Ⅰ Introduction
In order to realize a closed nuclear fuel cycle, the spent fuel discharged from nuclear power reactors must be reprocessed for isolating and recycling the unburned U and Pu generated. In the partition cycle of the improved Purex process used for the reprocessing of spent fuel, both Pu and Np are expected to be separated from U. On the other hand, U purification also involves the removal of Pu and Np. Two methods have been proposed for the separation of Pu and Np from U: one is the reduction of Pu(IV) and Np(VI) to Pu(III) and Np(V), which are unextractable by tri-butyl-phosphate (TBP), the other is to complex Pu(IV) and Np(IV), while U(VI) is unaffected. In the partition cycle, the concentrations of Pu and Np are relative higher, and hence, an appropriate reductant or complexant can effectively separate these nuclides from U. In the U purification cycle, however, the Pu and Np contents are very low; thus, only a complexant would be effective for the decontamination of U from Pu and Np [1,2]. A series of organic ligands, namely, carboxymethylamine, formic acid, acetic acid, butyric acid, pyruvic acid, glycolic acid, formohydroxamic acid, acetohydroxamic acid (AHA), and n-propionyl-hydroxamic acid were proposed and tested. The results showed that AHA is the best [2-6]. Many researchers studied the complexation of AHA with Pu(IV), Np(IV), and U(VI) [2-4,7-11] and found that the stability constants for AHA-Pu(IV) and AHA-Np(IV) are much higher than that for AHA-U(VI). Therefore, AHA can preferentially strip Pu(IV) and Np(IV) from the TBP phase into the aqueous phase, while U(VI) is unaffected. In addition, AHA can rapidly reduce Np(VI) to Np(V); U(VI) is not reduced, but Pu(IV), after initial complex formation, is slowly reduced to Pu(III) [3,12]. As AHA-Pu(IV), AHA-Np(IV), Np(V), and Pu(III) are unextractable by TBP, Pu and Np can be well separated from U by AHA [5,13-18]. AHA is composed of C, H, O, and N, and it can be completely incinerated to NO2 and CO2. Since no solid waste is generated by the addition of AHA [16], it is expected to be useful for the reprocessing of spent fuel. However, AHA might suffer from radiation damage during its use, which would affect its efficiency, and the resulting radiolytic products may hinder effective separation. Karraker [19] studied the radiolysis of AHA in HNO3 at doses up to 11 kGy, which was estimated from the spent fuel to be reprocessed, and found that radiation decomposed a minor fraction of AHA compared to the loss by hydrolysis, and that AHA radiolysis showed weak dependence on both the HNO3 concentration and the absorbed dose. In his study, the residual AHA content was analyzed by the light absorption of an Fe (III)-AHA complex. However, he compared the effect of radiation damage on AHA based on the light absorption value of the diluted samples and not the residual concentration of AHA. As the irradiated samples were diluted 100 to 400 times, even a slight change in absorption may cause a significant difference in the AHA concentration, and the absorbance value obtained will not be representative of the AHA concentration; hence, these results are not reliable. In this study, the radiolysis of AHA is monitored based on the change in the AHA concentration, and the radiolytic product of AHA is also reported. These results are expected to serve as an important reference for the application of AHA in the reprocessing of spent fuel.
Ⅱ Experiment
2.1 Reagent
AHA was supplied by Aldrich Chemical Company, and its purity was 98%. Two kinds of standard gas mixtures were supplied by Shanghai Institute of Measurement and Testing Technology: one was composed of 2.50% hydrogen, 1.00% carbon monoxide, 1.00% carbon dioxide, 0.30% methane, 0.01% ethane, 0.01% ethene, and 95.18% nitrogen; the other contained 3.00% nitrous oxide and 97.00% nitrogen.
