IP Library Granted Patent US 7,727,306
Granted Patent B2
US 7,727,306 · App. 11/731,149 · Granted Jun 1, 2010

Systems and methods for flow-through treatment of contaminated fluids

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Quick Facts
Patent No.
US 7,727,306
App. No.
11/731,149
Granted
Jun 1, 2010
Kind
B2
Abstract

A system for use in the treatment of contaminated fluid is provided. The system includes a source from which contaminated fluid may be introduced into the system, and a reservoir for an adsorbent material designed to remove contaminants from the fluid. The system also includes a reactor within which the adsorbent material and the contaminated fluid may be accommodated for treatment. A separation device may further be included for removing spent adsorbent materials from the system. A method for treating contaminated fluid is also provided.

Claims (56)

1. A system for treatment of contaminated fluid, the system comprising:

a reservoir of an adsorbent nanomaterial designed to remove contaminants from contaminated fluid;

a reactor for providing an environment within which a mixture of adsorbent nanomaterial and contaminated fluid can be accommodated for treatment of the contaminated fluid;

a pump designed to introduce, into the system, an amount of adsorbent nanomaterial that can be proportional to a flow rate of the contaminated fluid and an amount of contaminant in the contaminated fluid, so as to substantially reduce a period of time for treatment;

an outlet on the reactor through which treated fluid within the reactor can exit; and

a separation device for removal of spent adsorbent material.

2. A system as set forth in claim 1 , wherein the adsorbent nanomaterial in the reservoir includes a porous particle made from self-assembled monolayers on mesoporous supports (SAMMS).

3. A system as set forth in claim 2 , wherein the particle is made from silica.

4. A system as set forth in claim 2 , wherein the particle has a pore size ranging from about 2 nanometers (nm) to about 7 nm.

5. A system as set forth in claim 1 , wherein the adsorbent nanomaterial has an apparent density ranging from about 0.2 grams/milliliter to about 0.4 grams/milliliter.

6. A system as set forth in claim 1 , wherein the adsorbent nanomaterial is capable of removing heavy metal contaminants from the fluid.

7. A system as set forth in claim 6 , wherein the heavy metal contaminants include mercury, arsenic, cadmium, lead, silver, uranium, plutonium, neptunium, americium, other heavy metals, or a combination thereof.

8. A system as set forth in claim 1 , wherein the contaminated fluid is viscous in nature.

9. A system as set forth in claim 8 , wherein the viscous fluid includes one of oils, waste oils, other fluid viscous in nature, or a combination thereof.

10. A system as set forth in claim 1 , wherein the contaminated fluid is non-viscous in nature.

11. A system as set forth in claim 10 , wherein the non-viscous fluid includes a liquid or a gas.

12. A system as set forth in claim 10 , wherein the non-viscous fluid includes produced water.

13. A system as set forth in claim 1 , wherein the reactor includes an inlet to permit contaminated fluid and the adsorbent nanomaterial to be introduced into the reactor.

14. A system as set forth in claim 1 , wherein the reactor includes a pump to assist in the removal of treated fluid from the reactor.

15. A system as set forth in claim 1 , wherein the reactor includes a second inlet to introduce a volume of high pressure into the reactor to assist in the removal of treated fluid from the reactor.

16. A system as set forth in claim 1 , wherein the separation device is a centrifugal force type device capable of concentrating spent adsorbent material at a bottom of the device.

17. A system as set forth in claim 16 , wherein the separation device includes a collector at the bottom of the device, so that the spent adsorbent material concentrated at the bottom of the device can be directed thereinto and removed.

18. A system as set forth in claim 1 , wherein the separation device is a filter having pores or mesh openings capable of collecting the adsorbent nanomaterials thereon for removal.

19. A system as set forth in claim 1 , further including a pathway between the reservoir and the reactor to permit the mixture of adsorbent nanomaterial and contaminated fluid to travel to the reactor.

20. A system as set forth in claim 19 , further including a control valve on the pathway to adjust a flow rate of the mixture along the pathway.

21. A system as set forth in claim 1 , further including a mixer associated with the reactor to enhance mixing of the adsorbent nanomaterial and contaminated fluid.

22. A system as set forth in claim 1 , further including a sensor for indicating a level of the mixture of adsorbent nanomaterial and contaminated fluid within the reactor.

