Method and system of destruction of volatile compounds in wastewater

• US 8,282,837 B2
• Filed: 05/13/2010
• Issued: 10/09/2012
• Est. Priority Date: 03/07/2005
• Status: Active Grant

• Current Assignee: Elcon Recycling Center (2003) Ltd.
• Original Assignee: Elcon Recycling Center (2003) Ltd.
• Inventors: Levin, Alexander
• Primary Examiner(s): Drodge, Joseph
• Assistant Examiner(s): Allen, Cameron J
• Application Number:
  US12/779,183
• Publication Number:
  US 20100219132A1
• Time in Patent Office: 880 Days
• Field of Search: 210/748.11, 210/749, 210/758, 210/175, 210/180, 210/202, 210/205, 210/195.1, 210/259, 210/774, 210/806, 210/603, 210/607, 210/664, 210/634, 210/639, 210/669, 210/284, 210/280, 210/150, 210/177, 952/63, 952/53, 952/79, 951/53, 952/45, 422/169, 422/168, 422/171, 422/173, 961/32, 961/21, 961/30, 961/55, 961/81, 962/31, 423/210, 423/240.R
• US Class Current: 210/758
• CPC Class Codes: B01D 3/343 the substance being a gas

Abstract

The invention proposes a method of destruction of volatile organic and inorganic compounds in wastewater, this method includes following stages: stripping the aforementioned volatile compounds in a stripping-chemisorption column; preliminary heating the gaseous medium containing these volatile compounds in a first heat regenerator; thermal, flare or thermo-catalytic oxidation of the volatile compounds in circulating gaseous medium; cooling the gaseous medium in a second heat regenerator; chemisorption of acidic gases from the gaseous medium in the stripping-chemisorption column with stripping at the same time additional amount of the volatile compounds from the wastewater. After specific period, direction of the gaseous medium flow is alternated. The proposed method can be executed at elevated temperature. The invention includes as well systems realizing the proposed method.

Claims

1. A system for processing water contaminated with volatile compounds, comprising:

a stripping unit including a first inlet for contaminated water, a second inlet for a circulating gaseous medium, and an outlet;

wherein the stripping unit is operative to strip volatile compounds from the contaminated water and into said circulating gaseous medium, and for extraction of oxidation products from said circulating gaseous medium;

an oxidation unit having an inlet coupled to said stripping unit outlet, to oxidize the volatile compounds stripped into said circulating gaseous medium, and to form oxidation products in said circulating gaseous medium;

an outlet from said oxidation unit for said circulating gaseous medium carrying said formed oxidation products coupled to the second inlet of said stripping unit; and

a heat regeneration system to preheat said circulating gaseous medium carrying said stripped volatile compounds entering said oxidation unit from said stripping unit, and to cool said circulating gaseous medium carrying said formed oxidation products exiting said oxidation unit.

2. A system according to claim 1, wherein said heat regeneration system comprises:

a first and a second heat exchange unit and a heat flow reversal unit,

wherein the heat flow reversal unit is operative to change a direction of heat flow from a first state in which the first heat exchange unit cools said circulating gaseous medium carrying said formed oxidation products exiting said oxidation unit and the second heat exchange unit preheats said circulating gaseous medium carrying said stripped volatile compounds entering said oxidation unit, to a second state in which the second heat exchange unit cools said circulating gaseous medium carrying said formed oxidation products exiting said oxidation unit and the first heat exchange unit preheats said circulating gaseous medium carrying said stripped volatile compounds entering said oxidation unit.

3. A system according to claim 2, wherein said heat flow reversal unit reverses the flow direction of said circulating gaseous medium carrying said formed oxidation products exiting said oxidation unit and of said circulating gaseous medium carrying said stripped volatile compounds entering said oxidation unit.

4. A system according to claim 3, wherein the heat flow reversal unit includes a blower.

5. A system according to claim 3, wherein the heat flow reversal unit includes a system of shutters.

6. A system according to claim 2, wherein said heat flow reversal unit is responsive to an average temperature in the one of said first or said second heat exchange units then being used for cooling said circulating gaseous medium exiting said oxidation means reaching a certain level.

7. A system according to claim 1, wherein said oxidation unit is a thermal oxidation unit.

8. A system according to claim 1, wherein said oxidation unit is a flare oxidation unit.

9. A system according to claim 1, wherein said oxidation unit is a thermo-catalytic oxidation unit.

10. A system according to claim 1, further comprising a heating unit operative to heat the wastewater before entry thereof into said stripping unit.

11. A system according to claim 1, further comprising an inlet for adding an additional gas to said circulating gaseous medium carrying said stripped volatile compounds entering said oxidation unit from said stripping unit, said additional gas inlet being so located that the additional gas is preheated together with said circulating gaseous medium carrying said stripped volatile compounds entering said oxidation unit.

