IP Library › Granted Patent US 11,124,431
Granted Patent B2
US 11,124,431 · App. 16/698,360 · Granted Sep 21, 2021

System and method for water treatment including granular activated carbon regeneration

Inventor: Daniel J. Cho (Philadelphia, PA)
Assignee: Onvector LLC
C02F1/283B01J20/20B01J20/3416B01J20/3441B01D15/203C02F2101/301C02F2101/36C02F2303/16
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Quick Facts
Patent No.
US 11,124,431
App. No.
16/698,360
Granted
Sep 21, 2021
Kind
B2
Abstract

A water treatment system includes an adsorption column including granular activated carbon (GAC) that adsorbs contaminants from untreated water onto the GAC, thereby producing treated water, a first electrode disposed at a proximal side of the adsorption column, with a gap between the first electrode and the GAC, a second electrode disposed at a distal side of the adsorption column, a drain outlet in fluid communication with the adsorption column for draining water out of the adsorption column, a gas inlet in fluid communication with the adsorption column for injecting a displacement gas into the adsorption column, a high voltage power supply electrically connected to one of the first electrode and the second electrode for generating a plasma discharge within the GAC, thereby regenerating the GAC within the adsorption column, and a gas outlet in fluid communication with the adsorption column for venting waste gas produced by the plasma discharge.

Claims (47)

1. A water treatment system comprising:

an adsorption column including granular activated carbon (GAC) that adsorbs contaminants from untreated water onto the GAC, thereby producing treated water;

a first electrode disposed at a proximal side of the adsorption column, with a gap between the first electrode and the GAC;

a second electrode disposed at a distal side of the adsorption column;

a drain outlet in fluid communication with the adsorption column for draining water out of the adsorption column;

a gas inlet in fluid communication with the adsorption column for injecting a displacement gas into the adsorption column;

a high voltage power supply electrically connected to one of the first electrode and the second electrode for generating a plasma discharge within the GAC, thereby regenerating the GAC within the adsorption column; and

a gas outlet in fluid communication with the adsorption column for venting waste gas produced by the plasma discharge.

2. The water treatment system of claim 1 , wherein the first electrode is a high voltage electrode, the second electrode is a ground electrode, and the high voltage power supply is electrically connected to the first electrode.

3. The water treatment system of claim 1 , wherein the first electrode is a ground electrode, the second electrode is a high voltage electrode, and the high voltage power supply is electrically connected to the second electrode.

4. The water treatment system of claim 1 , wherein the plasma discharge is an arc plasma discharge.

5. The water treatment system of claim 1 , wherein the second electrode is embedded in the GAC at the distal side of the adsorption column.

6. The water treatment system of claim 1 , wherein the proximal side is a top side and the distal side is a bottom side of the adsorption column.

7. The water treatment system of claim 1 , further including a temperature sensor that measures temperature of the GAC.

8. The water treatment system of claim 1 , wherein contaminants include perfluorooctane sulfonate, perfluorooctanoic acid, or any combination thereof.

9. The water treatment system of claim 1 , wherein the displacement gas is a hydrocarbon gas heavier than air.

10. The water treatment system of claim 9 , wherein the displacement gas is propane, butane, or a mixture thereof.

11. The water treatment system of claim 1 , wherein the gap is in a range of between 0.5 cm and 1 cm.

12. The water treatment system of claim 1 , further including an untreated water inlet into the adsorption column and a treated water outlet out of the adsorption column.

13. The water treatment system of claim 12 , further including a pump in fluid communication with the untreated water inlet.

14. The water treatment system of claim 13 , wherein the pump includes a variable frequency motor.

15. A method of regenerating granular activated carbon (GAC) in a water treatment system, the method comprising:

draining water out of an adsorption column containing GAC of a water treatment system;

injecting a displacement gas into the adsorption column;

generating an electrical voltage between a first electrode disposed at a proximal side of the adsorption column and a second electrode disposed at a distal side of the adsorption column to form a plasma discharge within the GAC, thereby regenerating the GAC within the adsorption column; and

venting waste gas produced by the plasma discharge.

16. The method of claim 15 , wherein the first electrode is a high voltage electrode, the second electrode is a ground electrode, and a high voltage power supply is electrically connected to the first electrode.

17. The method of claim 16 , further including adjusting output power of the high voltage power supply based on a thermostatic feedback signal from a temperature sensor that measures temperature of the GAC.

18. The method of claim 15 , wherein the first electrode is a ground electrode, the second electrode is a high voltage electrode, and a high voltage power supply is electrically connected to the second electrode.

19. The method of claim 18 , further including adjusting output power of the high voltage power supply based on a thermostatic feedback signal from a temperature sensor that measures temperature of the GAC.

20. The method of claim 15 , wherein the electrical voltage is generated for a regeneration time that is less than 30 min.

21. The method of claim 20 , wherein the regeneration time is less than 10 min.

22. The method of claim 21 , wherein the regeneration time is less than 1 min.

23. A method of treating water, the method comprising:

flowing untreated water into an adsorption column including granular activated carbon (GAC) that adsorbs contaminants from the water onto the GAC, thereby producing treated water;

flowing the treated water out of the adsorption column;

draining water out of the adsorption column;

injecting a displacement gas into the adsorption column;

generating an electrical voltage between a first electrode disposed at a proximal side of the adsorption column and a second electrode disposed at a distal side of the adsorption column to form a plasma discharge within the GAC, thereby regenerating the GAC within the adsorption column; and

venting waste gas produced by the plasma discharge.

24. The method of claim 23 , wherein the first electrode is a high voltage electrode, the second electrode is a ground electrode, and a high voltage power supply is electrically connected to the first electrode.

25. The method of claim 24 , further including adjusting output power of the high voltage power supply based on a thermostatic feedback signal from a temperature sensor that measures temperature of the GAC.

26. The method of claim 23 , wherein the first electrode is a ground electrode, the second electrode is a high voltage electrode, and a high voltage power supply is electrically connected to the second electrode.

27. The method of claim 26 , further including adjusting output power of the high voltage power supply based on a thermostatic feedback signal from a temperature sensor that measures temperature of the GAC.

28. The method of claim 23 , wherein the electrical voltage is generated for a regeneration time that is less than 30 min.

29. The method of claim 28 , wherein the regeneration time is less than 10 min.

30. The method of claim 29 , wherein the regeneration time is less than 1 min.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 13, 2020
From: CHO, DANIEL J
To: ONVECTOR LLC
Reel/Frame 051489/0412 →
Continuity (2)
Provisional Application 62917268 · Nov 30, 2018
Related Publication 20200171409A1 · Jun 4, 2020
Cited By (8)
US 12,275,661 US 12,304,850 US 12,351,498 US 12,473,222 US 12,515,974 US 12,534,390 US 12,545,601 US 12,655,051