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1.上海大学 上海 200444
2.中国科学院上海应用物理研究所 嘉定园区 上海 201800
[ "黄丹丹,女,1990 年出生,2012 年毕业于郑州大学,现为硕士研究生,化学专业", "HUANG Dandan, female, born in 1990, graduated from Zhengzhou University in 2012, master student, major in chemistry" ]
付海英, E-mail:fuhaiying@sinap.ac.cn FU Haiying. E-mail:fuhaiying@sinap.ac.cn
王锦花, E-mail:jinhuawang@staff.shu.edu.cn WANG Jinhua. E-mail:jinhuawang@staff.shu.edu.cn
收稿日期:2016-09-26,
修回日期:2016-11-28,
纸质出版日期:2017-01
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黄丹丹, 贾昀澎, 王子豪, 等. 氧化物沉淀-减压蒸馏耦合分离FLiNaK熔盐中的NdF3[J]. 核技术, 2017,40(1):010603
Dandan HUANG, Yunpeng JIA, Zihao WANG, et al. Separation of NdF3 using precipitation-distillation coupled method in FLiNaK molten salt[J]. Nuclear techniques, 2017, 40(1): 010603
黄丹丹, 贾昀澎, 王子豪, 等. 氧化物沉淀-减压蒸馏耦合分离FLiNaK熔盐中的NdF3[J]. 核技术, 2017,40(1):010603 DOI: 10.11889/j.0253-3219.2017.hjs.40.010603.
Dandan HUANG, Yunpeng JIA, Zihao WANG, et al. Separation of NdF3 using precipitation-distillation coupled method in FLiNaK molten salt[J]. Nuclear techniques, 2017, 40(1): 010603 DOI: 10.11889/j.0253-3219.2017.hjs.40.010603.
利用氧化物沉淀-减压蒸馏耦合法研究FLiNaK熔盐体系中氟化物的蒸发行为及稀土Nd的分离。高温下氧化物CaO与稀土氟化物NdF
3
反应形成难溶于熔盐的稀土氧化物,通过减压蒸馏蒸发、收集冷凝FLiNaK熔盐,提高稀土与熔盐的分离度,促进熔盐的回收利用。研究表明,含有NdF
3
(
w
=3%)的FLiNaK熔盐中加入CaO,730℃下反应6 h,
n
(NdF
3
):
n
(CaO)=1:3时NdF
3
的转化率达95%。X射线衍射(X-ray Diffraction,XRD)分析表明生成的Nd
2
O
3
主要沉淀在熔盐的底部。经730℃高温沉淀、930℃熔盐蒸馏,冷凝盐中稀土Nd的去污因子达9.4×10
5
,而未经沉淀处理Nd的去污因子为3.1×10
4
,表明高温沉淀蒸馏耦合法使稀土NdF
3
转化为氧化物Nd
2
O
3
,显著增大稀土与FLiNaK的分离度,提高收集盐的纯度。
Background:
Low pressure distillation is a promising technology for the recovery and purification of carrier salts (LiF-BeF
2
) in the thorium based molten salt reactors (TMSR).
Purpose:
This study aims to compare the separation behavior of NdF
3
before and after adding the oxidant CaO in FLiNaK molten salt.
Methods:
Precipitation-distillation coupled method was employed in purification of molten salt. Then the X-ray Diffractio
n
(XRD) was applied to the analysis of the produced NdF
3
in the molten salt.
Results:
At high temperature
CaO was confirmed to react with NdF
3
and form rare earth oxide Nd
2
O
3
insoluble in molten salt. At 730℃
the conversion rate for Nd was up to 95%. After the precipitation reaction
the separation rate under low pressure distillation was compared with the preceding one. The decontamination factor of Nd was deduced to 9.4×10
5
whilst the value was 3.1×10
4
without adding CaO. Meanwhile
the evaporation rate also was improved after precipitation.
Conclusion:
The combination of the precipitation and distillation treatment is an effective way to achieve the high throughput performance in the salt separation process.
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