58 research outputs found

    Regenerated Uranium Separation in Matched Abundance Ratio Cascade with Additional Product Flow

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    This paper addresses known methods used to purify regenerated uranium in single and double cascades. A new method for separating regenerated uranium has been developed that enables a significant reduction of the concentration of 232,234U in the additional product flow. Matched abundance ratio cascades (Mβˆ—-cascades) with different key components and additional product flow are used in the new method. Main product flow of the Mβˆ—-cascade contains low enriched regenerated uranium. It can be used for reactor fuel production. Purified product can be enriched in the ordinary cascade in compliance with the requirements of ASTM C 996-10 set for isotopes 232,234U in low enriched commercial uranium, which is usually produced from the natural one. Computer experiment based on the new method has been performed. The experiment shows that the best cascade with the maximum flow of the enriched purified product is Mβˆ—-cascade with key components 232,236U. Β© Published under licence by IOP Publishing Ltd

    ΠžΡ‡ΠΈΡΡ‚ΠΊΠ° Ρ€Π΅Π³Π΅Π½Π΅Ρ€ΠΈΡ€ΠΎΠ²Π°Π½Π½ΠΎΠ³ΠΎ ΡƒΡ€Π°Π½Π° Π² каскадах с ΠΎΠ±ΠΎΠ³Π°Ρ‰Π΅Π½ΠΈΠ΅ΠΌ 235U Π΄ΠΎ 5 %

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    На основС Π²Ρ‹Ρ‡ΠΈΡΠ»ΠΈΡ‚Π΅Π»ΡŒΠ½ΠΎΠ³ΠΎ экспСримСнта исслСдована очистка Ρ€Π΅Π³Π΅Π½Π΅Ρ€ΠΈΡ€ΠΎΠ²Π°Π½Π½ΠΎΠ³ΠΎ ΡƒΡ€Π°Π½Π° Π² каскадС, ΠΎΠΏΡ‚ΠΈΠΌΠΈΠ·ΠΈΡ€ΠΎΠ²Π°Π½Π½ΠΎΠΌ Π½Π° Π·Π°Π΄Π°Π½Π½ΡƒΡŽ ΠΊΠΎΠ½Ρ†Π΅Π½Ρ‚Ρ€Π°Ρ†ΠΈΡŽ 232U, со смСщСниСм Ρ‚ΠΎΡ‡ΠΊΠΈ ΠΏΠΎΠ΄Π°Ρ‡ΠΈ питания Π² сторону ΠΎΡ‚Π±ΠΎΡ€Π°. ΠžΠΏΡ€Π΅Π΄Π΅Π»Π΅Π½Ρ‹ ΠΏΠ°Ρ€Π°ΠΌΠ΅Ρ‚Ρ€Ρ‹ каскада с ΠΎΠ±ΠΎΠ³Π°Ρ‰Π΅Π½ΠΈΠ΅ΠΌ 235U Π² ΠΎΡ‚Π±ΠΎΡ€Π΅ ΠΌΠ΅Π½Π΅Π΅ 5 %, ΠΎΠ±Π΅ΡΠΏΠ΅Ρ‡ΠΈΠ²Π°ΡŽΡ‰ΠΈΠ΅ Π² ΠΎΡ‚Π²Π°Π»ΡŒΠ½ΠΎΠΌ ΠΏΠΎΡ‚ΠΎΠΊΠ΅ практичСски ΠΏΠΎΠ»Π½ΡƒΡŽ очистку ΠΎΡ‚ 232U ΠΏΡ€ΠΈ ΠΊΠΎΠ½Ρ†Π΅Π½Ρ‚Ρ€Π°Ρ†ΠΈΠΈ 235U, Π±Π»ΠΈΠ·ΠΊΠΎΠΉ ΠΊ ΠΏΠΈΡ‚Π°Π½ΠΈΡŽ. РассмотрСны возмоТности ΠΎΠ΄Π½ΠΎΠ²Ρ€Π΅ΠΌΠ΅Π½Π½ΠΎΠΉ очистки ΠΎΡ‚ 234U ΠΏΡ€ΠΈ ΡƒΠΌΠ΅Π½ΡŒΡˆΠ΅Π½ΠΈΠΈ извлСчСния Ρ€Π΅Π³Π΅Π½Π΅Ρ€ΠΈΡ€ΠΎΠ²Π°Π½Π½ΠΎΠ³ΠΎ ΡƒΡ€Π°Π½Π° Π² ΠΎΡ‚Π²Π°Π» каскада. Для сниТСния ΠΊΠΎΠ½Ρ†Π΅Π½Ρ‚Ρ€Π°Ρ†ΠΈΠΈ 236U Π² Π½ΠΈΠ·ΠΊΠΎΠΎΠ±ΠΎΠ³Π°Ρ‰Π΅Π½Π½ΠΎΠΌ ΡƒΡ€Π°Π½Π΅, ΠΏΡ€ΠΎΠΈΠ·Π²ΠΎΠ΄ΠΈΠΌΠΎΠΌ ΠΈΠ· ΠΎΡ‡ΠΈΡ‰Π΅Π½Π½ΠΎΠ³ΠΎ Ρ€Π΅Π³Π΅Π½Π΅Ρ€ΠΈΡ€ΠΎΠ²Π°Π½Π½ΠΎΠ³ΠΎ ΡƒΡ€Π°Π½Π°, ΠΏΡ€Π΅Π΄Π»ΠΎΠΆΠ΅Π½Ρ‹ Π΄ΠΎΠΏΠΎΠ»Π½ΠΈΡ‚Π΅Π»ΡŒΠ½Ρ‹Π΅ ΠΎΠΏΠ΅Ρ€Π°Ρ†ΠΈΠΈ разбавлСния ΠΈ обогащСния

