Recovery of cobalt from spent copper leach solution using continuous ion exchange

Recovery of cobalt and lithium from spent lithium ion batteries using organic citric acid as leachant.

In this work, a hydrometallurgical process based on leaching is applied to recover cobalt and lithium from spent lithium ion batteries (LIBs). Citric acid and hydrogen peroxide are introduced as leaching reagents and the leaching of cobalt and lithium with a solution containing C(6)H(8)O(7) x H(2)O is investigated. When both C(6)H(8)O(7) x H(2)O and H(2)O(2) are used an effective recovery of Li...

Removal of Copper from Aqueous Solution by Ion Exchange Resins

Efficient removal of cobalt(II) ion from aqueous solution using amide-functionalized metal-organic framework

In this study, an amide-functionalized metal-organic framework, namely TMU-24 was selected to adsorb Co(II) from wastewater with an adsorption capacity of 500 mg. g-1 in less than 20 minutes in neutral pH (pH=7). The effect of diverse parameters such as adsorbent dosage, competitive ions, and contact time on the adsorption process was investigated to find the optimal amounts of them. Also, the ...

Ion exchange investigation for recovery of uranium from acidic pregnant leach solutions

In the face of depletion of fossil resources, the development of nuclear power in the world is inevitable. Poland is one of the few developed countries, which does not have a nuclear power plant [1]. Therefore, The programme of Polish nuclear energy has recently been implemented. Simultaneously, the interest in domestic uranium ores, which fi rst appeared in the fi ftieth of the previous centur...

Conversion of Soybean Oil into Ion Exchange Resins: Removal of Copper (II), Nickel (II), and Cobalt (II) Ions from Dilute Aqueous Solution Using Carboxylate- Containing Resin

An ion-exchange resin containing carboxylic acid groups was prepared by reaction of epoxidized soybean oil with triethylene tetramine, followed by hydrolysis of glycerides by using sodium hydroxide solution. The cation exchange capacity of the resins was determined to be 3.50 mequiv/g. The adsorption capacity for Cu , Ni , and Co on the obtained resin at pH 5.0 was found to be 192, 96, and 78 m...