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排序方式: 共有247条查询结果,搜索用时 15 毫秒
1.
Lewis R. Blackburn Shi-Kuan Sun Laura J. Gardner Ewan R. Maddrell Martin C. Stennett Claire L. Corkhill Neil C. Hyatt 《Journal of the American Ceramic Society》2021,104(7):2937-2951
A series of zirconolite ceramics with composition CaZr1-xThxTi2O7 (Δx = 0.10) were reactively sintered at 1350°C for 20 h, in air (0 ≤ x ≤ 0.60) and 5% H2/N2 (0 ≤ x ≤ 0.40). A sample with composition corresponding to x = 0.20 was also produced by hot isostatic pressing (HIP) at 1300°C and 100 MPa for 4 hours. Th4+ immobilization was most readily achieved under oxidizing conditions, with Th4+ preferentially incorporated within a pyrochlore-structured phase in the range 0.10 ≤ x ≤ 0.50, yet formation of the zirconolite-4M polytype was not observed. We report the novel synthesis of single-phase pyrochlore with nominal composition CaZr0.40Th0.60Ti2O7 when targeting x = 0.60. Th4+ incorporation under reducing conditions produced a secondary Th-bearing perovskite, comprising 24.2 ± 0.6 wt% of the phase assemblage when targeting x = 0.40, alongside 8.8 ± 0.3 wt% undigested ThO2. Under reducing conditions, powder XRD data were consistent with zirconolite adopting the 3T polytype structure. The sample produced by HIP presented a nonequilibrium phase assemblage, yielding a major phase of zirconolite-2M alongside accessory Th4+-bearing phases ThTi2O6, ThO2, and perovskite. These data highlight the efficacy of Th4+ as a Pu4+ surrogate, with implications for the formation of Zr-stabilized Th-pyrochlore phases as matrices for waste with elevated Th4+ content. 相似文献
2.
包头白云鄂博矿中钍资源非常丰富,近年来随着铁矿石的开采,钍被分配到一些产品或废渣中,这不仅造成钍资源的严重浪费,同时分散了的放射性钍给周边环境造成了严重污染。针对目前世界能源紧张的状况,开发新的能源势在必行,钍作为核能发电燃料的研究近年来已有突破,研究开发钍用于核电燃料研究是一项重大和长远的任务。全面分析了包头白云鄂博钍的资源现状及流向,介绍了在生产稀土的同时提取钍化合物、金属钍的工艺研究状况及钍用于核电燃料的研究进展,探讨了钍在核电燃料中的应用可行性及应用前景。 相似文献
3.
通过对国内某企业进口放射性铌铁精矿进行工艺矿物学分析,确定该精矿的主要矿相为烧绿石,同时伴生钛铁矿和白云母,矿石中放射性元素U和Th的含量分别为0.27%和1.03%。针对该铌铁精矿,探索H2SO4-Fe(Ⅲ)、H2SO4-HF-H2O2、H2SO4-HF、H2SO4-HF-H2O2-(NH4)2CO3体系中U和Th的浸出及分离效果,最终确定H2SO4-HF-H2O2-(NH4)2CO3多段浸出工艺能有效实现U和Th的脱除与分离。U、Th的脱除率分别为100%和80%。基于研究提出了铌铁精矿U、Th脱除及分离工艺流程。 相似文献
4.
5.
采用焙烧浸出-萃取沉淀法从白云鄂博稀土精矿中分离稀土和钍,得到最佳焙烧浸出条件为:矿酸比1∶1.5、焙烧时间1 h、焙烧温度200℃、水浸液固比8∶1、水浸时间4 h、水浸温度50℃,最佳条件下CeO2、La2O3、Nd2O3、Pr6O11、Sm2O3和ThO2浸出率分别为80.77%、69.24%、95.71%、76.82%、93.31%和98.13%。采用羧酸类萃取-沉淀剂从浸液中萃取分离稀土和钍,在萃取-沉淀剂皂化度70%、料液pH=3.1、萃取-沉淀剂和钍的摩尔比4∶1的最佳条件下,稀土和钍萃取-沉淀率分别为19%和90%,实现了稀土和钍的有效分离。 相似文献
6.
Marius Tchonang Pokaha Dawid E. Serfontein 《Journal of Nuclear Science and Technology》2018,55(8):843-849
In a previous study using a mixture of thorium and 20 a/o% LEU at 16 gram per fuel sphere heavy metal loading and adjusting the effective fuel enrichment to produce the same amount of cumulative energy per fuel sphere as with the 10 a/o% Low Enriched Uranium (LEU), the maximum Depressurized Loss Of Forced Cooling (DLOFC) temperature was reduced from 2273 to 1925 °C and 1811 °C for a symmetric and asymmetric core, respectively using an once-through-then-out (OTTO) fuelling scheme. This article presents an additional strategy for reducing the maximum DLOFC temperature by placing an optimized distribution of neutron poisons in the central reflector. This strategy produced maximum DLOFC temperatures of 1509 and 1448 °C for the symmetric and the asymmetric cores, respectively. These results are impressive as it means that the less complicated OTTO cycle with its lower capital cost achieved the same cumulative energy produced per fuel sphere than the standard six-pass refuelling scheme and that at substantially lower maximum DLOFC temperatures. Both the addition of the neutron poisons to the central reflector and the creation of a radially asymmetric core resulted in lower burn-ups that had to be reversed by increasing the enrichment of the fuel. 相似文献
7.
