TBP Re, Np U - · PDF fileHWAHAK KONGHAK Vol. 39, No. 1, February, 2001, pp. 36-42 (Journal...
Transcript of TBP Re, Np U - · PDF fileHWAHAK KONGHAK Vol. 39, No. 1, February, 2001, pp. 36-42 (Journal...
HWAHAK KONGHAK Vol. 39, No. 1, February, 2001, pp. 36-42(Journal of the Korean Institute of Chemical Engineers)
TBP Re, Np U
(2000 6 22 , 2000 11 22 )
A Selective-Separation of Re, Np and Residual U from the Simulated Radwaste SolutionContaining the Oxidant of Np by Solvent Extraction with Tributyl Phosphate
Eil Hee Lee, Soo Ho Kim, Jae Gwan Lim, Kwang Wook Kim and Jae-Hyung Yoo
Korea Atomic Energy Research InstituteReceived 22 June 2000; accepted 22 November 2000)
Np 1 g/L NH4VO3 10 Re, Np U
TBP! " #$ %&'( )&' *+ ,- # ./.0 1234. Re, Np, U %&' .05 TBP
678 9:;4 O/A ?8 2 @7 9:;0"[1, 2],
? @ 6A B Am(Americium), Cm(Curium)C6 D
9E F GH IJ ALI(Annual Limit of Intake)KL
:M ICRP(International commission on radiation protection) 30
EN OPQ0" RS T 0" UV W6[3].
XY ZXE HLW9 Tc; TcO4 [, Tc(VII)" \] W^ ,
Np; IV$, V$ _ VI$" \] W0`, 2 M 9 a
" V$", 3 M 79 bcd(disproportionation) ,e EN IV
$ _ VI$ f\g6 hiV W6[4, 5]. gj U; NE kl
U(VI)" \] W6. mno" a" III$" \] W Am, Cm
p Yd$ 7q _ r 7 s T t
u" RS g6[1, 2]. &g vw9 x I U;
yX(fertile material)" 34z {"|
]}YVo" 34 1 u" RSg6.
,z Tc, Np; ~ 9" [, Tc O 8!
,e0" y8! 9, NpE O 8! ,eE y8
36
Re, Np U 37
r,
e
! 9 {"| 63 }o" 8! +
zQp y +zQ %8! 9 3
S 50" [1, 6] W kl PQ0" RS
g6.
Tc, NpE ~0" *Z~, 1~, ~, 2~
n $D ~ 3V W0#[1, 2, 4, 5], 9 TBP(tri-
butyl phosphate) Eg *Z P/6. TBP Eg TcE
; 0#, 'E U(uranium) & Zr(zirconium) 7q
9 Tc 76[7, 8]. gj NpE ; Np(VI) > Np(IV)
Np(V) 0", Np(V) ZO V(V), KMnO4, Ce(IV),
K2Cr2O7 E Yd# HAN(hydroxyl amine nitrate), U(IV), ferrous
sulfamate E 2 $ ; Np(VI)# Np(IV)"
d3 g6. mn# g Yd(KMnO4, K2Cr2O7, Ce(IV) )
E O Np kl Np(VI)" Yd3 70" kl T W
0#, f\ ' W, r Ru(Ruthenium)
; kl RuO4" Yd3 h V`, Ce(Cerium); TBP
; Ce(IV)" 1234 6[9, 10]. &g g Yd
70" Np(VI) Np(V)" 63 2 T 3 J
w S3 W6.
DD TBP Eg Tc, NpE F Cz UE :$
; ( 0.1 M 7)9 Tc, Np Up s 7 fV,
#D 7(raffinate) V \] W0" N
[, UE /: 734 9 a" $ V ,
) U 7Q0" ZO Q; ( 103M /:) \
] O9E ZO ''g / W6. r
W [, HLW" Tc, Np, UE PQ
f/ Kh vw9E 1g /6.
u9 9 1 [11, 12] p 0" Np
Np(VI)" Yd34, 'D V(V)
(NH4VO3) NpE Yd" P/ HLW" Tc, Np m '
\] W U PQ0" T W f/ Kh Q0"
6. m TcE " 1 [11] Tcp dQ
X ` TcE dQ $ CjQ0" *
V W Re(Rhenium :XYZX9 ReO4" \]) P/
6. ; OP NpE Yd$ $ 3 ReE '
0`, 60" 10) *(Np Yd" 1 g/L
NH4VO3 ) 70" Re, Np, UE fp E PQ
NF m % |1 3 V
6.
2.
2-1.
kE*; E v 7 B Re, Npp U, Yd$ III$
E MA(Minor Actinide) _ RE(Rare Earth elements)E i " Nd
(Neodymium) _ Y(Yttrium), %E Cs(Cesium),
%E Sr(Strontium), m *Z f/ 1,9 J 0"
* W Zr, Mo(Molybdenum) _ Fe(Iron) V W
10)" 6. * 3 * k 3(Re _ Mo
kl XY q) _ NpE Yd 2 "
38
E(%) = 100=RD/(1+RD)
S(%) = 100 E
9 R : O/A(volume ratio of organic phase to aqueous phase)
D :)(distribution coefficient : COrg./CAq.)
