REDOX WATER TREATMENT METHOD

Abstract

A redox water treatment method comprises first determining the composition of water and whether water treatment requires either oxidation or reduction, or both to optimize nitrogen removal by a bioreactor. Sulfur dioxide (SO.sub.2) is injected into the water to be treated to provide H.sup.+, SO.sub.2, SO.sub.3.sup.=, HSO.sub.3.sup.−, dithionous acid (H.sub.2S.sub.2O.sub.4), and other sulfur intermediate reduction products forming a sulfur dioxide treated water, which behaves either as a reducing agent or an oxidizing agent depending on the strength of the acid concentration, which alters sulfurous acid from a reducing agent to a more powerful oxidizing agent.

Claims

1. A redox water treatment method employing sulfurous acid comprising: a. determining the compounds of interest in water to be treated and whether the compounds require oxidation, reduction, or both, b. injecting sulfur dioxide (SO.sub.2) into the water to be treated to provide H.sup.+, SO.sub.2, SO.sub.3.sup.=2, HSO.sub.3.sup.−, dithionous acid (H.sub.2S.sub.2O.sub.4), and other sulfur intermediate reduction products forming a sulfur dioxide treated water either: i. in the presence of oxygen, air, an oxidizing agent, such as hydrogen peroxide, ferric or ferrous compounds, and additional sulfur dioxide and any other acid to ensure that the electrical conductivity level of the sulfur dioxide treated water is sufficient to accept electrons to create an oxidizing solution to oxidize compounds of interest, or ii. in the presence of no oxygen and without additional other acid added for reduction to occur, but more sulfur dioxide can be added to ensure the electrical conductivity level of the sulfur dioxide treated water is sufficient for release of electrons from the sulfur dioxide, sulfites, bisulfites, and dithionous acid to form a reducing solution to reduce oxidants, disinfect pathogens, acid leach heavy metals from suspended solids into solution, and self-agglomerate suspended solids, and c. adjusting and selectively employing the oxidation reduction potential electrical conductivity levels of the sulfur dioxide treated water required for providing either an oxidizing or reducing solution, or both.

2. A redox water treatment method according to claim 1, including: a. removing and disposing of suspended solids from the reducing solution along with adsorbed polar molecules to produce a filtrate containing heavy metals, and b. raising the pH of the sulfur dioxide treated water with lime to precipitate any heavy metals, which form metal hydroxides for removal and fainting a disinfected demetalized filtrate suitable for biological treatment.

3. A redox water treatment method employing sulfurous acid according to claim 1, including injecting hydrogen peroxide or other oxygen containing compounds into the sulfur dioxide treated water to ensure that the electrical conductivity level of the sulfur dioxide treated water is sufficient to accept electrons to enhance the oxidizing solution.

4. A redox water treatment method according to claim 1, including adding additional sulfites and bisulfites from a different source in addition to that contained in the sulfur dioxide treated water.

5. A redox water treatment method according to claim 1, wherein the electrical conductivity is between −0.37 and -0.14 volt at 25° C. at 1 molal H.sup.+.

6. A redox water treatment method according to claim 1, wherein the additional acid is selected so that cations added do not adversely affect resultant treated water.

7. A redox water treatment method according to claim 1, including raising the pH of the reducing solution to approximately ≧7 to increase sulfite/bisulfate concentrations, and exposing the elevated sulfite/bisulfite reducing solution to at least one activation methods (ultraviolet light, ultrasound, electron beam, and microwaves) and reducing agents (dithionite, sulfite, ferrous iron, and sulfide) to degrade nitrates and perchlorates in solution.

8. A redox water treatment method according to claim 7, including adding a catalyst to the reducing solution to speed degradation.

9. A redox water treatment method comprising: a. determining the ionic and molecular composition of water to be treated for oxidation and reduction, b. injecting sulfur dioxide (SO.sub.2) into water to be treated to provide H.sup.+, SO.sub.2, SO.sub.3.sup.=2, HSO.sub.3.sup.−, dithionous acid (H.sub.2S.sub.2O.sub.4), and other sulfur intermediate reduction products forming a sulfur dioxide treated water in the presence of the amount of oxygen necessary for reduction to occur and no additional other acid is added, but more sulfur dioxide can be added to ensure the electrical conductivity level of the sulfur dioxide treated water is sufficient for release of electrons from the sulfur dioxide, sulfites, bisulfites, and dithionous acid to form a reducing solution to reduce oxidants, disinfect pathogens, acid leach heavy metals from suspended solids into solution, and self-agglomerate suspended solids, and c. removing and disposing of suspended solids from the reducing solution along with adsorbed polar molecules to produce a filtrate containing heavy metals, d. injecting oxygen and other additional acid including more sulfur dioxide into the filtrate to insure that the electrical conductivity level of the sulfur dioxide treated water is sufficient to accept electrons to create an oxidizing solution, and e. raising the pH of the sulfur dioxide treated water with lime to precipitate heavy metals for removal as metal hydroxides to form a disinfected demetalized filtrate suitable for raising crops and biological treatment.