《分离科学与技术》2012,47(17):2863-2878
ABSTRACTThe removal of Th(IV) and U(VI) by calcinated, non-calcinated, and methyl grafted SBA-15 (abbreviated as SBA-15, SBA-15-NC and SBA-15-MG, correspondingly) were compared to elucidate the role of pores and surface adsorption sites on SBA-15 adsorbents. It was proposed that the contribution of pores and surface-active sites of SBA-15 increases its higher adsorption capacity with respect to the other examined adsorbents. The kinetic studies revealed that the adsorption and also desorption occurred initially on the surface and then to the pores. Adsorption/desorption of the ions into pores was occurred with slow kinetics. 相似文献
8.
Marius Tchonang Pokaha Dawid E. Serfontein 《Journal of Nuclear Science and Technology》2017,54(5):589-599
This article presents the results for the PBMR-DPP-400, but for a once-through-then-out (OTTO) refueling scheme. An optimization attempt of the axial and radial power profiles is reported. The main aim was to reduce the maximum depressurized loss of forced coolant (DLOFC) temperature by adding thorium to the fuel and making the fuel layout radially asymmetric by placing lower enriched fuel in the inner and higher enriched fuel in the outer fuel flow regions. These measures (1) flattened the peaks in the axial power profiles and thus suppressed the hotspots in the axial DLOFC temperature profiles and (2) ‘pushed’ the power radially outwards, so as to reduce the distance that the decay heat must be evacuated towards the outside of the fuel core. This resulted in a huge reduction in the maximum DLOFC temperature for the OTTO cycle from 2273 to 1811 °C, which is still above the 1600 °C limit but represents a remarkable result. Maximum DLOFC temperature below the 1600 °C limit was obtained by reducing the power output. The results obtained and the proposed strategies for further improvement are applicable to the Chinese HTR-PM and could produce even better results in Prismatic Block Reactors such as the Japanese HTTR. 相似文献
9.
A novel polydentate neutral organophosphorus ligand 1 containing two Ph2P(O)CH2C(O)NH- bidentate moieties connected by a 4, 7, 10 - trioxatridecane spacer through amide nitrogen atoms was synthesized and studied as an extractant for U(VI), Th(IV), and lanthanides(III) ions from HNO3 solutions. The influence of aqueous and organic phases on the extraction efficiency was elucidated and stoichiometry of the complexes extracted was determined. Bis-CMPO ligand 1 was found to possess a higher extraction efficiency towards U(VI), Th(IV), and lanthanides(III) ions than its mono analog diphenylphosphorylacetic acid N-nonylamide 5 and bis-CMPO ligands containing a di- and a triethylene glycol spacers. The values of DU, DTh, and DLn for compound 1 are more than two orders of magnitude higher than those for its mono-CMPO analog 5. 相似文献
10.
M
S Gasser E
E Zaki H
F Aly 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2001,76(12):1267-1272
This paper investigates the transport of Th(IV) ions in nitric acid media through a supported liquid membrane (SLM) impregnated with di‐2‐ethylhexylphosphoric acid (HDEHP) in kerosene using an electric field. The transport was carried out in a three compartment cell fitted with microporous cellulose nitrate (SLM) and cation exchange membrane (Nafion). The effect of different parameters including nitric acid concentration in the feed solution, HDEHP concentration in the membrane, and HCl concentration were studied. The optimal conditions for Th(IV) transport were 0.1 mol dm?3 HDEHP, 10?3 mol dm?3 HNO3 in the feed solution, 1 mol dm?3 HCl in compartment 2 and 1 mol dm?3 HCl in compartment 3 at 25 °C. Under the optimal conditions of Th(IV) transport the recovery factor after 90 min was 0.25 without applying an electrostatic field, compared with 0.9 when the electric field was applied. The effect of electric current on the flux of Th(IV) through the membrane was also studied. The flux increased as the current density increased from 10 to 30 mA cm?2 to reach a maximum value at 30 mA cm?2 (8 × 10?9 g eq cm?2 s?1). The transport percentages of 0.3 g dm?3 Th(IV) in the presence of 0.1 g dm?3 Eu(III) and 1 g dm?3 U(VI) were 66, 84 and 15%, respectively. The determined selectivities of U(VI)–Th(IV) and Th(IV)–Eu(III) were 0.12 and 0.3, respectively, after 90 min. Therefore, the order of selectivity of this system is Eu(III) > Th(IV) > U(VI). © 2001 Society of Chemical Industry 相似文献