## Abstract A new model has been developed in order to predict pressure drop and gas fraction of industrial fixed bed reactor operated in downward bubbly flow. The mechanistic approach proposed by Attou and Ferschneider (1999) has been followed. In this approach, mass and momentum balances are solv
โฆ LIBER โฆ
CFD modelling and experimental validation of pressure drop and flow profile in a novel structured catalytic reactor packing
โ Scribed by H.P.A. Calis; J. Nijenhuis; B.C. Paikert; F.M. Dautzenberg; C.M. van den Bleek
- Book ID
- 108309866
- Publisher
- Elsevier Science
- Year
- 2001
- Tongue
- English
- Weight
- 552 KB
- Volume
- 56
- Category
- Article
- ISSN
- 0009-2509
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