2.2 Main equipment and accessories
A 3.7 × 1015 Bq 60Co-γ ray irradiator was supplied by Shanghai Institute of Applied Physics, Chinese Academy of Sciences. A T90 UV-VIS spectrophotometer was supplied by Beijing Purkinje General Instrument Co. Ltd. An ion chromatograph (research-style) was obtained from Switzerland Metrohm Co. Ltd. A GC900A gas chromatograph and a packed column with 5 Å molsieve (2 m × 3 mm) were supplied by Shanghai Ke Chuang Chromatograph Instruments Co. Ltd. A capillary column with aluminum oxide (50 m × 0.53 mm) was supplied by Lanzhou Institute of Chemistry and Physics, Chinese Academy of Sciences.
2.3 Sample preparation, irradiation, pretreatment, and analysis
0.2 mol·L-1 AHA solutions containing different concentrations of HNO3 were prepared as follows. A certain amount of AHA was put in a beaker, which was then placed in an ice-water bath. A certain amount of 0.5 mol·L-1 HNO3 was slowly dropped into the beaker with stirring, and then, a certain amount of slightly diluted HNO3 was added. The solution was transferred to a 100-mL measuring flask to a constant volume. Thus, solutions in which the AHA concentration was 0.2 mol·L-1 and the HNO3 concentration was 0.2, 0.5, 1.0, and 2.0 mol·L-1 were prepared. Four milliliters of each solution was placed in 7-mL glass vials, which were sealed with a sealing machine. The samples were irradiated by 60Co γ-ray to 5, 10, 15, 20, and 25 kGy, and the absorbed doses were monitored by dichromate dosimeters. Control samples were used for comparison of the radiation effect on the loss of AHA by hydrolysis as well as on the amount of radiolytic product. The gases evolved from the irradiated AHA solutions were tested by gas chromatography for the analysis of H2, N2 O, CH4, and C2 H6. The irradiated AHA solutions and control samples were neutralized by KOH solution and then diluted to the suitable concentrations. Finally, these pretreated samples were tested by ultraviolet-visible spectrophotometry and ion chromatography for the analysis of AHA, HCOOH, and HNO2.
2.4 Analysis of AHA and its radiolytic products
Quantitative analysis of AHA was performed by ultraviolet-visible spectrophotometry. 2.7, 5.3, 8.0, and 10.7 m mol L-1 standard AHA solutions were prepared using high-purity water. 1.00 milliliter of each solution was placed in a 10 mL measuring flask, to which 3.00 mL FeCl3 solution (10 wt %) and 4.00 mL CCl3 COOH solution (2.5 wt %) were separately added. Then, water was added to constant volume, and the solutions were shaken well. The reference solution was prepared in the same manner as the standard AHA solutions but without AHA. These standard AHA solutions were tested at 502 nm by using an ultraviolet-visible spectrophotometer. The response curve for AHA was obtained from the AHA concentrations and the corresponding absorbance. The irradiated AHA solutions and control samples were neutralized by KOH solutions and diluted to suitable concentrations. These pretreated samples were tested by using the ultraviolet-visible spectrophotometer. From the response curve for AHA and the absorbance of the diluted samples, the residual AHA concentrations in the samples were calculated. H2, N2 O, CH4, and C2 H6 were analyzed by gas chromatography. For H2 analysis, a 5 Å molsieve packed column was used, and the column temperature was 80 ℃; a thermal conductivity detector (TCD) was employed, and its temperature was 110 ℃. The carrier gas was Ar, with a flow rate of 10 mL min-1. N2 O analysis was conducted using a packed shincarbon T column and a TCD detector. H2 was used as the carrier gas, and its flow rate was 25 mL· min-1. The column temperature was programmed as follows: initial temperature, 100℃; initial isothermal period, 7 min; programmed heating rate, 35 ℃·min-1; final temperature, 220 ℃; and final isothermal period, 1 min. The TCD temperature was 120 ℃. CH4 and C2 H6 were analyzed using a PLOT Al2 O3 column and a flame ionization detector (FID). The carrier gas was N2, and its flow rate was 19 mL·min-1. The column temperature was 40 ℃, and the FID temperature was 110 ℃. CH3 COOH and HNO2 were analyzed by ion chromatography with an electric conductivity detector, using a METROSEP A SUPP 5-250 column. The eluent was a solution containing 3.2 mmol·L-1Na2 CO3 and 1.0 mmol·L-1NaHCO3, and its flow rate was 0.7 mL·min-1.
