water from another opening on the vessel and through an individually-valved header directly adjacent to this opening, and
i) with a controller halting the feeding of step g) and the removing of step h) once a desired degree of rinsing has been attained.
11. The process of claim 10 additionally comprising the step j) reinstalling the vessel having the rinsed regenerated resin bed produced in step i) in service in the first subset of vessels.
12. The process of claim 11 wherein at least two vessels are undergoing regeneration at the same time with one of these vessels being more completely regenerated than another vessel and wherein fresh regenerant solution is passed over the more regenerated resin bed and thereafter passed in series over the less completely regenerated resin bed.
13. The process of claim 11 wherein at least two vessels are undergoing rinsing at the same time with one of these vessels being more completely rinsed than another vessel and wherein fresh rinse water is passed over the more rinsed resin bed and thereafter passed in series over the less completely rinsed resin bed.
14. The process of claim 11 wherein the immobile vessels are vertically oriented with their first openings above the resin beds and their second openings below the resin beds such that feeding of water to the first subset of vessels is downflow through the resin beds.
15. The process of claim 14 wherein the passing of regenerant solution in step d is downflow.
16. The process of claim 15 wherein the passing of rinse water in step g is upflow.
17. The process of claim 16 wherein the plurality of vessels is at least ten vessels and wherein the first subset of vessels is at least about one half of the plurality of vessels.
18. The process of claim 17 wherein the regenerant solution is a brine solution.
19. The process of claim 18 wherein the contaminant additionally comprises perchlorate.
20. The process of claim 14 wherein the passing of regenerant in step d is upflow.
21. A process for continuously removing nitrate contaminant from nitrate-contaminated water comprising:
a) with a controller continuously feeding nitrate contaminated water downflow through a first manifold to individually-valved first headers each directly adjacent to a first opening into each of a first subset of a plurality of vertical immobile vessels, each containing between said first opening and a second opening an ion exchange resin bed capable of binding nitrate contaminant from the contaminated water and yielding reduced nitrate level water and a nitrate-contaminated resin bed, the vessels in said first subset having been in service for varying periods of time and thus having varying degrees contamination of their resin beds,
b) with a controller continuously removing reduced nitrate level water through the second opening from each of the vessels in the first subset, and passing said reduced nitrate level water through a second individually-valved header directly adjacent to the second opening and through a second manifold to a treated water discharge,
c) with a controller periodically halting the feeding of step a) and the removing of step b) to and from the vessel in the first subset of vessels having the most highly nitrate contaminated resin bed thereby withdrawing that vessel from nitrate removal service,
d) with a controller feeding regenerant brine solution to an individually-valved first header directly adjacent to an opening on the vessel withdrawn from service in step c) and passing the regenerant solution over the nitrate-contaminated resin bed so that the regenerant displaces the nitrate contaminants off of the resin bed to yield a regenerated resin bed and spent regenerant solution containing nitrate,
e) with a controller removing spent regenerant solution from another opening on the vessel and through an individually-valved header directly adjacent to this opening,
f) with a controller halting the feeding of step d) and the removing of step e) once a desired degree of regeneration has been attained thereby withdrawing that vessel from regeneration service,
g) with a controller feeding rinse water to an individually-valved second header directly adjacent to an opening on the vessel withdrawn from service in step f) and passing the rinse water over the regenerated resin bed so that the rinse water displaces regenerant solution from the regenerated resin bed to yield a rinsed regenerated resin bed and used rinse water,
h) with a controller removing used rinse water from another opening on the vessel and through an individually-valved header directly adjacent to this opening, and
i) with a controller halting the feeding of step g) and the removing of step h) once a desired degree of rinsing has been attained, and reinstalling the vessel having the rinsed regenerated resin bed produced in step g) in service in the first subset of vessels.
22. The process of claim 21 wherein at least two vessels are undergoing regeneration at the same time with one of these vessels being more completely regenerated than another vessel and wherein fresh regenerant solution is passed downflow over the more regenerated resin bed and thereafter passed in series over the less completely regenerated resin bed.
23. The process of claim 22 wherein at least two vessels are undergoing rinsing at the same time with one of these vessels being more completely rinsed than another vessel and wherein fresh rinse water is passed over the more rinsed resin bed and thereafter passed in series over the less completely rinsed resin bed.
24. A process for continuously removing nitrate contaminant from nitrate-contaminated water comprising:
a) with a controller continuously feeding nitrate-contaminated water through a first opening of each of a first subset of a plurality of immobile vessels, each containing between said first opening and a second opening a resin bed capable of binding nitrate contaminant from the nitrate-contaminated water and yielding reduced nitrate level water and a nitrate-contaminated resin bed, the vessels in said first subset having been in service for varying periods of time and thus having varying degrees nitrate contamination of their resin beds,
b) with a controller continuously removing reduced nitrate level water through the second opening from each of the vessels in the first subset, and passing said reduced nitrate level water to a reduced nitrate level water discharge,
c) with a controller periodically halting the feeding of step a) and the removing of step b) to and from the vessel in the first subset of vessels having the most highly contaminated resin bed thereby withdrawing that vessel from nitrate removal service,
d) with a controller feeding regenerant brine solution comprising salt and make up water to an opening on the vessel withdrawn from service in step c) and contacting the regenerant solution with the nitrate-contaminated resin bed so that the regenerant displaces the nitrate contaminants off of the nitrate-contaminated resin bed to yield a regenerated resin bed and spent regenerant solution containing nitrate,
e) with a controller removing spent regenerant solution from the vessel
f) with a controller halting the feeding of step d) and the removing of step e) once a desired degree of regeneration has been attained thereby withdrawing that vessel from regeneration service,
g) with a controller feeding rinse water solution to an opening on the vessel withdrawn from regeneration service in step f) and contacting the rinse water solution with the regenerated resin bed so that the rinse water displaces regenerant solution from the regenerated resin bed to yield a rinsed regenerated resin bed and used rinse water,
h) with a controller removing used rinse water from the vessel containing the rinsed regenerated resin bed of step g),
i) with a controller halting the feeding of step g) and the removing of step h) once a desired degree of rinsing has been attained,
j) reinstalling the vessel having the rinsed regenerated resin bed produced in step i) in service in the first subset of vessels, and
k) using the used rinse water removed in step h) as make up water in the regenerant brine solution.
25. The process of claim 24 wherein at least two vessels are undergoing regeneration at the same time with one of these vessels being more completely regenerated than another vessel and wherein fresh regenerant solution is contacted with the more completely regenerated resin bed and thereafter contacted in series with the less completely regenerated resin beds.
26. The process of claim 25 wherein at least two vessels are undergoing rinsing at the same time with one of these vessels being more completely rinsed than another vessel and wherein fresh rinse water is contacted with the more completely rinsed resin bed and thereafter contacted in series with the less completely rinsed resin beds and thereafter used as make up water in the regenerant brine solution.