Journal
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH
Volume 57, Issue 12, Pages 4399-4406Publisher
AMER CHEMICAL SOC
DOI: 10.1021/acs.iecr.7b04820
Keywords
-
Categories
Funding
- National Key Natural Science Foundation of China [U1507203]
- Chinese National Natural Science Foundation [21676273]
- Chinese National Technology Research and Development Program [2015CB251402]
- Chinese High Technology Research and Development Program [2015CB251402, 17-163-12-ZD-001-013-01]
- Youth Innovation Promotion Association, CAS [2016043]
Ask authors/readers for more resources
The separation efficiency of cesium (Cs(I)) and rubidium (Rb(I)) from a synthetic brine solution containing potassium (K(I)) was improved via a kinetics-controlled strategy. Specifically, 4-tert-butyl-2-(alpha-methylbenzyl) phenol (t-BAMBP) dodecane solution was partially saponified by NaOH solution first and then was directly used in extraction without adjusting the pH of the feed solution to exceed 13. Compared to the traditional process, much higher separation factors of Cs(I) and Rb(I) over K(I) (beta(Cs/K) = 1550.7, beta(Rb/K) = 45.2) were gained due to the enhanced kinetics differences during ion exchanges. In addition, the consumption of NaOH was reduced by 70-97%, and a large amount of strong alkaline wastewater was avoided because of the recydability of NaOH saponifying agent. For synthetic brine solution containing high concentration K(I), 99.1% Cs(I) and 86.5% Rb(I) were recovered after three-stage extraction. The novel process showed a bright prospect for the extraction of Cs(I) and Rb(I).
Authors
I am an author on this paper
Click your name to claim this paper and add it to your profile.
Reviews
Recommended
No Data Available