IP Library Granted Patent US 10,377,648
Granted Patent B2
US 10,377,648 · App. 15/355,927 · Granted Aug 13, 2019

Selenium removal using aluminum salt at conditioning and reaction stages to activate zero-valent iron (ZVI) in pironox process

Inventors: Yongheng Huang (College Station, TX); Michael Wismer (Lino Lakes, MN); Lew Andrew Reyes (Singapore, SG); Xiangyi Qiao (Singapore, SG); Simon Dukes (Chelmsford, MA); Frank Sassaman (Fombell, PA); David Berger (Wampum, PA)
Assignees: The Texas A&M University System; Evoqua Water Technologies LLC
C02F1/705B01J20/0225B01J20/0229C02F1/281C02F1/5245B01J21/02B01J23/745B01J37/0201C02F1/001C02F1/66C02F1/74C02F2101/103C02F2101/106C02F2101/20C02F2103/06C02F2103/18C02F2103/365C02F2209/005C02F2209/40
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Quick Facts
Patent No.
US 10,377,648
App. No.
15/355,927
Granted
Aug 13, 2019
Kind
B2
Abstract

A system containing a reactor vessel including zero valent iron media, a source of a conditioning additive, a source of a reaction additive, and a process control subsystem is disclosed. A method for reducing a concentration of one or more contaminants in contaminated water including contacting zero valent iron media with a conditioning additive, contacting contaminated water with conditioned zero valent iron media, and introducing a reaction additive is also disclosed. The conditioning additive and reaction additive may each contain an aluminum salt.

Claims (34)

1. A system comprising:

a reactor vessel comprising at least one inlet, an outlet, and a side wall;

zero valent iron media at least partially coated with one or more iron oxide compounds disposed within the reactor vessel;

the reactor vessel being configured to receive a conditioning additive comprising a soluble aluminum salt through the at least one inlet, and contact the zero valent iron media with the conditioning additive to produce a conditioned zero valent iron media,

the reactor vessel being configured to receive a contaminated water and a reaction additive comprising a soluble aluminum salt through the at least one inlet and contact the conditioned zero valent iron media with the contaminated water and the reaction additive; and

a process control subsystem comprising a control module configured to maintain a predetermined concentration of aluminum ions in a solution within the reactor vessel,

the process control subsystem further comprising:

a first sensor system configured to measure at least one of a flowrate of a solution being received in the reactor vessel through the at least one inlet and a concentration of one or both of the conditioning additive and the reaction additive; and

a second sensor system configured to measure a concentration of one or both of the conditioning additive and the reaction additive in the solution within the reactor vessel,

the control module being in electrical communication with the first and second sensor systems and configured to receive information from the first and second sensor systems.

2. The system of claim 1 , wherein the control module is configured to maintain the predetermined concentration of aluminum ions in the solution within the reactor vessel by adjusting a flowrate of the reaction additive.

3. The system of claim 1 , wherein at least one of the conditioning additive and the reaction additive comprises aluminum chloride.

4. The system of claim 1 , wherein the process control subsystem further comprises a third sensor system in electrical communication with the control module and configured to measure at least one of a concentration of aluminum ions in a solution exiting the reactor vessel through the outlet and a flowrate of the solution exiting the reactor vessel through the outlet.

5. The system of claim 1 , wherein the conditioning additive comprises aluminum chloride and sodium nitrate.

6. The system of claim 1 , wherein the reaction additive comprises aluminum chloride.

7. The system of claim 1 , wherein the conditioning additive comprises about 20 mM of the soluble aluminum salt.

8. The system of claim 1 , wherein the predetermined concentration of aluminum ions within the reactor vessel is between about 0.25 mM and about 2.0 mM.

9. The system of claim 1 , wherein the zero valent iron media is disposed in a media bed selected from the group consisting of a packed bed, a fluidized bed, and a mixed bed.

10. The system of claim 1 , configured to reduce a concentration of one or more contaminants in the contaminated water selected from the group consisting of selenium, arsenic, cadmium, chromium III, chromium VI, cobalt, copper, lead, mercury, antimony, molybdenum, nickel, titanium, tungsten, vanadium, and zinc.

11. A system comprising:

a reactor vessel including zero valent iron media at least partially coated with an iron oxide compound disposed within the reactor vessel;

a source of a conditioning additive comprising a soluble aluminum salt in fluid communication with the reactor vessel and configured to introduce the conditioning additive into the reactor vessel to contact the zero valent iron media and produce a conditioned zero valent iron media;

a source of contaminated water fluidly connectable to the reactor vessel and configured to introduce the contaminated water into the reactor vessel to contact the conditioned zero valent iron media;

a source of a reaction additive comprising a soluble aluminum salt in fluid communication with the reactor vessel and configured to introduce the reaction additive into the reactor vessel to contact the contaminated water and conditioned zero valent iron media; and

a process control subsystem configured to maintain a concentration of aluminum ions within the reactor vessel within a predetermined range,

the process control subsystem further comprising:

a first sensor system configured to measure at least one of a flowrate of a solution being received in the reactor vessel through the at least one inlet and a concentration of one or both of the conditioning additive and the reaction additive; and

a second sensor system configured to measure a concentration of one or both of the conditioning additive and the reaction additive in the solution within the reactor vessel,

the control module being in electrical communication with the first and second sensor systems and configured to receive information from the first and second sensor systems.

12. The system of claim 11 , wherein at least one of the conditioning additive and the reaction additive comprises aluminum chloride.

13. The system of claim 11 , wherein the conditioning additive comprises aluminum chloride and sodium nitrate.

14. The system of claim 11 , wherein the reaction additive comprises aluminum chloride.

15. The system of claim 11 , wherein the process control subsystem is configured to maintain the concentration of aluminum ions in the reactor vessel between about 0.25 mM and 2.0 mM.

16. The system of claim 11 , wherein the concentration of soluble aluminum salt in the conditioning additive is about 20 mM.

Assignments (4)
RELEASE OF SECURITY INTEREST Recorded May 26, 2023
From: JPMORGAN CHASE BANK N.A., AS COLLATERAL AGENT
To: EVOQUA WATER TECHNOLOGIES LLC; NEPTUNE BENSON, INC.
Reel/Frame 063787/0943 →
SECURITY INTEREST Recorded Apr 7, 2021
From: EVOQUA WATER TECHNOLOGIES LLC; NEPTUNE BENSON, INC.
To: JPMORGAN CHASE BANK, N.A., AS COLLATERAL AGENT
Reel/Frame 055848/0689 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 3, 2017
From: HUANG, YONGHENG
To: THE TEXAS A&M UNIVERSITY SYSTEM
Reel/Frame 041166/0537 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 3, 2017
From: WISMER, MICHAEL; REYES, LEW ANDREW; QIAO, XIANGYI; DUKES, SIMON; SASSAMAN, FRANK; BERGER, DAVID
To: EVOQUA WATER TECHNOLOGIES LLC
Reel/Frame 041166/0837 →
Continuity (7)
Continuation In Part 13071343 · Mar 24, 2011
Continuation In Part PCTUS2010049528 · Sep 20, 2010
Provisional Application 62256734 · Nov 18, 2015
Provisional Application 61357466 · Jun 22, 2010
Provisional Application 61351194 · Jun 3, 2010
Provisional Application 61243875 · Sep 18, 2009
Related Publication 20170129792A1 · May 11, 2017