    Π­Ρ„Ρ„Π΅ΠΊΡ‚ΠΈΠ²Π½ΠΎΡΡ‚ΡŒ использования ΠΏΠΎΡ‚Π΅Π½Ρ†ΠΈΠ°Π»ΠΎΠ² раздСлСния ΠΏΡ€ΠΈ ΠΎΠΏΡ‚ΠΈΠΌΠΈΠ·Π°Ρ†ΠΈΠΈ каскадов

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    РассмотрСна оптимизация каскадов ΠΏΠΎ ΠΊΡ€ΠΈΡ‚Π΅Ρ€ΠΈΡŽ максимума Ρ€Π°Π·Π΄Π΅Π»ΠΈΡ‚Π΅Π»ΡŒΠ½ΠΎΠΉ способности элСмСнтов, опрСдСляСмой с ΠΏΠΎΠΌΠΎΡ‰ΡŒΡŽ ΠΏΠΎΡ‚Π΅Π½Ρ†ΠΈΠ°Π»Π° раздСлСния. На основС Π²Ρ‹Ρ‡ΠΈΡΠ»ΠΈΡ‚Π΅Π»ΡŒΠ½ΠΎΠ³ΠΎ экспСримСнта ΠΈ сравнСния с ΠΌΠΈΠ½ΠΈΠΌΠΈΠ·Π°Ρ†ΠΈΠ΅ΠΉ суммарного ΠΏΠΎΡ‚ΠΎΠΊΠ° установлСно, Ρ‡Ρ‚ΠΎ нСзависимо ΠΎΡ‚ эффСкта обогащСния Π½Π° ступСнях каскада для Π±ΠΈΠ½Π°Ρ€Π½Ρ‹Ρ… смСсСй ΠΏΡ€ΠΈΠΌΠ΅Π½ΠΈΠΌΡ‹ Ρ€Π°Π·Π½Ρ‹Π΅ Ρ„ΠΎΡ€ΠΌΡ‹ ΠΏΠΎΡ‚Π΅Π½Ρ†ΠΈΠ°Π»ΠΎΠ², Π²ΠΊΠ»ΡŽΡ‡Π°ΡŽΡ‰ΠΈΠ΅ ΠΈΡ… Π·Π°Π²ΠΈΡΠΈΠΌΠΎΡΡ‚ΡŒ ΠΎΡ‚ коэффициСнтов раздСлСния. ΠŸΡ€ΠΈ ΠΌΠ½ΠΎΠ³ΠΎΠΊΠΎΠΌΠΏΠΎΠ½Π΅Π½Ρ‚Π½ΠΎΠΌ Ρ€Π°Π·Π΄Π΅Π»Π΅Π½ΠΈΠΈ Π²Ρ‹Π±ΠΎΡ€ ΠΏΠΎΡ‚Π΅Π½Ρ†ΠΈΠ°Π»Π° раздСлСния зависит ΠΎΡ‚ ΠΈΠ·ΠΎΡ‚ΠΎΠΏΠ½ΠΎΠΉ смСси ΠΈ особСнностСй процСсса