10. A redox water treatment method according to claim 9, including adding lime and/or calcium carbonate to adjust the pH and calcium ion concentration of the discharged brine retentates to provide soil concentrations with a sodium adsorption ratio SAR less than 15, electrical conductivity EC less than 2 dS m.sup.−1 (m mho cm.sup.−1), cation exchange capacity CEC less than 57.5 centimoles/kg, and a pH less than 8.

11. A redox water treatment method according to claim 10, wherein the concentration of sulfurous acid has a pH between 2 and 6.8 for land application to alkaline soils.

12. A redox water treatment method according to claim 1, wherein the sulfurous acid reducing solution has a free SO.sub.2 and bisulfate (HSO.sub.3.sup.−) concentration, a pH level, and a dwell time sufficient to affect disinfection before land application.

13. A redox water treatment method according to claim 9, wherein the oxidizing solution is first raised to a pH level of up to 11 using lime to precipitate any heavy metals, which form metal hydroxides as metal hydroxides for removal, and the resultant metal free filtrate is then pH lowered for raising plants and biological treatment, and providing a soil sodium adsorption ratio SAR level suitable for plant propagation and reduce soil carbonates/bicarbonates to improve water penetration.

14. A redox water treatment method according to claim 1, wherein the water is wastewater containing nitrogen compounds, total suspended solids (TSS), biological oxygen demand compounds (BOD), chemical oxygen demand compounds (COD) undergoing biological nitrogen reduction in a bioreactor, including: a. controlling and monitoring the composition of wastewater or wastewater process streams entering the bioreactor to be treated and whether the wastewater and wastewater process steams require biological nutrient removal under oxidation or reduction conditions, or both, b. injecting sulfur dioxide (SO.sub.2) into the wastewater to be treated to provide H.sup.+, SO.sub.2, SO.sub.3.sup.=, HSO.sub.3.sup.−, dithionous acid (H.sub.2S.sub.2O.sub.4), and other sulfur intermediate reduction products forming a sulfur dioxide treated wastewater with agglomerated suspended solids and acid leached heavy metals in solution, which form either: i. in the presence of oxygen and sufficient acid to insure that the electrical conductivity level of the sulfur dioxide treated wastewater is sufficient to accept electrons to create an oxidizing solution, or ii. in the presence of minimal oxygen and no additional acid to insure the electrical conductivity level of the sulfur dioxide treated wastewater is sufficient for release of electrons from the sulfur dioxide, sulfites, bisulfites, and dithionous acid to form a reducing solution, c. removing the suspended solids forming either an oxidizing or reducing solution filtrate, d. adding lime to the oxidizing or reducing solution filtrate to precipitate heavy metals as metal hydroxides, and phosphates as calcium phosphate precipitates, e. removing metal hydroxides and calcium phosphate precipitates forming a pH adjusted oxidizing or reducing solution second filtrate and transferring the second filtrate to the bioreactor; and f. selectively monitoring and altering the oxidation reduction potential (ORP) of the second filtrate to form either an oxidizing solution or reducing solution, or both in the bioreactor at the oxidation reduction potential (ORP) and dissolved oxygen (DO) level/levels required to stimulate and accelerate biological removal of nitrogen compounds forming a conditioned wastewater.

15. A redox water treatment method according to claim 14, wherein the ORP electrical conductivity is adjusted and held at an mV required for nitrification.

16. A redox water treatment method according to claim 14, wherein after nitrification, the ORP electrical conductivity is adjusted and held at an mV required for denitrification.

17. A redox water treatment method according to claim 14, wherein the second filtrate is treated under oxic or aerobic conditions at an ORP between +50 and +300 mV for nitrification, and an ORP between +50 and −50 mV under anoxic anaerobic conditions for denitrification.