12. A system according to claim 1, wherein the stripping unit includes a chemisorption bed.

36. A system according to claim 1, wherein the contaminated water is preheated in said stripping unit before further processing.

37. A system according to claim 1, wherein the stripping unit is operative to strip substantially all volatile compounds from the contaminated water and into said circulating gaseous medium.

38. A system according to claim 1, wherein heat to preheat said circulating gaseous medium carrying said stripped volatile products entering said oxidation unit from said stripping unit is provided by heat extracted from said circulating gaseous medium carrying said formed oxidation products exiting said oxidation unit.

13. A method of processing water contaminated with volatile organic and inorganic compounds, the method comprising:

delivering the contaminated water and a circulating gaseous medium to a stripping unit;

stripping the volatile compounds from the contaminated water and into said circulating gaseous medium;

oxidizing the volatile compounds stripped into said circulating gaseous medium, to form oxidation products in said circulating gaseous medium;

preheating said circulating gaseous medium before oxidation of the volatile compounds;

cooling said circulating gaseous medium carrying said formed oxidation products, said preheating and cooling being performed in a heat regeneration system; and

removing said oxidation products formed in said circulating gaseous medium by said stripping unit.

14. The method of claim 13, wherein the heat regeneration system includes a first and a second heat exchange unit, and

wherein the method further includes reversing a direction of heat flow from a first state in which the first heat exchange unit cools said circulating gaseous medium carrying said formed oxidation products, and the second heat exchange unit preheats said circulating gaseous medium carrying said stripped volatile compounds before oxidation, to a second state in which the second heat exchange unit cools said circulating gaseous medium carrying said formed oxidation products, and the first heat exchange unit preheats said circulating gaseous medium carrying said stripped volatile compounds before oxidation.

15. A method according to claim 14, wherein the direction of said heat flow is reversed by reversing the flow direction of said circulating gaseous medium.

16. A method according to claim 14, wherein the direction of said heat flow is reversed by a blower.

17. A method according to claim 14, wherein the direction of said heat flow is reversed by a system of shutters.

18. The method of claim 14, wherein the direction of said heat flow is reversed when average temperature is elevated up to a certain level in said first or in said second heat exchange unit being used for cooling said circulating gaseous medium carrying said formed oxidation products.

19. A method according to claim 13 further comprising adding an additional gas into said circulating gaseous medium carrying said stripped volatile products before oxidation, said additional gas being added at a location such that said additional gas is preheated together with said circulating gaseous medium carrying said stripped volatile products.

20. A method according to claim 19, wherein said additional gas includes oxygen.

21. The method of claim 19, wherein the amount of said additional gas added into said circulating gaseous medium is determined in accordance with an amount of oxygen consumed by said oxidation.

22. A method according to claim 13, wherein oxidation products are removed from said circulating gaseous medium by chemisorption.

23. A method according to claim 22, wherein said chemisorption is performed in said stripping unit.

24. A method according to claim 13, wherein said oxidation is performed by thermal oxidation.

25. A method according to claim 13, wherein said oxidation is performed by flare oxidation.

26. A method according to claim 13, wherein said oxidation is performed by thermo-catalytic oxidation.

27. A method according to claim 13, further comprising measuring a concentration of the volatile compounds in said contaminated water or in said circulating gaseous medium after stripping, and/or measuring temperatures in different locations in said circulating gaseous medium.

28. A method according to claim 13, further comprising changing a temperature of the contaminated water before stripping.

29. A method according to claim 28, wherein the temperature of the contaminated water is changed to achieve a desired rate of evaporation of the volatile compounds and, to prevent danger of explosion of said circulating gaseous medium.

30. A method according to claim 27, wherein the temperature of the contaminated water is changed to maintain a concentration of the volatile compounds in said circulating gaseous medium significantly lower than a dangerous level which can cause explosion of said circulating gaseous medium.

31. A method according to claim 13, wherein said contaminated water is delivered to the stripping unit in a continuous stream, and wherein stripping, oxidation, and chemisorption are performed in a plurality of processing subunits, each comprised of a stripping unit, an oxidation unit and a chemisorption unit arranged in series.

32. A method according to claim 31, wherein a temperature of said contaminated water is gradually elevated in a direction starting from first said processing sub-units to maintain a concentration of volatile compounds in the gaseous medium in processing sub-unit lower than a dangerous level.

33. A method according to claim 13, wherein said contaminated water is processed in batches.

34. A method according to claim 13, wherein the contaminated water is preheated in said stripping unit before processing.

35. A method according to claim 13, wherein the stripping unit is operative to strip substantially all volatile compounds from the contaminated water and into said circulating gaseous medium.