COrg. :79E < :(mol/L)
CAq. :*79E < :(mol/L)
3.
Re, Np _ UE f _ E ; HLWE 3
]Q d R9 HLW"E E )
(separation factor : DFP/DLLN) 100 7 W[15],
9 %(mixer settler)E + ; 1
+ 70-80% /:, ; v7 ; 60-70% 7,
m 7; 10% $ (7 ) 10/:) V
/Q0" / 6. /;
^ W Q Q; +9 pQ0" T W0
`, +E - E h} Q0" -3
W p$ W6.
3-1.
3-1-1. Re, Np _ U r
Fig. 1 +) 70" NpE Yd(1 g/LE NH4VO3)$
$ 3 30% TBP, O/A=19 XY: d uH Re, Np
_ UE ## W6. ReE Cz NpE Yd
$ v)t XY t O NE VD , X
Y: 1 M D XY: $ u $6$ 1 M
9 - W6. E [11]9 g 5
p XY: 1 M 9 XY : Re T
! TBP :$ T $ W $D, 1 M
79 XY : $ u 7E XY V " B
ReE * ! TBPE :$ 7Q0" -
XY :$ $: b -g 50" }
Re, Np U 39
Eg ,e; E [11, 12]9 g 5p ReE
O (1)p (5) ER, Np _ U;
40
$V ReE r B6. U O XY
: $ u 6 - D - .; m @D ,
5 M9 5% $ fV6. Fig. 1E XY : 2 M
79E U XY : $ u 93-97% /:"
^ Bg6. ,z Np; XY : $ u -` 5 M9
21% /:$ fV6. (2) XY :$ $
T NO3 :$ $V $Vo" -V6.
" ReE PQ 3 U; J$ t0#, Np; 7
fVo" RS g6. R9
B O/A E d /g NpE f -$ V^, I a
ERST w; O/A $34z Npp Re kl $
E kl - 5o" Q S g6.
Fig. 7; XY: _ O/A d uH NpE 6. X
Y: _ O/A $ u - W6. 5 M XY _ O/A=4
9 NpE 6% " - Np fV J
01T W 50" CB6.
Fig. 8; XY: _ O/A d uH ReE 6. X
Y: $ u $`, O/A $ u9 - W6.
+9 -g 5p 1 M 7E XY9 TBP g ReE
r ER, m O/A $ uA ! TBP :
$ ER $ - ^ Bg6. 7E
p" ReE PQ ; 5 M XY, O/A=4 /:z QT
50" +V`, I Re; 80% /: V6.
3-2-3. \ U
Table 2. Separation factor of each element with respected to Np, Re and U
S.F.(DM/DNp) S.F.(DM/DRe) S.F.(DM/DU)
NBA [M] Re/Np Np/Np U/Np HNO3 [M] Re/Re Np/Re U/Re HNO3 [M] Re/U Np/U U/U
0.17 0.5 1.0 13.9 2 1.0 7.7 886 0.01 0.8 0.6 1.00.59 0.7 1.0 15.7 3 1.0 29.4 383 0.05 0.7 0.5 1.01.04 0.9 1.0 16.4 4 1.0 83.8 684 0.1 0.5 0.3 1.01.46 1.4 1.0 25.1 5 1.0 306 690 0.3 0.2 0.1 1.0
Fig. 5. Stripping yields of Np with concentration of normal butyralde-hyde concentration in various O/A ratios.
Fig. 6. Stripping yields of Re, Np and U with nitric acid concentrationat O/A=1.
Fig. 7. Stripping yields of Np with nitric acid concentration in variousO/A ratios.
Fig. 8. Stripping yields of Re with nitric acid concentration in variousO/A ratios.
39 1 2001 2
Re, Np U 41
Fig. 9 O/A=19 XY : d uH Re, Np _ UE f
6. XY : $ u kl - W6. ; XY
:9 TBP g E )$ Q;^[5, 15, 17] B 5
0", 0.05 M HNO39 U, Re _ Np
42
i-
cal
.:
k,
-
ing
m
2,
and
ci-
of
ss-
que-
" pM66. m < E : R
d -,866.
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39 1 2001 2
TBP Re, Np U (2000 6 22 , 2000 11 22 )
A Selective-Separation of Re, Np and Residual U from the Simulated Radwaste Solution Containing t...Eil Hee Lee, Soo Ho Kim, Jae Gwan Lim, Kwang Wook Kim and Jae-Hyung YooKorea Atomic Energy Research Institute (Received 22 June 2000; accepted 22 November 2000)
1. 2. 3. 4.