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Process of Metallic Replacment

Table of Contents:

Foreword

Process of Metallic Replacement

Method

Test Procedure

Sample Analysis

Results and Discussion

Mini-Column Tests

True-Size Column Tests - Low Flow Rate (110 to 150 ml/min)

Comparing a Low Flow Rate Metafix MRC with a Competitor's MRC

True-Size Column Tests - High to Very High Flow Rates (1 to 12 L/min)

Commercial Use of Metafix MRCs

Summary

Guidelines for Selecting Metafix MRCs

References

 

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Silver recovery via metallic replacement from used photo processing solutions is carried out by using metallic replacement cartridges (MRCs). Several papers review and discuss this method of silver recovery 1, 2 ,3, 4, along with two detailed studies carried out on black/white fixer by Dannenberg et al. 5 and by Cooley 6. Metallic replacement occurs when a solution containing dissolved ions of an active metal such as silver, contact a more active solid metal such as iron. The more active metal goes into solution as an ion and is replaced by the less active metal as a solid. This reaction is shown in the following equation:

REACTION 1

Ag(I) + Fe=Ag + Fe(II)

Iron becomes ionic and goes into solution while the silver ions, originally in the solution, become silver metal. Other metals, such as aluminum, copper, magnesium and zinc, will also work because they are more active than silver. Iron in various forms is the most widely-used metal because it is less expensive and has minimal environmental impact.
In photo processing applications, the spent silver-rich solutions are metered through the iron-filled MRC. The silver metal is retained in the cartridge and the ionic iron is discharged along with the desilvered solution. In this paper, the terms "column" and "cartridge" are used interchangeably. When referring to Metafix MRCs manufactured with MetaWool, the term Metafix MRC is used. MRCs are known for performing inconsistently and inefficiently. A problem is the inefficient use of iron. Based on chemical principles, one gram of iron could theoretically recover 3.86 grams of silver. In reality, most commercial cartridges have a recovery efficiency of only 0.1 to 0.5 grams of silver per gram of iron in the cartridge. When MRCs are used to recover silver from acidic silver-rich solutions (e.g., fixer), part of the iron is consumed by the acid; as the acidity of the solution increases, the efficiency of the iron decreases. With bleach-fix, the ferric-EDTA consumes iron indirectly as in the following equation:

REACTION 2

Ag + Fe(III)=Ag(I) + Fe(II)-EDTA

The silver recovered in the MRC reacts with ferric-EDTA in the bleach-fix and is dissolved back into solution. Ferric-EDTA becomes ferrous-EDTA. The silver is recovered again downstream as in Reaction 1. The net effect of Reactions 1 and 2 is that metallic iron is consumed by ferric-EDTA, as shown in the following equation:

NET EFFECT OF REACTIONS 1 AND 2

Fe + Fe(III)-EDTA=Fe(II) + Fe(II)-EDTA

A major cause of the inefficient use of iron in MRCs, when they are used with silver-rich photo processing solutions (including color and black/white), is channeling -- a phenomenon where the silver-rich solution creates distinct paths through which it flows, leaving much of the iron unused and reducing the amount of silver recovered. Silver-rich solutions include fixer, bleach-fix, stabilizers from washless processes and low-flow wash water.
Channeling in MRCs occurs for two reasons:
  • Iron fibers (commonly called steel wool) tend to cluster together. Most manufacturing processes are unable to eliminate gaps between iron clusters or iron layers.
  • Silver ions and acids in the silver-rich solutions react and consume iron, thus enlarging the paths through which the silver-rich solution flows. Silver-rich solutions will preferably flow along these paths, offering the silver ions less chance to react with iron, leading to higher silver concentrations in the cartridge effluent.

Due to channeling, much of the initial iron in the MRC remains unused when “breakthrough” occurs. In this study, breakthrough was defined as the point at which the effluent from the MRC contained more than 5 ppm of silver. This number was used because it is a typical compliance limit in municipal sewer ordinances.

The purpose of this study was to find a medium for MRCs that used the iron more efficiently, minimized channeling and improved cartridge performance, when used with silver-rich solutions from photofinishing processes.

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