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37 MEETING STRINGENT METALS REMOVAL REQUIREMENTS WITH IRON ADSORPTION/COPRECIPITATION Mark A. Manzione, Engineer Brown and Caldwell Consulting Engineers Pleasant Hill, California 94523 Douglas T. Merrill, Engineer Brown and Caldwell Consulting Engineers Pleasant Hill, California 94523 Mary McLearn, Project Manager Electric Power Research Institute Palo Alto, California 94303 Winston Chow, Project Manager Electric Power Research Institute Palo Alto, California 94303 INTRODUCTION The Water Quality Act of 1987 set the stage for establishing a far more stringent set of metals- removal discharge requirements than industry and municipalities have previously faced. These requirements cover elements the USEPA designates as priority pollutants such as arsenic, antimony, selenium, beryllium, cadmium, chromium, copper, lead, nickel, silver, and zinc. (For convenience, these elements are called "metals" here, even though not all exhibit metal-like behavior.) Some states also restrict discharge of other metals, such as molybdenum and vanadium. Many industrial and municipal facilities discharge wastewaters that contain these metals. The new metals limits are beginning to come into effect now, and managers of these facilities are seeking cost- effective ways to remove these metals. The iron adsorption/ coprecipitation process can help these managers meet the new metals limits by removing both dissolved and suspended forms of these metals simply and economically. Treatment involves adding an iron salt such as ferric chloride to the water, unless the water contains sufficient dissolved iron already. Iron oxyhydroxide precipitate then forms, as shown in Equation 1. FeCl3 + 3H20 - Fe(OH)3(s)i + 3H+ + 3C1" (1) The metals are trapped within (coprecipitated) and adsorbed onto the precipitate, which then settles out, leaving a purified effluent. Treatment equipment is the same as that used in conventional physical/chemical water treatment systems, typically a reaction mix tank, flocculation chamber, and a clarifier. Chemical feed and sludge handling equipment is also needed. This technology's main advantages are: 1. Simplicity. The operator merely adjusts pH and iron dose to remove the metals of choice to the extent desired. 2. Selectivity. Generally, major components such as calcium, magnesium, and bicarbonate do not compete with the metallic elements for adsorption sites. 3. Effectiveness. The technology can reduce metals concentrations to the parts per billion levels regulatory agencies now require. These levels are far below those that can be achieved by precipitation, the traditional method for metals removal. 4. Low cost. The ability to remove only the components needed, low chemical demands, and elimination of the need for pretreatment or post-treatment make costs low relative to costs of other metals removal processes. 5. Versatility. The process can be retrofitted into existing wastewater and water treatment 44th Purdue Industrial Waste Conference Proceedings, © 1990 Lewis Publishers, Inc., Chelsea, Michigan 48118. Printed in U.S.A.
Object Description
Purdue Identification Number | ETRIWC198937 |
Title | Meeting stringent metals removal requirements with iron adsorption/ coprecipitation |
Author |
Manzione, Mark A. Merrill, Douglas T. McLearn, Mary E. Chow, Winston |
Date of Original | 1989 |
Conference Title | Proceedings of the 44th Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,40757 |
Extent of Original | p. 335-342 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital object copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Date Digitized | 2009-08-18 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 335 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Transcript | 37 MEETING STRINGENT METALS REMOVAL REQUIREMENTS WITH IRON ADSORPTION/COPRECIPITATION Mark A. Manzione, Engineer Brown and Caldwell Consulting Engineers Pleasant Hill, California 94523 Douglas T. Merrill, Engineer Brown and Caldwell Consulting Engineers Pleasant Hill, California 94523 Mary McLearn, Project Manager Electric Power Research Institute Palo Alto, California 94303 Winston Chow, Project Manager Electric Power Research Institute Palo Alto, California 94303 INTRODUCTION The Water Quality Act of 1987 set the stage for establishing a far more stringent set of metals- removal discharge requirements than industry and municipalities have previously faced. These requirements cover elements the USEPA designates as priority pollutants such as arsenic, antimony, selenium, beryllium, cadmium, chromium, copper, lead, nickel, silver, and zinc. (For convenience, these elements are called "metals" here, even though not all exhibit metal-like behavior.) Some states also restrict discharge of other metals, such as molybdenum and vanadium. Many industrial and municipal facilities discharge wastewaters that contain these metals. The new metals limits are beginning to come into effect now, and managers of these facilities are seeking cost- effective ways to remove these metals. The iron adsorption/ coprecipitation process can help these managers meet the new metals limits by removing both dissolved and suspended forms of these metals simply and economically. Treatment involves adding an iron salt such as ferric chloride to the water, unless the water contains sufficient dissolved iron already. Iron oxyhydroxide precipitate then forms, as shown in Equation 1. FeCl3 + 3H20 - Fe(OH)3(s)i + 3H+ + 3C1" (1) The metals are trapped within (coprecipitated) and adsorbed onto the precipitate, which then settles out, leaving a purified effluent. Treatment equipment is the same as that used in conventional physical/chemical water treatment systems, typically a reaction mix tank, flocculation chamber, and a clarifier. Chemical feed and sludge handling equipment is also needed. This technology's main advantages are: 1. Simplicity. The operator merely adjusts pH and iron dose to remove the metals of choice to the extent desired. 2. Selectivity. Generally, major components such as calcium, magnesium, and bicarbonate do not compete with the metallic elements for adsorption sites. 3. Effectiveness. The technology can reduce metals concentrations to the parts per billion levels regulatory agencies now require. These levels are far below those that can be achieved by precipitation, the traditional method for metals removal. 4. Low cost. The ability to remove only the components needed, low chemical demands, and elimination of the need for pretreatment or post-treatment make costs low relative to costs of other metals removal processes. 5. Versatility. The process can be retrofitted into existing wastewater and water treatment 44th Purdue Industrial Waste Conference Proceedings, © 1990 Lewis Publishers, Inc., Chelsea, Michigan 48118. Printed in U.S.A. |
Resolution | 300 ppi |
Color Depth | 8 bit |
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