trpo process
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2018 ◽  
Vol 29 (4) ◽  
Author(s):  
Wu-Hua Duan ◽  
Tiao-Xiang Sun ◽  
Jian-Chen Wang


2017 ◽  
Vol 314 (1) ◽  
pp. 221-229 ◽  
Author(s):  
Wenbing Li ◽  
Wuhua Duan ◽  
Taoxiang Sun ◽  
Changjian Liu ◽  
Jianchen Wang ◽  
...  


2012 ◽  
Vol 291 (3) ◽  
pp. 717-723 ◽  
Author(s):  
Meng Wei ◽  
Xuegang Liu ◽  
Jing Chen


2011 ◽  
Vol 292 (2) ◽  
pp. 697-704 ◽  
Author(s):  
Shaowei Li ◽  
Jing Chen ◽  
Jianchen Wang


2009 ◽  
Vol 51 (2) ◽  
pp. 313-318 ◽  
Author(s):  
Wuhua Duan ◽  
Qin Cheng ◽  
Xiuzhu Zhou ◽  
Jiazhen Zhou


Author(s):  
Meng Wei ◽  
Xuegang Liu ◽  
Jing Chen

To reduce the long-term risk of the high-level liquid waste (HLLW) and the waste disposal cost, transuranium (TRU) elements should be removed from HLLW. A so-called TRPO process has been developed by Chinese scientists to partition HLLW. In this process, the extractant, trialkyl phosphine oxide (TRPO), is able to extract TRU elements into organic phase completely, which makes the treatment and disposal of raffinate HLLW much easier. However, the treatment of extracted TRU elements in organic phase, in return, becomes new troublesome issue. Generally, there are three promising ways to treat the extracted TRU elements: (1)transmutation; (2)conditioning; (3)recycling U+Pu in Purex-TRPO Integrated Process. In any of the three ways, the back extraction agents and processes play significant roles. In this paper, the investigations on back extraction agents for TRU elements, such as TTHA, DTPA, AHA, HEDPA, DOGA, and carbonates are introduced. The corresponding back extraction processes and experimental results are reviewed.



2007 ◽  
Vol 273 (1) ◽  
pp. 65-71 ◽  
Author(s):  
Ping Zhang ◽  
Hairong Wang ◽  
Jianchen Wang ◽  
Jing Chen
Keyword(s):  


2007 ◽  
Vol 273 (1) ◽  
pp. 103-107 ◽  
Author(s):  
Wuhua Duan ◽  
Jianchen Wang ◽  
Jing Chen ◽  
Jiazhen Zhou ◽  
Xiuzhu Zhou




2001 ◽  
Vol 89 (3) ◽  
Author(s):  
W. Jianchen ◽  
S. Chongli

The crown ether strontium extraction(CESE) process for partitioning strontium from HLLW was studied. A hot test was carried out in a counter current mode with genuine HLLW by using a miniature centrifugal contactor set. 0.1 mol/L DCH18C6 in 1-octanol was used as extractant. The feed solution was the HLLW raffinate of TRPO process after removing TRU elements. Acidity of the feed was 1.45 mol/L HNO



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