2.5 Formulae used in the paper
The hydrolysis rate of AHA is defined as follows: hydrolysis rate = (C0 -Cc )/C0 ×100%, where C0 is the original AHA concentration and Cc is the AHA concentration in the control sample. The radiolysis rate of AHA is defined by the equation: radiolysis rate=(Cc -Ci )/Cc ×100%, where Ci is the AHA concentration in the irradiated sample. The volume fraction of the gas product is calculated as follows: if the response curve equation of a component is y = ax + b, the X axis is the injected volume of the standard gas mixture, and the Y axis is the corresponding peak area of the component. Then, the volume fraction of the component is calculated by the following formula: volume fraction= (A-b)c/ae, where A is the component peak area in the gas chromatogram of the gas sample, c is the volume fraction of the component in the standard gas mixture, and e is the injected volume of sample gas.
Ⅲ Results and Discussion
3.1 Radiolysis of AHA in HNO3 solution
As AHA can complex with Fe(III) in an acidic solution to yield a colored product, it can be analyzed by ultraviolet-visible spectrophotometry [15]. The response curve for AHA is y=114.38x+0.0142 (concentration range: 2.70-10.7 m·mol L-1), and the correlation coefficient (R2) is 0.9994. The AHA concentration in control samples decreases drastically with increasing HNO3 concentration. When the HNO3 concentration is 0, 0.2, 0.5, 1.0, and 2.0 mol·L-1, the hydrolysis rate of AHA is 8.20%, 23.1%, 41.2%, 66.2%, and 85.9% respectively, indicating that the rate increases with the HNO3 concentration. This result is consistent with that reported by Taylor [20] and Tkac [10]. In an acidic solution, AHA hydrolyzes to acetic acid and hydroxylamine:
As the time lag among sample preparation, irradiation, and neutralization is very long (about 9h), this observation cannot be used to elucidate the hydrolysis of AHA employed in the advanced Purex process. In the separation of Pu and Np from U by countercurrent liquid-liquid extraction, the residence time is about 30 min; if the separation occurs in the centrifugal contactor, the residence time is much shorter. We have studied the hydrolysis of AHA in HNO3 at different times [21]. At 0.2 mol·L-1AHA, with 0.2, 0.5, 1.0, and 2.0 mol·L-1 HNO3, the hydrolysis rate of AHA at 0.5h is 2.40, 5.30, 7.60, and 8.40 respectively; thus, the hydrolysis of AHA in 0.2-2.0 mol·L-1HNO3 would not be drastic. In addition, fast complexation of AHA with a metal leads to slower hydrolysis and stabilization of AHA in solution [10], so the hydrolysis of AHA will not affect its application in the separation of Pu and Np from U. Fig.1 illustrates the radiolysis rate of AHA as a function of dose.
