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<title>Eugeny Y. Kenig</title>
<copyright>Copyright (c) 2012  All rights reserved.</copyright>
<link>http://works.bepress.com/eugeny_kenig</link>
<description>Recent documents in Eugeny Y. Kenig</description>
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<title>Modeling Fluid Separation Processes Using a Complementary Approach</title>
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<pubDate>Tue, 30 Mar 2010 14:25:57 PDT</pubDate>
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	<p>Modern fluid separation processes occur under very complex conditions. As a result, their modeling is usually based on severe assumptions and experimentally estimated gross parameters. On the other hand, the process optimization can only be achieved with reasonable model accuracy, whereas the process rates should be considered in a rigorous way, with respect to both transport phenomena and chemistry.</p>
<p>Depending on the complexity of process fluid dynamics, different modeling ways can be applied, their rigor and complexity stretching over a wide range. Among these ways are a direct application of the equations of fluid dynamics, the hydrodynamic analogy method and the rate-based approach. These methods are complementary in the sense that, together, they are able to govern both simple and very complex process fluid dynamic conditions. Moreover, there is also another complementarity between the different approaches, namely, they can be applied in combination, for instance, by estimating process parameters by a more rigorous method and delivering them to the less rigorous one. In this contribution, the complementary modeling is discussed in detail and illustrated with case studies.</p>

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<author>Eugeny Y. Kenig </author>


<category>Chemical and reaction engineering</category>

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<title>Advanced Modeling of Reactive Separation Units with Structured Packings</title>
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<pubDate>Tue, 30 Mar 2010 14:25:56 PDT</pubDate>
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	<p>Reactive separations combining mass transfer with simultaneous chemical reactions within a single column unit provide an important synergistic effect and bring about several advantages. The influence of column internals in reactive separations increases significantly, because these internals have to enhance both separation and reaction and maintain a sound balance between them. To solve this problem, a novel generation of column internals with enhanced mass transfer performance and low pressure drop has been created. Among them, corrugated packings of the regular type or structured packings have gained a wide acceptance.</p>
<p>This paper gives a state-of-the-art review of the structured packings modeling methods, focusing on two innovative and particularly promising approaches. The first of them is based on the application of CFD, whereas the second one employs the idea of hydrodynamic analogy between complex and simple flow patterns. Both approaches are illustrated with several case studies.</p>

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<author>E. Y. Kenig</author>


<category>Chemical process modeling and simulation</category>

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