This article describes the influence of the polymerization rate on the working domain of a counter-rotating twin-screw extruder used as a polymerization reactor. The rate of polymerization was varied by changing the maleic anhydride (Mah) content in the feed, which consisted of styrene, n-butylmethacrylate, and maleic anhydride. It appeared that the Mah content influenced the operating window of the extruder. Higher Mah percentages resulted in higher throughputs and a decreased dependence on the extruder parameters. On the basis of these results, a new theory concerning reactive extrusion was developed, which resulted in a diagram that is useful in optimizing the extruder, when it is used as polymerization reactor. In addition to the effect...
This article describes the radical copolymerization of styrene (St) and n-butylmethacrylate (BMA) in...
The goal of the research was to examine the possibilities of this type of extruder as a polymerizati...
Numerical models are useful to study the behaviour of the extruder as a polymerization reactor. With...
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...
This article describes the influence of the polymerization rate on the working domain of a counter-r...
This article describes the copolymerization of styrene-butylmethacrylate (St-BMA) and the homopolyme...
Numerical models are useful to study the behaviour of the extruder as a polymerization reactor. With...
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...
The bulk polymerization of n-butylmethacrylate was investigated in a counter-rotating twin screw ext...
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...
The goal of the research was to examine the possibilities of this type of extruder as a polymerizati...
Numerical models are useful to study the behaviour of the extruder as a polymerization reactor. With...
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...
This article describes the influence of the polymerization rate on the working domain of a counter-r...
This article describes the copolymerization of styrene-butylmethacrylate (St-BMA) and the homopolyme...
Numerical models are useful to study the behaviour of the extruder as a polymerization reactor. With...
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...
The bulk polymerization of n-butylmethacrylate was investigated in a counter-rotating twin screw ext...
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...
The goal of the research was to examine the possibilities of this type of extruder as a polymerizati...
Numerical models are useful to study the behaviour of the extruder as a polymerization reactor. With...