-201802/1001-8042-29-02-011/alternativeImage/1001-8042-29-02-011-F001.jpg)
Fig.1 shows that the radiolysis rate of AHA is 6.63%-77.5 % in AHA solution irradiated to 5-25 kGy, and it increases with the dose and HNO3 concentration. Karraker [19] reported that AHA radiolysis shows weak dependence on both HNO3 concentration and absorbed dose, and this differs from our experimental results. When the dose is increased fivefold, from 5 to 25 kGy, the radiolysis rate increases 1.3-2.8 times. When the HNO3 concentration is increased fivefold, from 0.2 to 1.0 mol·L-1, the radiolysis rates increases 2.3-4.2 times. Thus, the effect of HNO3 concentration on the radiolysis of AHA is stronger than that of the dose. Water radiolyzes to produce ·OH, e-1aq,·H, and so on:
-201802/1001-8042-29-02-011/media/1001-8042-29-02-011-M001.jpg)
·OH may react with HNO3 by H abstraction to form ·NO3 [22]:
When using 0.2-2.0 mol·L-1 HNO3, most of the acid dissociates to form NO3-. γ-ray may react directly with HNO3 and NO3- to produce ·NO3 [23]:
-201802/1001-8042-29-02-011/media/1001-8042-29-02-011-M002.jpg)
-201802/1001-8042-29-02-011/media/1001-8042-29-02-011-M003.jpg)
·OH and ·NO3 are oxidative radicals, and they may react with AHA as follows [24]:
Since the concentrations of ·OH and ·NO3 increase with dose (Eqs.2, 4-5) and the ·NO3 concentration increases with HNO3 concentration (Eqs.3-5), the radiolysis rate increases with both dose and HNO3 concentration.
3.2 Radiolytic product of AHA
HNO3 ionizes to produce H+, and e-1aq can react with H+ to form H:
-201802/1001-8042-29-02-011/media/1001-8042-29-02-011-M004.jpg)
H· may react with AHA to form H2:
eaq- and ·H· may also react with NO3- generated from the ionization of HNO3, as follows [22]:
Two ·NO2 radicals may react with each other to form N2 O4, which can react with water to produce HNO2:
The C-C bond in the excited AHA molecule may be broken as follows [25]:
-201802/1001-8042-29-02-011/media/1001-8042-29-02-011-M005.jpg)
·CH3 may react with AHA by H abstraction to form CH4, or two ·CH3 radicals may also react with each other to produce C2 H6:
Two CH3 CONHO· radicals may react with each other to produce CH3 CON=O [26]:
-201802/1001-8042-29-02-011/media/1001-8042-29-02-011-M006.jpg)
CH3 CON=O may hydrolyze to form acetic acid and nitroxyl [27-28]:
-201802/1001-8042-29-02-011/media/1001-8042-29-02-011-M007.jpg)
Two nitroxyls can react with each other to generate N2 O:
Thus, the main radiolytic product of AHA in HNO3 may be H2, N2 O, CH4, C2 H6, CH3 COOH, and HNO2.
3.2.1 H2 generated by the radiolysis of AHA in HNO3
H2 was analyzed by gas chromatography using a packed 5 Å molsieve column and a TCD detector [29]. The response curve of H2 is y=2297.8x+48.87 (volume range: 0.100-1.20 mL), and R2 is 1.000. The volume fraction of H2 as a function of dose is shown in Fig.2.
-201802/1001-8042-29-02-011/alternativeImage/1001-8042-29-02-011-F002.jpg)
Fig.2 shows that the volume fraction of H2 evolved from the AHA solutions irradiated with a dose of 5-25 kGy is (1.30-11.8) × 10-3. The H2 volume fraction increases with the dose but decreases with increased HNO3 concentration. H2 is produced by the reaction of H· and AHA (Eq.9). H· is generated from the radiolysis of H2 O (Eq.2), and it may also be produced by the reaction of H+ and eaq- (Eq.8). As the concentrations of H· and eaq- increase with the dose, the H2 volume fraction also increases with increasing dose. Upon the addition of HNO3, NO3- can react with ·H and eaq- (Eqs.10-11), so that the ·H concentration is reduced; hence, the volume fraction of H2 decreases with increased HNO3 concentration.
3.2.2 N2 O generated from the radiolysis of AHA in HNO3
We used gas chromatography with a packed shincarbon T column and a TCD detector to analyze N2 O. The response curve of N2 O is y=220.83x–17.67 (volume range: 0.020-3.00 mL), and R2 is 0.9933. The volume fraction of N2 O as a function of dose is shown in Fig.3.
