Abstract
The process of third plutonium cycle with critically safe multistage mixer-settler is experimentally studied. During the experiment the total level surface of two phases is lower than the critically safe limit. The uranium (plutonium) is extracted through (1 {approx} 9) stages then separated from fission products in (10 {approx} 17) stages of the mixer-settler. The experimental values of U(Pu), HNO{sub 3} profiles in extraction cascade are also obtained. The recovery ratio of U(Pu) is greater than 99.9%, and stage efficiency of extraction section of the mixer-settler is 95%.
Rongzhou, Jiao;
Jianchen, Wang;
Bingren, Liu;
[1]
Sulan, Wang
[2]
- Qinghua Univ., Beijing, BJ (China). Inst. of Nuclear Energy Technology
- Beijing Inst. of Nuclear Engineering (China)
Citation Formats
Rongzhou, Jiao, Jianchen, Wang, Bingren, Liu, and Sulan, Wang.
Experimental research of the process of solvent extraction of Pu with 3A mixer-settler.
China: N. p.,
1993.
Web.
Rongzhou, Jiao, Jianchen, Wang, Bingren, Liu, & Sulan, Wang.
Experimental research of the process of solvent extraction of Pu with 3A mixer-settler.
China.
Rongzhou, Jiao, Jianchen, Wang, Bingren, Liu, and Sulan, Wang.
1993.
"Experimental research of the process of solvent extraction of Pu with 3A mixer-settler."
China.
@misc{etde_10157462,
title = {Experimental research of the process of solvent extraction of Pu with 3A mixer-settler}
author = {Rongzhou, Jiao, Jianchen, Wang, Bingren, Liu, and Sulan, Wang}
abstractNote = {The process of third plutonium cycle with critically safe multistage mixer-settler is experimentally studied. During the experiment the total level surface of two phases is lower than the critically safe limit. The uranium (plutonium) is extracted through (1 {approx} 9) stages then separated from fission products in (10 {approx} 17) stages of the mixer-settler. The experimental values of U(Pu), HNO{sub 3} profiles in extraction cascade are also obtained. The recovery ratio of U(Pu) is greater than 99.9%, and stage efficiency of extraction section of the mixer-settler is 95%.}
place = {China}
year = {1993}
month = {Jun}
}
title = {Experimental research of the process of solvent extraction of Pu with 3A mixer-settler}
author = {Rongzhou, Jiao, Jianchen, Wang, Bingren, Liu, and Sulan, Wang}
abstractNote = {The process of third plutonium cycle with critically safe multistage mixer-settler is experimentally studied. During the experiment the total level surface of two phases is lower than the critically safe limit. The uranium (plutonium) is extracted through (1 {approx} 9) stages then separated from fission products in (10 {approx} 17) stages of the mixer-settler. The experimental values of U(Pu), HNO{sub 3} profiles in extraction cascade are also obtained. The recovery ratio of U(Pu) is greater than 99.9%, and stage efficiency of extraction section of the mixer-settler is 95%.}
place = {China}
year = {1993}
month = {Jun}
}