    ΠžΠΏΡ‚ΠΈΠΌΠΈΠ·Π°Ρ†ΠΈΡ каскада Ρ†Π΅Π½Ρ‚Ρ€ΠΈΡ„ΡƒΠ³ для раздСлСния ΠΌΠ½ΠΎΠ³ΠΎΠΊΠΎΠΌΠΏΠΎΠ½Π΅Π½Ρ‚Π½ΠΎΠΉ смСси ΠΈΠ·ΠΎΡ‚ΠΎΠΏΠΎΠ²

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    Π Π°Π·Ρ€Π°Π±ΠΎΡ‚Π°Π½ ΠΌΠ΅Ρ‚ΠΎΠ΄ расчСта ΠΎΠΏΡ‚ΠΈΠΌΠ°Π»ΡŒΠ½Ρ‹Ρ… ΠΏΠ°Ρ€Π°ΠΌΠ΅Ρ‚Ρ€ΠΎΠ² каскада Π³Π°Π·ΠΎΠ²Ρ‹Ρ… Ρ†Π΅Π½Ρ‚Ρ€ΠΈΡ„ΡƒΠ³ для раздСлСния ΠΌΠ½ΠΎΠ³ΠΎΠΊΠΎΠΌΠΏΠΎΠ½Π΅Π½Ρ‚Π½ΠΎΠΉ смСси ΠΈΠ·ΠΎΡ‚ΠΎΠΏΠΎΠ². ΠŸΡ€Π΅Π΄Π»ΠΎΠΆΠ΅Π½Π° ΡƒΠ½ΠΈΠ²Π΅Ρ€ΡΠ°Π»ΡŒΠ½Π°Ρ Π²Ρ‹Ρ‡ΠΈΡΠ»ΠΈΡ‚Π΅Π»ΡŒΠ½Π°Ρ схСма, ΠΏΠΎΠ·Π²ΠΎΠ»ΡΡŽΡ‰Π°Ρ ΠΎΠΏΡ‚ΠΈΠΌΠΈΠ·ΠΈΡ€ΠΎΠ²Π°Ρ‚ΡŒ каскад ΠΏΡ€ΠΈ Ρ€Π°Π·Π½Ρ‹Ρ… критСриях ΠΎΠΏΡ‚ΠΈΠΌΠΈΠ·Π°Ρ†ΠΈΠΈ. На основС Π²Ρ‹Ρ‡ΠΈΡΠ»ΠΈΡ‚Π΅Π»ΡŒΠ½ΠΎΠ³ΠΎ экспСримСнта исслСдованы особСнности ΠΌΠΈΠ½ΠΈΠΌΠΈΠ·Π°Ρ†ΠΈΠΈ суммарного ΠΏΠΎΡ‚ΠΎΠΊΠ° каскада ΠΏΡ€ΠΈ Π·Π°Π΄Π°Π½Π½Ρ‹Ρ… Π²Π½Π΅ΡˆΠ½ΠΈΡ… ΠΏΠΎΡ‚ΠΎΠΊΠ°Ρ… ΠΈ ΠΊΠΎΠ½Ρ†Π΅Π½Ρ‚Ρ€Π°Ρ†ΠΈΠΈ Ρ†Π΅Π»Π΅Π²ΠΎΠ³ΠΎ ΠΈΠ·ΠΎΡ‚ΠΎΠΏΠ°. Показано, Ρ‡Ρ‚ΠΎ ΠΏΡ€ΠΈ смСщСнии Ρ‚ΠΎΡ‡ΠΊΠΈ ΠΏΠΎΠ΄Π°Ρ‡ΠΈ питания каскада ΠΎΡ‚Π½ΠΎΡΠΈΡ‚Π΅Π»ΡŒΠ½ΠΎ ΠΎΠΏΡ‚ΠΈΠΌΡƒΠΌΠ°, ΠΎΠ±Π΅ΡΠΏΠ΅Ρ‡ΠΈΠ²Π°ΡŽΡ‰Π΅Π³ΠΎ минимально Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΠ΅ число Ρ†Π΅Π½Ρ‚Ρ€ΠΈΡ„ΡƒΠ³, ΠΌΠΎΠΆΠ½ΠΎ сущСствСнно ΠΈΠ·ΠΌΠ΅Π½ΠΈΡ‚ΡŒ ΠΊΠΎΠ½Ρ†Π΅Π½Ρ‚Ρ€Π°Ρ†ΠΈΡŽ Π½Π΅Ρ†Π΅Π»Π΅Π²Ρ‹Ρ… ΠΈΠ·ΠΎΡ‚ΠΎΠΏΠΎΠ² Π² ΠΎΡ‚Π±ΠΎΡ€Π΅ ΠΈ ΠΎΡ‚Π²Π°Π»Π΅ каскада. Вакая ΠΎΡΠΎΠ±Π΅Π½Π½ΠΎΡΡ‚ΡŒ ΠΎΠΏΡ‚ΠΈΠΌΠΈΠ·Π°Ρ†ΠΈΠΈ ΠΌΠΎΠΆΠ΅Ρ‚ Π±Ρ‹Ρ‚ΡŒ эффСктивно использована для очистки Ρ€Π΅Π³Π΅Π½Π΅Ρ€ΠΈΡ€ΠΎΠ²Π°Π½Π½ΠΎΠ³ΠΎ ΡƒΡ€Π°Π½Π° ΠΎΡ‚ 232U

