2016
DOI: 10.1051/matecconf/20167201106
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Mathematical Modeling of Nonstationary Separation Processes in Gas Centrifuge Cascade for Separation of Multicomponent Isotope Mixtures

Abstract: Abstract. This article presents results of development of the mathematical model of nonstationary separation processes occurring in gas centrifuge cascades for separation of multicomponent isotope mixtures. This model was used for the calculation parameters of gas centrifuge cascade for separation of germanium isotopes. Comparison of obtained values with results of other authors revealed that developed mathematical model is adequate to describe nonstationary separation processes in gas centrifuge cascades for … Show more

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Cited by 6 publications
(7 citation statements)
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“…On one hand, it is desirable that a transient process should be as short as possible, so that a centrifuge can reach the set-up working state as quickly as possible [1]. On the other hand, it is also desirable that a transient process can be utilized to create special separation effects that are otherwise unable to be produced by an ordinary steady state operation [2,3,4], so that components of small abundance can be separated efficiently. No matter what situation it is, a better understanding of the hydraulics as well as the law of separation during transient processes would allow us to have better control and use of transient processes.…”
Section: Introductionmentioning
confidence: 99%
“…On one hand, it is desirable that a transient process should be as short as possible, so that a centrifuge can reach the set-up working state as quickly as possible [1]. On the other hand, it is also desirable that a transient process can be utilized to create special separation effects that are otherwise unable to be produced by an ordinary steady state operation [2,3,4], so that components of small abundance can be separated efficiently. No matter what situation it is, a better understanding of the hydraulics as well as the law of separation during transient processes would allow us to have better control and use of transient processes.…”
Section: Introductionmentioning
confidence: 99%
“…Following a set of experimental determinations, it is advisable to design a mathematical model, thus generating equations with which they can be tracking, analysed and optimized different industrial processes [27][28][29][30][31][32][33][34][35][36][37][38][39][40][41].…”
Section: Introductionmentioning
confidence: 99%
“…In order to create a mathematical model corresponding for study, many works have been made and are presented in the specialized literature [28,29,31,32,34,38,[41][42][43][44], but a rather difficult problem arises when it is desired to identify a mathematical model that corresponds to several studies: -Studies that have been performed at different time intervals or in different locations but at the same time; -Studies conducted by different authors, but which have the same research field.…”
Section: Introductionmentioning
confidence: 99%
“…The usage of these type of models has the disadvantage that they cannot be used for highlighting the effects of the parametric disturbances that occur in the separation plant operation. In [48][49][50][51], the proposed models are designed for a simplified process, near a steady-state working point. These types of models are not complex enough (they do not cover the entire range of the variation domains of the input and output signals that occur in the separation plant operation) for obtaining high-control performances in the case when they are included in automatic control systems.…”
Section: Introductionmentioning
confidence: 99%