Zobrazeno 1 - 10
of 37
pro vyhledávání: '"van Wpm Wim Swaaij"'
Publikováno v:
Chemical Engineering Science, 66(12), 2764-2773. Elsevier
An earlier developed hydrodynamic model describing dense gas-solid two phase flow has been used to study the bubble formation process at a single orifice. A systematic experimental and theoretical study has been conducted to investigate the effect of
Publikováno v:
Chemical engineering science, 60(22), 5982-5990. Elsevier
Chemical Engineering Science, 60(22), 5982-5990. Elsevier
Chemical Engineering Science, 60(22), 5982-5990. Elsevier
In this paper the concept of micro-fluidized beds is introduced. A cylindrical quartz reactor with an internal diameter of only 1 mm is used for process conditions up to Click to view the MathML source and 244 bar. In this way, fast, safe, and inhere
Publikováno v:
Chemical engineering science, 58(2), 457-472. Elsevier
Chemical Engineering Science, 58(2), 457-472. Elsevier
Chemical Engineering Science, 58(2), 457-472. Elsevier
A model describing hydrodynamics of a filtering slurry system is presented, incorporating axial effects in the entire slurry volume as well as radial effects at the axial positions where a filter is present. It is demonstrated that the model is capab
Publikováno v:
Chemical engineering science, 57(5), 833-854. Elsevier
A new reactor concept is studied for highly endothermic heterogeneously catalysed gas phase reactions at high temperatures with rapid but reversible catalyst deactivation. The reactor concept aims to achieve an indirect coupling of energy necessary f
Publikováno v:
Chemical Engineering Science. 57:855-872
The new reactor concept for highly endothermic reactions at elevated temperatures with possible rapid catalyst deactivation based on the indirect coupling of endothermic and exothermic reactions in reverse flow, developed for irreversible reactions i
Publikováno v:
Chemical Engineering Science, 56(4), 1517-1524. Elsevier
Chemical engineering science, 56(4), 1517-1524. Elsevier
ISCRE-16
Chemical engineering science, 56(4), 1517-1524. Elsevier
ISCRE-16
A new reverse flow reactor is developed where endothermic reactants (propane dehydrogenation) and exothermic reactants (fuel combustion) are fed sequentially to a monolithic catalyst, while periodically alternating the inlet and outlet positions. Upo
Publikováno v:
Chemical engineering science, 56, 571-578. Elsevier
Chemical Engineering Science, 56(2), 571-578. Elsevier
ISCRE-16
Chemical Engineering Science, 56(2), 571-578. Elsevier
ISCRE-16
A two-dimensional multi-fluid Eulerian CFD model with closure laws according to the kinetic theory of granular flow has been applied to study the influence of the coefficient of restitution on the hydrodynamics of dense gas-fluidised beds. It is demo
Publikováno v:
Powder Technology, 109(1-3), 41-48. Elsevier
Powder technology, 109(1-3), 41-48. Elsevier
Powder technology, 109(109), 41-48. Elsevier
Powder technology, 109(1-3), 41-48. Elsevier
Powder technology, 109(109), 41-48. Elsevier
A hard-sphere discrete particle model of a gas-fluidised bed was used in order to simulate segregation phenomena in systems consisting of particles of different sizes. In the model, the gas-phase hydrodynamics is described by the spatially averaged N
Publikováno v:
Chemical Engineering Science, 55(17), 3385-3395. Elsevier
Chemical engineering science, 55(17), 3385-3395. Elsevier
Chemical engineering science, 55(17), 3385-3395. Elsevier
This paper highlights the development of a new ensemble correlation, multiphase flow PIV technique. The particular approach discussed in this paper is a straightforward extension of single-phase PIV and one of the major advantages of the technique is
Publikováno v:
Chemical engineering science, 55(18), 3739-3742. Elsevier
Chemical Engineering Science, 55(18), 3739-3742. Elsevier
Chemical Engineering Science, 55(18), 3739-3742. Elsevier
The film model and penetration model predict different influences of binary interactions and thermodynamic non-idealities on gas–liquid mass transfer. Therefore, in case of concentrated systems, as often encountered in extraction and distillation p