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Ion Exchange Resins - Industrial Processes

 

Uranium Recovery

 

 

Uranium is recovered from leach liquors as anionic complex, the two most frequently encountered being the sulfate (from acid leach liquors) and the carbonate (from alkaline leach liquors) complexes:

 

UO2(SO4)34- and UO2(CO3)34-

 

Specially conceived strong base anion exchangers are used to fix these anionic complexes in presence of high concentrations of other anions such as sulfates, carbonates or ferric sultates. Both fixed bed or continuous systems are used for both loading and elution steps. The resin characteristics for the various systems may vary, for example in particle size, depending on the specific operating conditions employed. The operating capacity depends on the feed solution composition.

 

Elution of the uranium from the resin is practiced today using three main systems:

 

In the case of carbonate leaching, only NH4NO3 or NaCl can be used as eluants. Acid elution can not be used because the acid will react with the carbonates to form CO2. The quantity of eluant in a fixed system is of the order of 5 BV for nitrate or 10 BV for sulfuric acid or 15 BV for NaCl solutions. With continuous elution systems this quantity of eluants can be reduced.

 

Product Portfolio

 

For sampling, pricing, availability or more information please contact your Rohm and Haas representative.

 

Ambersep™ 400 SO4

For acid leach (fixed bed, continuous system, Nimcix, Porter).

Ambersep™ 4400 HCO3

For alkaline leach.
Ambersep™ 920U Cl For acid leach (RIP, fixed bed, continuous systems). High silica tolerance.
Ambersep™ 920U SO4 For acid leach (RIP, fixed bed, continuous systems). High silica tolerance.
Ambersep™ 920UHC SO4 For acid leach (RIP, fixed bed, continuous systems). High silica tolerance.

 

 

 

 

 

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Product Data Sheets

 

Ambersep™ 400 SO4

Ambersep™ 4400 HCO3
Ambersep™ 920U Cl
Ambersep™ 920U SO4

Ambersep™ 920UHC SO4

 

Events

 

16-18 September 2009

 

MiningWorld Central Asia 2009

Almaty, Kazakhstan - Booth: B48

 

Presentation:

September 17, 2009 from 2- 3 pm in seminar room 16B, pavilion 9B

 

Ion Exchange Resins in Hydrometallurgy

 

Speaker: Areski Rezkalla