This article describes the radical copolymerization of styrene (St) and n-butylmethacrylate (BMA) in a counter-rotating twin-screw extruder. In order to investigate the effect of the polymer melt viscosity on the working domain in reactive extrusion, the copolymer was crosslinked with different amounts of divinylbenzene (DVB). Crosslinking of the polymer resulted in a higher polymer melt viscosity. It was demonstrated that not only the product properties but also the process characteristics were strongly influenced by the addition of divinylbenzene to the reaction mixture. The product properties changed as expected: more crosslink agent led to a higher molecular weight or an increase in gel fraction, and a much higher melt viscosity of the ...
To understand the performance of multicomponent reactions in extruders, the mixing mechanism in the ...
The self-wiping co-rotating twin-screw extruder was studied as a reactor for two polymerizations in ...
The self-wiping co-rotating twin-screw extruder was studied as a reactor for two polymerizations in ...
This article describes the radical copolymerization of styrene (St) and n-butylmethacrylate (BMA) in...
This article describes the radical copolymerization of styrene (St) and n-butylmethacrylate (BMA) in...
This article describes the radical copolymerization of styrene (St) and n-butylmethacrylate (BMA) in...
This article describes the copolymerization of styrene-butylmethacrylate (St-BMA) and the homopolyme...
This article describes the copolymerization of styrene–butylmethacrylate (St-BMA) and the homopolyme...
This article describes the influence of the polymerization rate on the working domain of a counter-r...
This article describes the influence of the polymerization rate on the working domain of a counter-r...
The research of this thesis describes the use of an extruder as a reactor for the improvement of the...
This article describes the influence of the polymerization rate on the working domain of a counter-r...
To understand the performance of multicomponent reactions in extruders, the mixing mechanism in the ...
The self-wiping co-rotating twin-screw extruder was studied as a reactor for two polymerizations in ...
The self-wiping co-rotating twin-screw extruder was studied as a reactor for two polymerizations in ...
This article describes the radical copolymerization of styrene (St) and n-butylmethacrylate (BMA) in...
This article describes the radical copolymerization of styrene (St) and n-butylmethacrylate (BMA) in...
This article describes the radical copolymerization of styrene (St) and n-butylmethacrylate (BMA) in...
This article describes the copolymerization of styrene-butylmethacrylate (St-BMA) and the homopolyme...
This article describes the copolymerization of styrene–butylmethacrylate (St-BMA) and the homopolyme...
This article describes the influence of the polymerization rate on the working domain of a counter-r...
This article describes the influence of the polymerization rate on the working domain of a counter-r...
The research of this thesis describes the use of an extruder as a reactor for the improvement of the...
This article describes the influence of the polymerization rate on the working domain of a counter-r...
To understand the performance of multicomponent reactions in extruders, the mixing mechanism in the ...
The self-wiping co-rotating twin-screw extruder was studied as a reactor for two polymerizations in ...
The self-wiping co-rotating twin-screw extruder was studied as a reactor for two polymerizations in ...