-201802/1001-8042-29-02-011/alternativeImage/1001-8042-29-02-011-F003.jpg)
Fig.3 shows that the volume fraction of N2 O produced from AHA solutions irradiated up to a dose of 5-25 kGy is (3.29 -16.2) × 10-2. The N2 O volume fraction increases with the dose and with the HNO3 concentration when the acid concentration is ≤ 0.5 mol·L-1. The dependence of the N2 O volume fraction on the HNO3 concentration is not obvious when the acid concentration is higher than 0.5 mol·L-1. ·OH, ·NO3, ·H, and ·CH3 react with AHA to form CH3 CONHO· (Eqs. 6-7, 9, 14), and two CH3 CONHO· radicals react to produce CH3 CON=O (Eq.16). After hydrolysis, the HNO produced generates N2 O (Eqs.17-18). Since the concentrations of ·OH, ·NO3, ·H, and ·CH3 increase with the dose (Eqs.2-5, 13), the volume fraction of N2 O also increases with the dose. On the other hand, the higher the HNO3 concentration, the higher is the concentration of ·NO3, CH3 CONHO·, CH3 CON=O, and HNO (Eqs.3-5, 7, 16-17). N2 O is produced by the reaction between two moieties of HNO (Eq.18), and thus, the volume fraction of N2 O increases with HNO3 concentration. However, as discussed above, the radiolysis rate of AHA increases with HNO3 concentration, and the reduction of AHA concentration causes a decrease in the N2 O content (Eqs. 7, 16-17). At higher HNO3 concentration, The increase in N2 O content resulting from the increased HNO3 concentration is balanced by the decrease in N2 O content due to the reduced AHA concentration; consequently, the volume fraction of N2 O changes very slightly at high HNO3 concentrations.
3.3.3 CH4 and C2 H6 generated from radiolysis of AHA in HNO3
CH4 and C2 H6 were analyzed by gas chromatography with a PLOT Al2 O3 column and a FID detector [21]. The response curves of CH4 and C2 H6 are y=242.7x+193.8 and y=25.56x-171.3, respectively. The volume range is 2.0 to 200.0 μL, and the corresponding R2values are 0.9998 and 0.9956. The volume fractions of CH4 and C2 H6 evolved from AHA solutions irradiated up to 5-25 kGy are (1.90-47.4) × 10-5 and (0.200-1.00) × 10-5, respectively; the volume fraction of CH4 is much higher than that of C2 H6. CH4 is produced by the reaction of ·CH3 and AHA (Eq.14), while C2 H6 is generated by the reaction of two ·CH3 radicals (Eq.15). As the concentration of AHA exceeds that of ·CH3, the volume fraction of CH4 is much higher than that of C2 H6.
Fig.4 shows that the volume fraction of CH4 increases with the dose and with the HNO3 concentration at HNO3≤1.0 mol·L-1. When the HNO3 concentration increases from 1.0 to 2.0 mol·L-1, there is no obvious change in the CH4 volume fraction. CH4 is generated by the reaction of ·CH3 and AHA (Eq.14). The ·CH3 concentration increases with the dose, so the volume fraction of CH4 also increases with the dose. ·CH3 may react with HNO3 as below:
-201802/1001-8042-29-02-011/alternativeImage/1001-8042-29-02-011-F004.jpg)
Thus, the volume fraction of CH4 increases with the HNO3 concentration. However, the radiolysis rate of AHA also increases with the HNO3 concentration, as shown above, and the reduction of AHA concentration leads to a decrease in the CH4 content (Eq.14). At higher HNO3 concentration, the reduction in CH4 content caused by the decrease of AHA concentration is balanced by the increase in CH4 content resulting from the increase of HNO3 concentration; hence, the volume fraction of CH4 changes slightly at high HNO3 concentrations. The volume fractions of N2 O, H2, CH4, and C2 H6 have the following relationship: N2 O ≈ 10 H2 . ≈ 150 CH4 ≈ 7500 C2 H6.