23. A system as set forth in claim 1 , further including a discharge valve to remove treated fluid from the system.

24. A system as set forth in claim 23 , further including a flow meter associated with the discharge valve to determine a flow rate of treated fluid being removed from the system.

25. A system as set forth in claim 1 , further having at least one additional reactors to permit a continuous treatment process to be implemented.

26. A system as set forth in claim 1 , wherein the period of time for treatment is less than 15 minutes.

27. A system as set forth in claim 1 , wherein the period of time for treatment ranges from less than about 2 minutes to about 10 minutes.

28. A method for treating contaminated fluid, the method comprising:

providing an environment within which contaminated fluid can be treated;

introducing an amount of an adsorbent nanomaterial and a contaminated fluid into the environment, the amount of adsorbent nanomaterial being introduced being proportional to the flow-rate of the contaminated fluid and an amount of contaminant within the contaminated fluid;

allowing the adsorbent nanomaterial to interact with the contaminated fluid over a period of time, so that the adsorbent nanomaterial can attract and remove contaminants from the fluid; and

discharging treated fluid from the environment.

29. A method as set forth in claim 28 , wherein the step of providing includes providing a source of contaminated fluid to be treated and a reservoir of the adsorbent nanomaterial.

30. A method as set forth in claim 28 , wherein the step of introducing includes generating a slurry of adsorbent nanomaterial.

31. A method as set forth in claim 28 , wherein the step of introducing includes mixing the adsorbent nanomaterial and the contaminated fluid prior to directing them into the environment.

32. A method as set forth in claim 28 , wherein the step of introducing includes directing the adsorbent nanomaterial and the contaminated fluid independently into the environment.

33. A method as set forth in claim 28 , wherein, in the step of introducing, the adsorbent nanomaterial includes a porous particle made from self-assembled monolayers on mesoporous supports (SAMMS).

34. A method as set forth in claim 33 , wherein the step of introducing includes providing a slurry of SAMMS having an apparent density ranging from about 0.2 grams/milliliter to about 0.4 grams/milliliter.

35. A method as set forth in claim 28 , wherein the step of introducing includes controlling a rate at which the contaminated fluid may be introduced, so that an appropriate amount of the adsorbent nanomaterial can be determined for introduction.

36. A method as set forth in claim 35 , wherein, in the step of controlling, the amount of adsorbent nanomaterial can be proportional to the flow rate of the contaminated fluid and the amount of contaminant within the fluid flow.

37. A method as set forth in claim 28 , wherein, in the step of introducing, the contaminated fluid is viscous in nature.

38. A method as set forth in claim 37 , wherein, in the step of introducing, the viscous fluid includes one of oils, waste oils, other fluid viscous in nature, or a combination thereof.

39. A method as set forth in claim 28 , wherein, in the step of introducing, the contaminated fluid is non-viscous in nature.

40. A method as set forth in claim 39 , wherein, in the step of introducing, the non-viscous fluid includes a liquid or a gas.

41. A method as set forth in claim 39 , wherein, in the step of introducing, the non-viscous fluid includes produced water.

42. A method as set forth in claim 28 , wherein, in the step of allowing, the period of time ranges from less than about 2 min. to about 10 min.

43. A method as set forth in claim 28 , wherein the step of allowing includes permitting the adsorbent nanomaterial to remove heavy metal contaminants from the fluid.

44. A method as set forth in claim 43 , wherein, in the step of permitting, the heavy metal contaminants include mercury, arsenic, cadmium, lead, silver, uranium, plutonium, neptunium, americium, other heavy metals, or a combination thereof.

45. A method as set forth in claim 28 , wherein the step of allowing includes permitting the adsorbent nanomaterial to bind and trap the contaminants within the nanomaterial.

46. A method as set forth in claim 28 , wherein the step of discharging includes collecting spent adsorbent nanomaterial having contaminants attracted thereto.

47. A method as set forth in claim 28 , further including providing a plurality of similar environments within which contaminated fluid can be treated, so as to implement a substantially continuous treatment process.

Assignments (1)
CHANGE OF NAME Recorded Feb 25, 2014
From: PERRY EQUIPMENT CORPORATION
To: PECOFACET (US), INC.
Reel/Frame 032332/0465 →