A mathematical model of a continuous polycondensation reactor used in the finishing stages is developed. This axial dispersion model predicts the directions in which mixing, and other process and operational variables, will influence the progress of polycondensation. The available pilot plant data have been compared with the model predictions. In view of the neglect of the side reactions in our model, the comparison is only approximate but appears reasonable. The analysis developed is used to highlight certain critical design considerations
A mathematical model is developed for the molecular weight distribution (IMWD) of a polyethylene ter...
In the industry when someone wants to modify the way a chemical reactor works; it is not possible to...
A comprehensive mathematical model for the finishing stages of polyethylene terephthalate (PET) synt...
A mathematical model for the continuous prepolymerization of BHET to PET, carried out in a series of...
A simplified approach to polycondensation kinetics has been used to develop engineering models for t...
This research study predicted the conversion and yield pattern for the polymerization of propylene t...
A new comprehensive model for solid-state polycondensation (SSP) of polyethylene terephthalate (PET)...
The formation of polyethylene terephthalate (PET) has been modeled to have reactions with monofuncti...
The polycondensation step of poly(ethylene terephthalate) (PET) formation is assumed to include vari...
This work presents the analysis of a slurry polymerization stirred tank reactor for the production o...
The second stage of a batch polyethylene terephthalate (PET) reactor with a kinetic scheme consistin...
Poly(ethylene terephthalate) (PET) formation in homogeneous, continuous-flow-stirred tank reactors (...
An improved two-phase model has been developed for a wiped film (third stage) polyester reactor. The...
A mathematical model has been developed to compute the molecular weight distribution (MWD) in the po...
A mathematical model is developed for the molecular weight distribution (IMWD) of a polyethylene ter...
A mathematical model is developed for the molecular weight distribution (IMWD) of a polyethylene ter...
In the industry when someone wants to modify the way a chemical reactor works; it is not possible to...
A comprehensive mathematical model for the finishing stages of polyethylene terephthalate (PET) synt...
A mathematical model for the continuous prepolymerization of BHET to PET, carried out in a series of...
A simplified approach to polycondensation kinetics has been used to develop engineering models for t...
This research study predicted the conversion and yield pattern for the polymerization of propylene t...
A new comprehensive model for solid-state polycondensation (SSP) of polyethylene terephthalate (PET)...
The formation of polyethylene terephthalate (PET) has been modeled to have reactions with monofuncti...
The polycondensation step of poly(ethylene terephthalate) (PET) formation is assumed to include vari...
This work presents the analysis of a slurry polymerization stirred tank reactor for the production o...
The second stage of a batch polyethylene terephthalate (PET) reactor with a kinetic scheme consistin...
Poly(ethylene terephthalate) (PET) formation in homogeneous, continuous-flow-stirred tank reactors (...
An improved two-phase model has been developed for a wiped film (third stage) polyester reactor. The...
A mathematical model has been developed to compute the molecular weight distribution (MWD) in the po...
A mathematical model is developed for the molecular weight distribution (IMWD) of a polyethylene ter...
A mathematical model is developed for the molecular weight distribution (IMWD) of a polyethylene ter...
In the industry when someone wants to modify the way a chemical reactor works; it is not possible to...
A comprehensive mathematical model for the finishing stages of polyethylene terephthalate (PET) synt...