3.3.4 CH3 COOHand HNO2 generated by radiolysis of AHA in HNO3
Under alkaline conditions, CH3 COOH and HNO2 can be converted into CH3 COO- and NO2-, which can be analyzed by ion chromatography. The response curves of CH3 COOH and HNO2 are y=872.97x and y=3766.1x, respectively. The concentration range for CH3 COOH is 0.169-1.70 m·mol L-1, and that for HNO2 is 0.0217-0.435 m·mol L-1. The R2 values for the response curves of CH3 COOH and HNO2 are 0.9998 and 0.9984, respectively.
Fig.5 shows that the CH3 COOH concentration is (4.64-19.7) × 10-2 mol·L-1 in AHA solutions irradiated up to 5-25 kGy. The CH3 COOH concentration increases markedly with HNO3 concentration and slightly with the dose. ·OH, ·NO3, ·H, and ·CH3 react with AHA to form CH3 CONHO· (Eqs.6-7, 9, 14); these radicals react with each other to produce CH3 CON=O (Eq.16), which in turn hydrolyzes to produce CH3 COOH (Eq.17). Since the concentration of ·OH, ·NO3, ·H, and ·CH3 increases with the dose (Eqs.2-5, 13), the CH3 COOH concentration also increases with the dose. When the HNO3 concentration is high, the concentration of ·NO3, CH3 CONHO·, and CH3 CON=O (Eqs.3-5, 7, 16) also increases, as does the concentration of CH3 COOH (Eq. 17). For this reason, the CH3 COOH concentration increases with HNO3 concentration.
-201802/1001-8042-29-02-011/alternativeImage/1001-8042-29-02-011-F005.jpg)
Fig.6 shows that the HNO2 concentration is (0.321-4.80) × 10-3 mol·L-1 in AHA solutions irradiated at a dose of 5-25 kGy; the concentration of HNO2 increases with increasing concentration of HNO3. When the HNO3 concentration is ≤1.0 mol·L-1, the dependence of the HNO2 concentration on the dose is not obvious. At a HNO3 concentration of 2.0 mol·L-1, the HNO2 concentration increases with the dose at lower dose levels, reaching the maximum value at 15 kGy, and then decreases with a further increase in the dose but changes only slightly beyond 20 kGy. Some papers [27,29,30] reported that AHA can react with HNO2 and can scavenge HNO2 and stabilize Pu(III) and Np(V); thus an additional holding reductant is unnecessary[17]. The above mentioned results show that a significant concentration of HNO2 exists in the irradiated AHA-HNO3 solution; this means that AHA cannot effectively destroy HNO2, so a holding reductant should be used when AHA is applied for the separation of Pu and Np from U.
-201802/1001-8042-29-02-011/alternativeImage/1001-8042-29-02-011-F006.jpg)
Ⅳ Conclusion
AHA is a potential complexant and reductant used in the separation of Pu and Np from U in the advanced Purex process for the reprocessing of spent fuel. The radiation stability of AHA in HNO3 depends on the absorbed dose and HNO3 concentration, but the effect of the latter is greater than that of the former. At a dose of 5-25 kGy, 0.2 mol·L-1 AHA is recommended for use in HNO3 with concentrations lower than 0.5 mol·L-1, where the radiolytic rate of AHA is lower than 29%. The use of AHA with 2.0 mol·L-1 HNO3 should be avoided, as the radiolytic rate of AHA is higher than 57%. The main gaseous products are N2 O and H2, and the volume fraction of N2 O is higher than that of H2. The main liquid products are CH3 COOH and HNO2, and the concentration of the former is much higher than that of the latter. As HNO2 will affect the stability of Pu(III) and Np(V), a holding reductant should be applied to scavenge HNO2 when AHA is used for the separation Pu and Np from U. The effect of the holding reductant on the destruction of HNO2, as well as on the stabilization of AHA and the radiolytic product of AHA in HNO3, will be studied in the near future.
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