Arsenic removal system

Patent metadata

Field	Value
Publication number	US-9718713-B2
Application number	US-201313768477-A
Country	US
Kind code	B2
Filing date	Feb 15, 2013
Priority date	Feb 17, 2012
Publication date	Aug 1, 2017
Grant date	Aug 1, 2017

Abstract

A system is provided for removing arsenic from water to safe levels at or below the EPA standards. The system is a hybrid spouted vessel/fixed bed filter system that significantly enhances/improves arsenic removal for drinking water using zero-valent iron (ZVI) particles. Movement of the circulating, iron-containing particles in a dense moving bed that forms on the spouted vessel bottom creates an abrasive “self-polishing” action among them that continuously generates colloidal iron corrosion products. This material then circulates with the water in the vessel and is removed and concentrated in a fixed bed filter. The colloidal material captured and immobilized in the filter has been shown to remove arsenic from contaminated water at very rapid rates.

First claim

What is claimed:

1. A system for the removal of arsenic from water, comprising
a vessel having a spouted vessel bottom and containing zero valent iron particles having corrosion products on their surfaces; water containing arsenic disposed within said vessel; and
a fluid circulation system comprising an external inlet nozzle connected to the spouted vessel bottom, an inlet liquid jet in fluid communication with the external inlet nozzle and a draft tube disposed above an inlet spout;
wherein water containing arsenic from the inlet liquid jet enters the external inlet nozzle and circulates said zero valent iron particles upwardly along said draft tube to redeposit them into the vessel wherein the spouted vessel bottom channels the zero valent iron particles towards the inlet spout causing zero valent iron particle-zero valent iron particle abrasion and removal of the corrosion products from the the surfaces of the zero valent iron particles, wherein the zero valent iron particles are carbon steel spheres, and wherein the corrosion products bind with arsenic within the water.

2. The system of claim 1 , wherein the zero valent iron particles circulate in a moving bed formed on the spouted vessel bottom.

3. The system of claim 2 , further comprising: a filter within said vessel, said filter removing arsenic bound to the corrosion products from the water containing arsenic as it is circulated within said vessel.

4. The system of claim 1 , wherein said zero valent iron particles are carbon steel spheres having a diameter of about ⅛″.

5. The system of claim 1 , further comprising: a filter within said vessel, said filter removing arsenic bound to the corrosion products from the water containing arsenic as it is circulated within said vessel.

6. The system of claim 5 , wherein the filter is a fixed bed filter.

7. A method for the removal of arsenic from water, comprising
circulating water including arsenic through a vessel having a spouted vessel bottom and a fluid circulation system comprising an external inlet nozzle connected to the spouted vessel bottom, an inlet liquid jet in fluid communication with the external inlet nozzle and a draft tube disposed above an inlet spout, and containing zero valent iron particles having corrosion products on their surfaces, wherein the water including arsenic from the inlet liquid jet enters an external inlet nozzle and circulates said zero valent iron particles upwardly along said draft tube to redeposit them into the vessel, wherein the spouted vessel bottom channels the zero valent iron particles towards the inlet spout, and wherein circulation causes zero valent iron particle-zero valent iron particle abrasion and removal of the corrosion products from the surfaces of the zero valent iron particles to create colloidal iron corrosion products and wherein the zero valent iron particles are carbon steel spheres;
binding the arsenic to the colloidal iron corrosion products; and
removing the arsenic bound to the colloidal iron corrosion products from the water.

8. The method of claim 7 , wherein the zero valent iron particles circulate in a moving bed formed on the spouted vessel bottom.

9. The method of claim 8 , wherein the moving bed containing zero valent iron particles is in fluid communication with said vessel; wherein the vessel includes a filter, said filter removing colloidal arsenic from the water.

10. The method of claim 7 , wherein said zero valent iron particles are carbon steel spheres having a diameter of about ⅛″.

11. The method of claim 7 , further comprising a filter within said vessel, said filter removing arsenic bound to the colloidal iron corrosion products from said water as it is circulated within said vessel.

12. The method of claim 11 , wherein the filter is a fixed bed filter.

13. The method of claim 11 , further comprising periodic backwashing of the filter to remove collected colloidal material, wherein the collected colloidal material comprises the arsenic bound to the colloidal iron corrosion products.

Assignees

• Univ Brown

Inventors

• Calo Joseph
• Lakshmi Madhavan
• Kirchner Johannes
• Bain Euan

Classifications

• B01D24/36

  with the filter bed fluidised during the filtration (with the filter bed being stationary B01D24/02) · CPC title

• C02F1/281 Primary

  using inorganic sorbents · CPC title

• B01D15/26

  characterised by the separation mechanism · CPC title

• C02F2101/103

  Arsenic compounds · CPC title

• B01D15/1892

  the sorbent material moving as a whole, e.g. continuous annular chromatography, true moving beds or centrifugal chromatography · CPC title