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

Patent metadata

Field	Value
Publication number	US-11208338-B2
Application number	US-201916527900-A
Country	US
Kind code	B2
Filing date	Jul 31, 2019
Priority date	Sep 18, 2009
Publication date	Dec 28, 2021
Grant date	Dec 28, 2021

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.

First claim

The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:

1. A method for reducing a concentration of one or more contaminants in contaminated water having a first concentration of contaminants, the method comprising:
providing zero valent iron media, at least partially coated with an iron oxide compound, in a reactor vessel;
contacting the zero valent iron media with a conditioning additive comprising a soluble aluminum salt to produce a conditioned zero valent iron media;
contacting the contaminated water with the conditioned zero valent iron media in the reactor vessel to produce a product water having a second concentration of contaminants lower than the first concentration of contaminants;
introducing a reaction additive comprising a soluble aluminum salt into the reactor vessel; and
maintaining a concentration of aluminum ions within the reactor vessel within a predetermined range by monitoring and adjusting a flow rate of the reaction additive with a process control subsystem,
the process control subsystem comprising:
a first sensor system configured to measure at least one of a flow rate of a solution being received in the reactor vessel through 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,
a 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 method of claim 1 , wherein contacting the zero valent iron media with the conditioning additive comprises contacting the zero valent iron media with aluminum chloride.

3. The method of claim 1 , wherein contacting the zero valent iron media with the conditioning additive comprises contacting the zero valent iron media with aluminum chloride and sodium nitrate.

4. The method of claim 1 , wherein introducing the reaction additive comprises introducing aluminum chloride.

5. The method of claim 1 , wherein producing the product water having the second concentration of contaminants comprises reducing a concentration of one or more contaminants 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 in the contaminated water.

6. The method of claim 1 , wherein providing zero valent iron media in the reactor vessel comprises providing zero valent iron media in one of a packed bed, a fluidized bed, and a mixed bed.

7. The method of claim 1 , wherein contacting the contaminated water with the conditioned zero valent iron media comprises introducing contaminated water originating from a source selected from the group consisting of flue-gas desulfurization waste water, petroleum refining process waste water, mining operations waste water, surface water, and ground water.

8. The method of claim 1 , wherein the soluble aluminum salt is selected from the group consisting of aluminum chloride and aluminum sulfate.

9. A method for selectively reducing the concentration of selenate in contaminated water having a first concentration of selenate and a first concentration of nitrate, the method comprising:
providing zero valent iron media, at least partially coated with an iron oxide compound, in a reactor vessel;
contacting the zero valent iron media with a conditioning additive comprising a soluble aluminum salt to produce a conditioned zero valent iron media;
introducing a reaction additive comprising a soluble aluminum salt into the reactor vessel and maintaining a concentration of aluminum ions within the reactor vessel within a predetermined range by monitoring and adjusting a flowrate of the reaction additive with a process control subsystem; and
contacting the contaminated water with the conditioned zero valent iron media in the reactor vessel to produce a product water having a second concentration of selenate and a second concentration of nitrate,
wherein the second concentration of selenate is less than the first concentration of selenate,
wherein the second concentration of nitrate is less than the first concentration of nitrate, and
wherein the decrease in selenate concentration is greater than the decrease in nitrate concentration, and
wherein the process control subsystem comprises:
a first sensor system configured to measure at least one of a flow rate of a solution being received in the reactor vessel through 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,
a 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.

10. The method of claim 9 , wherein the soluble aluminum salt is selected from the group consisting of aluminum chloride and aluminum sulfate.

11. The method of claim 9 , wherein contacting the zero valent iron media with the conditioning additive comprises contacting the zero valent iron media with a soluble aluminum salt and sodium nitrate.

12. The method of claim 9 , wherein the contaminated water further comprises one or more contaminants selected from the group consisting of arsenic, cadmium, chromium III, chromium VI, cobalt, copper, lead, mercury, antimony, molybdenum, nickel, titanium, tungsten, vanadium, and zinc.

13. The method of claim 9 , wherein contacting the contaminated water with the conditioned zero valent iron media comprises introducing contaminated water originating from a source selected from the group consisting of flue-gas desulfurization waste water, petroleum refining process waste water, mining operations waste water, surface water, and ground water.

14. The method of claim 9 , wherein providing zero valent iron media in the reactor vessel comprises providing zero valent iron media in one of a packed bed, a fluidized bed, and a mixed bed.

Assignees

• Texas A & M Univ Sys
• Evoqua Water Tech Llc

Inventors

• Huang Yongheng
• Wismer Michael
• Reyes Lew Andrew
• Qiao Xiangyi
• Dukes Simon
• Sassaman Frank
• Berger David

Classifications

• C02F2209/005

  Processes using a programmable logic controller [PLC] · CPC title

• C02F2103/365

  from petrochemical industry (e.g. refineries) · CPC title

• B01J37/0201

  Impregnation · CPC title

• C02F1/5245

  using basic salts, e.g. of aluminium and iron · CPC title

• C02F1/281

  using inorganic sorbents · CPC title