    OPTIMIZATION OF MULTISTREAM CASCADES WITH A GIVEN NUMBER OF GAS CENTRIFUGES FOR PURIFICATION OF REGENERATED URANIUM HEXAFLUORIDE FROM 232, 234, 236U

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    method for optimization of multistream cascades for purification of regenerated ura-nium from even isotopes is improved by using several types of stages with a given number of gas centrifuges. The operating modes of the stages have been determined by the artificial bee colony algorithm

    Reprocessed uranium purification in cascades with 235U enrichment to 5%

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    Reprocessed uranium purification in cascades with 235U enrichment to 5%

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    The purification of reprocessed uranium in a cascade optimized to a prescribed 232U concentration with the feed flow displaced toward the product flow is investigated by means of a computational experiment. The parameters of a cascade with 235U enrichment <5% in the product, which ensures almost complete purification from 232U with 235U concentration close to that in the feed flow, are determined. The possibilities for simultaneous purification from 234U with reduction of reprocessed uranium extraction into the waste flow are examined. Additional dilution and enrichment operations are proposed in order to decrease the 236U concentration in low-enrichment uranium produced from purified reprocessed uranium. Β© 2013 Springer Science+Business Media New York

    Optimization of the Cascade with Two Additional Product Flows for the Simultaneous Concentration of Intermediate Molybdenum Isotopes

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    A technique has been developed for optimizing multiflow cascades to obtain highly concentrated intermediate molybdenum isotopes. A computational experiment was carried out to separate a mixture of molybdenum isotopes. Various cases for the separation of molybdenum isotopes in cascades with large step separation coefficients corresponding to gas centrifuges were considered. It is shown that using of the bee swarm optimization has an advantage over the Hook-Jeeves method. Β© 2020 American Institute of Physics Inc.. All rights reserved

    Production of highly concentrated intermediate molybdenum isotopes in optimal cascade with two additional product flows

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    The problem of highly concentrated molybdenum isotopes production in multiflow cascades is considered. A method of the cascade with two additional product flows optimization has been developed. Two components intermediate in weight are concentrated simultaneously in those flows. The optimization problem is solved using a variation of the partial flow cuts of the cascade stages with large separation coefficients. The optimization criterion is the minimum of the stage total feed flow while ensuring a given concentration of isotopes. A computational experiment was carried out to separate a mixture of molybdenum hexafluoride. The experiment demonstrated the features of intermediate components concentrating in additional product flows of the cascade. Β© 2020 Published under licence by IOP Publishing Ltd

    Separation of boron isotopes in optimal cascade of uniflow gas centrifuges

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    Was considered a problem of an optimization of concurrent gas centrifuges for separation of Boron isotopes in form of trifluoride BF3. As the criteria was used a minimum of total number of gas centrifuges upon the given external parameters of the cascades' scheme. The method is based on the analytical relationships for the flows of stages, received under approximating minimization of the total feed flow. Conducted cascade calculations showed that it is possible to obtain BF3 with enrichment up to 99.9 % of 10B in the selection and up to 0.1 % in the waste, which is equivalent to 99.9 % of 11B. Β© 2020 Published under licence by IOP Publishing Ltd
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