Model-based development of optimal reaction concepts for plant wide process intensification

Beitrag bei einer Tagung


Details zur Publikation

Autor(en): Peschel A, Jörke A, Freund H, Sundmacher K
Verlag: Elsevier BV
Jahr der Veröffentlichung: 2012
Band: 31
Seitenbereich: 150-154
ISSN: 1570-7946


Abstract


The oxygen based production of ethylene oxide, one of the most important bulk chemicals, is considered as an example. Here, advanced cooling and distributed dosing of oxygen is identified as best reaction concept from an economical and technological point of view. Applying this innovative reaction concept, the production costs of an average sized plant are reduced by 1.35 Mio $/a, and the CO2 emissions are decreased by 2.7.10(4) t/a compared to an optimized reference case. This general method provides a first step towards more economical and greener processes.



FAU-Autoren / FAU-Herausgeber

Freund, Hannsjörg Prof. Dr.
Professur für Katalytische Reaktoren und Prozesstechnik


Autor(en) der externen Einrichtung(en)
Max-Planck-Institut für Dynamik komplexer technischer Systeme / Max Planck Institute for Dynamics of Complex Technical Systems


Zitierweisen

APA:
Peschel, A., Jörke, A., Freund, H., & Sundmacher, K. (2012). Model-based development of optimal reaction concepts for plant wide process intensification. (pp. 150-154). Elsevier BV.

MLA:
Peschel, Andreas, et al. "Model-based development of optimal reaction concepts for plant wide process intensification." Elsevier BV, 2012. 150-154.

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Zuletzt aktualisiert 2018-10-08 um 05:24