We present a new micro reactor concept which is suitable for investigations of heterogeneously catalyzed liquid phase reactions. In the set-up two reactants are mixed in a commercially available interdigital micro mixer. The outlet of the micro mixer is connected to a modular micro reactor that consists of stacked plates. Each plate contains a milled meandering channel filled with catalyst beads. By using a variable number of plates the residence time can be manipulated and thus adjusted for a specific task. The synthesis of butyl acetate is considered as a model reaction since it has been investigated in detail in conventional reaction systems. In a first step, some experimental results of the heterogeneously catalyzed reaction are present...
For enzyme-catalyzed reactions, batch processes using stirred tank reactors are the state-of-the-art...
The principle of a discontinuously operated chromatographic reactor was studied experimentally and t...
We successfully demonstrated a novel process intensification concept enabled by the development of m...
We present a new micro reactor concept which is suitable for investigations of heterogeneously catal...
One of the most promising approaches for intensification of chemical processes is process integratio...
A microplant concept is introduced for the analysis of homogeneously and heterogeneously catalyzed l...
A miniaturized-plant concept is presented for the analysis of homogeneous and heterogeneous acid-cat...
A miniaturized-plant concept is presented for the analysis of homogeneous and heterogeneous acid-cat...
Reactive chromatography, i.e., coupling chemical reaction and selective sorption, allows us to drive...
Reactive chromatography is a special topic in chemical reaction engineering, consisting of the combi...
The article is focused on the aspects of using micro-catalytic pulse reactors for studying gas-phase...
A discontinuously operated chromatographic reactor and a reaction calorimeter were used to study exp...
The research carried out within this thesis studied the hydrodynamics, reaction applications and sca...
Developing continuous enzymatic process, especially when a two-phase medium is required, remains now...
The esterification reaction of acetic acid with n-butanol in a continuous catalytic distillation sys...
For enzyme-catalyzed reactions, batch processes using stirred tank reactors are the state-of-the-art...
The principle of a discontinuously operated chromatographic reactor was studied experimentally and t...
We successfully demonstrated a novel process intensification concept enabled by the development of m...
We present a new micro reactor concept which is suitable for investigations of heterogeneously catal...
One of the most promising approaches for intensification of chemical processes is process integratio...
A microplant concept is introduced for the analysis of homogeneously and heterogeneously catalyzed l...
A miniaturized-plant concept is presented for the analysis of homogeneous and heterogeneous acid-cat...
A miniaturized-plant concept is presented for the analysis of homogeneous and heterogeneous acid-cat...
Reactive chromatography, i.e., coupling chemical reaction and selective sorption, allows us to drive...
Reactive chromatography is a special topic in chemical reaction engineering, consisting of the combi...
The article is focused on the aspects of using micro-catalytic pulse reactors for studying gas-phase...
A discontinuously operated chromatographic reactor and a reaction calorimeter were used to study exp...
The research carried out within this thesis studied the hydrodynamics, reaction applications and sca...
Developing continuous enzymatic process, especially when a two-phase medium is required, remains now...
The esterification reaction of acetic acid with n-butanol in a continuous catalytic distillation sys...
For enzyme-catalyzed reactions, batch processes using stirred tank reactors are the state-of-the-art...
The principle of a discontinuously operated chromatographic reactor was studied experimentally and t...
We successfully demonstrated a novel process intensification concept enabled by the development of m...