Interaction between Hydrodynamics and Chmical Reaction Rate in Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor. II. Applications.
-
- Cantero Hector J.
- Instituto de Desarrollo Tecnológico para la Industria Química, INTEC
-
- Baltanás Miguel A.
- Instituto de Desarrollo Tecnológico para la Industria Química, INTEC
-
- Grau Ricardo J.
- Instituto de Desarrollo Tecnológico para la Industria Química, INTEC
Bibliographic Information
- Other Title
-
- Interaction between Hydrodynamics and Chemical Reaction Rate in Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor:2.Applications
Search this article
Abstract
The behavior of an isothermal, vertical tube reactor in a dispersed bubble flow environment in either upflow, downflow or upflow-downflow configurations is examined, using the performance indicators defined in Part I. The hydrogenation of a coalescent organic system, like the one found in the mild hydrogenation process of soybean oil, is taken as a reference system. The likelihood of the axial changes of the local gas-slurry mass transfer efficiency and, then, of the controlling regimes of the process rate is discussed. Further effects of the configuration on the conversion of the liquid reactant, the unconverted mass of the gas phase, and the pressure drop are also analyzed.
Journal
-
- JOURNAL OF CHEMICAL ENGINEERING OF JAPAN
-
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 33 (1), 25-31, 2000
The Society of Chemical Engineers, Japan
- Tweet
Details 詳細情報について
-
- CRID
- 1390001204564991872
-
- NII Article ID
- 130000020426
-
- NII Book ID
- AA00709658
-
- COI
- 1:CAS:528:DC%2BD3cXhsFGjs74%3D
-
- ISSN
- 18811299
- 00219592
-
- NDL BIB ID
- 5284082
-
- Text Lang
- en
-
- Data Source
-
- JaLC
- NDL
- Crossref
- CiNii Articles
-
- Abstract License Flag
- Disallowed