Method for removal of recalcitrant selenium species from wastewater

Patent metadata

Field	Value
Publication number	US-11084743-B2
Application number	US-201615769289-A
Country	US
Kind code	B2
Filing date	Oct 20, 2016
Priority date	Oct 21, 2015
Publication date	Aug 10, 2021
Grant date	Aug 10, 2021

Abstract

Methods and systems for reducing the concentration of selenium species in water, particularly water containing recalcitrant selenium species. In the methods and systems, water containing one or more selenium species is treated with permanganate to provide permanganate-treated water, which is then contacted with a zero-valent iron treatment system comprising (a) a reactive solid comprising zero-valent iron and one or more iron oxide minerals in contact therewith and (b) ferrous iron.

First claim

The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:

1. A method for reducing the concentration of selenium species in a water, comprising:
treating a water comprising one or more selenium species that are not reducible by treatment with zero-valent iron, with permanganate in a first vessel that does not include zero-valent iron to convert the one or more selenium species that are not reducible by treatment with zero-valent iron to one or more selenium species that are reducible by treatment with zero-valent iron; and
transferring the one or more selenium species that are reducible by treatment with zero-valent iron to a second vessel; and
contacting the one or more selenium species that are reducible by treatment with zero-valent iron with a zero-valent iron treatment system in a second vessel, wherein the zero-valent iron treatment system comprises (a) a reactive solid comprising zero-valent iron and one or more iron oxide minerals in contact therewith and (b) ferrous iron, whereby the concentration of the one or more selenium species that are not reducible by treatment with zero-valent iron in the water is decreased.

2. The method of claim 1 , wherein the concentration of permanganate is from about 5 to about 100 mg/L.

3. The method of claim 1 , wherein the permanganate is potassium permanganate.

4. The method of claim 1 , wherein the one or more selenium species that are not reducible by treatment with zero-valent iron are selected from the group consisting of selenite (Se 4+ ), and selenide (Se −2 ) species, and mixtures thereof.

5. The method of claim 1 , wherein the one or more selenium species that are not reducible by treatment with zero-valent iron are selected from the group consisting of selenite, selenocyanate, selenomethionine, and methylselenic acid.

6. The method of claim 1 , wherein the the reduction in the concentration of selenium species is measured by a decrease in total selenium.

7. The method of claim 1 , wherein the concentration of permanganate in the first vessel is maintained at about 1 to about 100 mg/L.

8. The method of claim 1 , wherein contacting the one or more selenium species that are not reducible by treatment with zero-valent iron with a zero-valent iron treatment system occurs in a first reactor.

9. The method of claim 8 , wherein the first reactor is a packed bed or a fluidized bed.

10. The method of claim 8 , wherein the ferrous iron is continuously introduced to the first reactor.

11. The method of claim 1 , wherein the water further comprises a contaminant selected from arsenic, aluminum, antimony, beryllium, cobalt, lead, cadmium, chromium, silver, zinc, nickel, molybdenum, thallium, vanadium, and ions and oxyanions thereof; borates, nitrates, bromates, iodates, and periodates; trichloroethylene; dissolved silica; and mixtures thereof.

12. The method of claim 1 , wherein the water further comprises an oxyanion, a chlorinated organic compound, or mixtures thereof.

13. The method of claim 1 , wherein the water is selected from flue gas desulfurization wastewater, industrial waste stream, oil refinery waste, tail water of a mining operation, stripped sour water, surface water, ground water, and an influent stream.

14. The method of claim 1 , wherein the water is flue gas desulfurization wastewater.

15. The method of claim 1 , wherein the one or more iron oxide minerals of the reactive solid comprise magnetite.

16. The method of claim 1 , wherein the reactive solid comprises a plurality of particles.

17. The method of claim 1 , wherein the method does not include introducing air or oxygen (aeration) to the water containing the selenium species either in the permanganate treatment step or the zero-valent iron treatment step.

18. In a method for reducing the concentration of selenium species in a water comprising one or more selenium species that are not reducible by treatment with zero-valent iron involving contacting the water with a zero-valent iron treatment system comprising (a) a reactive solid comprising zero-valent iron and one or more iron oxide minerals in contact therewith and (b) ferrous iron, the improvement comprising treating the water comprising one or more selenium species that are not reducible by treatment with zero-valent iron with permanganate in a first vessel prior to contacting the water comprising one or more selenium species that are reducible by treatment with zero-valent iron produced in the first vessel with the zero-valent iron treatment system in a second vessel.

19. A system for reducing the concentration of one or more selenium species in water, comprising:
a first vessel for receiving water comprising one or more selenium species that are not reducible by treatment with zero-valent iron, wherein the first vessel comprises aqueous permanganate and does not comprise zero-valent iron; and
a first reactor in fluid communication with the first vessel for receiving permanganate-treated water from the first vessel, wherein the first reactor comprises a zero-valent iron treatment system comprising (a) a reactive solid comprising zero-valent iron and one or more iron oxide minerals in contact therewith and (b) ferrous iron.

Assignees

• Texas A & M Univ Sys
• Texas A&M Univ System

Inventors

• Huang Yongheng

Classifications

• C02F2103/10

  from quarries or from mining activities · CPC title

• C02F2103/18

  from the purification of gaseous effluents · CPC title

• C02F1/72

  by oxidation {(C02F1/4672 takes precedence)} · CPC title

• C02F2101/106

  Selenium compounds · CPC title

• C02F1/705 Primary

  Reduction by metals · CPC title