Modular dynamic simulation for integrated particulate processes by means of tool integration

In this contribution a sequential modular strategy for the dynamic simulation of particulate process flowsheets is presented and the efficiency of the approach is demonstrated by means of an example process for the crystallization of pentaerythritol. The flowsheet of the process consists of a number...

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Veröffentlicht in:Chemical engineering science Jg. 60; H. 7; S. 2069 - 2083
Hauptverfasser: Kulikov, Viatcheslav, Briesen, Heiko, Grosch, Robert, Yang, Aidong, von Wedel, Lars, Marquardt, Wolfgang
Format: Journal Article
Sprache:Englisch
Veröffentlicht: Oxford Elsevier Ltd 01.04.2005
Elsevier
Schlagworte:
Applied sciences
Centrifugation, cyclones
Chemical engineering
Crystallization
Crystallization, leaching, miscellaneous separations
Dynamic simulation
Exact sciences and technology
Heat exchangers and evaporators
Liquid-liquid and fluid-solid mechanical separations
Modular algorithm
Population balance
Sequential modular approach
Tool integration
Dynamic simulation
Tool integration
Population balance
Crystallization
Sequential modular approach
Modular algorithm
Mixer
Crystallizer
Modeling
Flowsheet
Hydrocyclone
Evaporator
Dynamic model
Mathematical model
Unit operation
ISSN:0009-2509, 1873-4405
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Beschreibung
Zusammenfassung:In this contribution a sequential modular strategy for the dynamic simulation of particulate process flowsheets is presented and the efficiency of the approach is demonstrated by means of an example process for the crystallization of pentaerythritol. The flowsheet of the process consists of a number of different unit operations, e.g. evaporator, crystallizer, hydrocyclone, and mixer, which are described by mathematical models of largely varying complexity and structure. A key advantage of the presented sequential modular strategy is that specialized tools can be selected for the modelling and solution of each unit operation in the flowsheet. The tools are then coupled together by means of the tool integration framework CHEOPS in order to capture the overall structure of the flowsheet. In a case study, a startup of a crystallization flowsheet is carried out. As a result, detailed information about the dynamic plantwide process behavior is obtained. The practical relevance of the approach is demonstrated by means of a scenario where potential blocking of the filters following the crystallizer has been analyzed.
Bibliographie:ObjectType-Article-2
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content type line 23
ISSN:0009-2509
1873-4405
DOI:10.1016/j.ces.2004.11.037