Integrated selenium removal system for waste water
View Patent ↗The inventive process scheme and its various embodiments described herein will comprise filtering a selenium containing water by reverse osmosis or nanofiltration to produce a primary permeate stream at least meeting the water stream effluent discharge requirements of the location and a concentrate stream containing the removed selenium and other species, a RO or NF concentrate treatment specific to the case which will treat and reduce the selenium content of the concentrate, optionally in conjunction with a sulfate removal process, and result in a highly concentrated sludge or other output, and a selenium depleted aqueous overflow stream, a portion of which will be combined with the primary permeate stream so that the selenium content of the combined stream does not exceed the local requirement, and the reminder of the selenium depleted aqueous overflow stream will be returned to be combined with the selenium containing water entering the inlet of the primary reverse osmosis treatment.
1. An integrated process for removing selenium from a water source containing selenium, the process comprising:
filtering a first water feed stream including water from the water source with a membrane filtration process to produce a first water product stream having a reduced selenium content and a first retentate;
separating sulfate from the first retentate to produce a stream including removed sulfate and an overflow stream depleted in sulfate;
treating the overflow stream to produce a second water product stream having a selenium content less than a selenium content of the first retentate, and a concentrate by metabolically reducing selenium ions in the overflow stream with bacteria under anaerobic conditions;
combining a first portion of the second water product stream with the first water product stream to produce a process effluent having a selenium content less than or equal to a predefined maximal selenium content; and
combining a remaining portion of the second water product stream with the water from the water source to generate the first water feed stream.
2. The process of claim 1 , wherein the membrane filtration process is a reverse osmosis process.
3. The process of claim 1 , wherein the membrane filtration process is a nanofiltration process.
4. The process of claim 1 , wherein treating the overflow stream further includes chemically reducing selenium in the overflow stream by contacting the overflow stream with iron.
5. The process of claim 4 , wherein the iron is steel wool.
6. The process of claim 1 , wherein the minimum ratio of Jp to Jo of the second product stream being combined with the first product stream is defined by the equation
Jp/Jo =( Q−Co )/( Cp−Q )
where;
Jp=first water product stream flow rate
Jo=second water product steam portion combining with Jp
Cp=Se content of the first water product stream
Co=second water product steam portion Se content
Q=maximum design or regulated effluent Se content under the conditions that;
Cp<Q and Co>Q.
7. The process of claim 1 , wherein the minimum ratio of Jo to Jp of the second product stream being combined with the first product stream is defined by the equation
Jo/Jp =( Q−Cp )/( Co−Q )
where;
Jp=first water product stream flow rate
Jo=second water product steam portion combining with Jp
Cp=Se content of the first water product stream
Co=second water product steam portion Se content
Q=maximum design or regulated effluent Se content under the conditions that;
Co<Q and Cp>Q.
8. The process of claim 1 , further comprising adding one or more anti-scalant chemicals to the remaining portion of the second water product stream.
9. The process of claim 1 , further comprising pretreating the water source with a sulfate removal process.
10. The process of claim 1 , wherein separating sulfate from the first retentate includes precipitating sulfate from the first retentate by the addition of lime to the first retentate.
11. The process of claim 10 , wherein the lime is added to the first retentate in a reactor, and the process further comprises precipitating sulfate in a clarifier downstream of the reactor and returning a portion of the precipitated sulfate to the reactor to act as a seed for initiating precipitation of the sulfate.
12. The process of claim 1 , wherein separating sulfate from the first retentate includes removing sulfate from the first retentate by strong acid cation exchange.
13. The method of claim 1 , further comprising treating the remaining portion of the second water product stream with an ion exchange resin prior to combining the remaining portion of the second water product stream with the water from the water source.
14. The process of claim 13 , wherein treating the remaining portion of the second water product stream with the ion exchange resin includes passing the remaining portion of the second water product stream through a strong acid ion exchange resin.
15. The method of claim 13 , further comprising regenerating the ion exchange resin with brine.
16. The method of claim 1 , wherein the predefined maximal selenium content is 5 μg/L.
17. The method of claim 1 , wherein filtering the first water feed stream with the membrane filtration process to produce the first water product stream includes removing more than 95% of the selenium from the first water feed stream.
18. The method of claim 1 , comprising recovering greater than 95% of the water from the water source.
19. An integrated process for removing selenium from a water source containing selenium, the process comprising:
filtering a first water feed stream including water from the water source with a membrane filtration process to produce a first water product stream having a reduced selenium content and a first retentate;
separating sulfate from the first retentate to produce a stream including removed sulfate and an overflow stream depleted in sulfate;
treating the overflow stream to produce a second water product stream having a selenium content less than a selenium content of the first retentate, and a concentrate by one of metabolically reducing selenium ions in the overflow stream with bacteria under anaerobic conditions or chemically reducing selenium in the overflow stream by contacting the overflow stream with iron;
combining a first portion of the second water product stream with the first water product stream to produce a process effluent having a selenium content less than or equal to a predefined maximal selenium content; and
combining a remaining portion of the second water product stream with the water from the water source to generate the first water feed stream.