LrgpV1, Hal, Checkpoint, bibRecord, 000517

Intensification principle of a new three-phase catalytic slurry reactor. Part II: Eco-efficiency and techno-economic performances

Identifieur interne : 000517 ( Hal/Checkpoint ); précédent : 000516; suivant : 000518

Intensification principle of a new three-phase catalytic slurry reactor. Part II: Eco-efficiency and techno-economic performances

Auteurs : Stephan Machefer [France] ; Laurent Falk [France] ; Fabrice Panthou

Source :

Chemical Engineering and Processing: Process Intensification [ 0255-2701 ] ; 2013-08.

RBID : Hal:hal-01282101

Abstract

In two papers, the concept and the performances of a new continuous intensified reactor named RAPTOR (R) (French acronym for Reactor with Polyvalent Rectilinear Stirred Reactor with Optimised Transfer) are presented. Based on flow, heat and mass transfer characterisations and real hydrogenation experiments, Paper I presented a simple analytical model based on characteristic times that enables to explain the intensified performances compared with a semi-batch stirred reactor and to generalise the operability, rapidity and the flexibility of this minireactor. In Paper II (this article), the model is used to evaluate in a comparative study the eco-efficiency and the techno-economical advantages of a continuous process involving a RAPTOR (R) versus a classical batch process equipped with a stirred reactor. Economical, environmental aspects are considered as well as productivity, safety and process control.

Url:

https://hal.univ-lorraine.fr/hal-01282101

DOI: 10.1016/j.cep.2012.06.005

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Le document en format XML

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<front><div type="abstract" xml:lang="en">In two papers, the concept and the performances of a new continuous intensified reactor named RAPTOR (R) (French acronym for Reactor with Polyvalent Rectilinear Stirred Reactor with Optimised Transfer) are presented. Based on flow, heat and mass transfer characterisations and real hydrogenation experiments, Paper I presented a simple analytical model based on characteristic times that enables to explain the intensified performances compared with a semi-batch stirred reactor and to generalise the operability, rapidity and the flexibility of this minireactor. In Paper II (this article), the model is used to evaluate in a comparative study the eco-efficiency and the techno-economical advantages of a continuous process involving a RAPTOR (R) versus a classical batch process equipped with a stirred reactor. Economical, environmental aspects are considered as well as productivity, safety and process control.</div>
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<abstract xml:lang="en">In two papers, the concept and the performances of a new continuous intensified reactor named RAPTOR (R) (French acronym for Reactor with Polyvalent Rectilinear Stirred Reactor with Optimised Transfer) are presented. Based on flow, heat and mass transfer characterisations and real hydrogenation experiments, Paper I presented a simple analytical model based on characteristic times that enables to explain the intensified performances compared with a semi-batch stirred reactor and to generalise the operability, rapidity and the flexibility of this minireactor. In Paper II (this article), the model is used to evaluate in a comparative study the eco-efficiency and the techno-economical advantages of a continuous process involving a RAPTOR (R) versus a classical batch process equipped with a stirred reactor. Economical, environmental aspects are considered as well as productivity, safety and process control.</abstract>
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Intensification principle of a new three-phase catalytic slurry reactor. Part II: Eco-efficiency and techno-economic performances

Intensification principle of a new three-phase catalytic slurry reactor. Part II: Eco-efficiency and techno-economic performances

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Abstract

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Le document en format XML

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Pour mettre un lien sur cette page dans le réseau Wicri