18. A redox water treatment method according to claim 14, wherein the lime added is spent lime, which adds additional carbon if required by denitrifying bacteria.

19. A redox water treatment method according to claim 14, including injecting hydrogen peroxide, oxygen containing compounds, and ferrous compounds into the second filtrate to adjust the electrical conductivity level sufficiently to accept electrons to enhance the oxidizing solution.

20. A redox water treatment method according to claim 19, including adding additional acid to the second filtrate to make a more powerful oxidizing solution.

21. A redox water treatment method according to claim 20, wherein the additional acid for oxidation is selected to provide compatible cations consistent with the discharge needs of an end user.

22. A redox water treatment method according to claim 14, including adding additional sulfites and bisulfites from salts to the second filtrate reducing solution to adjust the electrical conductivity level of the sulfur dioxide treatment wastewater sufficiently to donate electrons to enhance the reducing solution.

23. A redox water treatment method according to claim 1, including adding lime and calcium carbonate to adjust the pH and calcium ion concentration of the conditioned wastewater for land application to provide soil concentrations of sodium absorption ratio (SAR) less than 15, soil electrical conductivity (EC) less than 2 dS m.sup.−1 (m mho cm.sup.−1), cation exchange capacity (CEC) less than 57.5 centimoles/kg, and a pH less than 8; the specific soil ratios and concentration levels selected for raising a particular crop and reducing soil bicarbonates/carbonates to increase soil porosity and improve water penetration.

24. A redox water treatment method according to claim 23, wherein the concentration of sulfurous acid of the conditioned wastewater has a pH between 2 and 6.8 for alkaline soil land application.

Description

DESCRIPTION OF THE DRAWINGS

[0121] FIG. 1 illustrates an example of an influent flow scheme for wastewater treatment.

[0122] FIG. 2 illustrates an application flow scheme for wastewater disinfection and denitrification.

DESCRIPTION OF THE ILLUSTRATED EMBODIMENTS

[0123] FIG. 1 illustrates an example of an influent flow scheme for wastewater treatment. The saline influent high in BOD, TSS, N, and P is micro-screened to remove separated solids; thereby reducing the filtrate BOD<50%, N<25%, and P<25%. The filtrate is passed through a sulfurous acid generator adding sulfur dioxide, sulfites and bisulfites thereto at a pH of ˜3. The acid enhanced filtrate is then pH adjusted with lime to concentrate the sulfites and bisulfites at a pH of approximately 7. The calcium precipitates ˜25% of the phosphates, and many heavy metals in solution, which are removed by a second filter.

[0124] This reduced phosphate, heavy metal free filtrate is then exposed to low pressure UV for ½ to 1 hour to remove the nitrates and disinfect the filtrate. If Phosphorous has to be further reduced, ferric chloride or another reagent is added and filtered to remove the phosphorous.

[0125] Lastly, if BOD's are too high, the reduced metal, nitrogen, and phosphorous filtrate is exposed to ozone to remove the BOD to provide a salt balanced, disinfected filtrate suitable for open stream discharge.

[0126] FIG. 2 illustrates an application flow scheme for wastewater disinfection and denitrification. Saline secondary treated wastewaters with BOD removed, and nitrogen and phosphorous reduced, is passed through a sulfurous acid generator as before to add adding sulfur dioxide, sulfites and bisulfites thereto at a pH of ˜3. The acid enhanced filtrate is then pH adjusted with lime to concentrate the sulfites and bisulfites at a pH of approximately 7. The calcium precipitates ˜25% of the phosphates, and many heavy metals in solution, which are removed by a second filter

[0127] This reduced phosphate, heavy metal free filtrate is then exposed to low pressure UV for ½ to 1 hour to remove the nitrates and disinfect the filtrate; providing a salt balanced filtrate suitable for land application.

[0128] While the invention has been described with reference to its presently-preferred embodiment, it is not limited thereto. Rather, this invention is limited only insofar as it is defined by the following set of patent claims and includes within its scope all equivalents thereof. The present invention may be embodied in other specific forms without departing from its structures, methods, or other essential characteristics as broadly described herein and claimed hereinafter. The described embodiments are to be considered in all respects only as illustrative, and not restrictive. The scope of the invention is, therefore, indicated by the appended claims, rather than by the foregoing description. All changes that come within the meaning and range of equivalency of the claims are to be embraced within their scope.