The formation of polyethylene terephthalate (PET) has been modeled to have reactions with monofunctional compounds, redistribution, and cyclization reactions in addition to the usual polycondensation step. In the final stages, the overall polymerization is mass-transfer controlled and solution of the reactor performance equations have been determined through the orthogonal collocation technique. This technique is found to be considerably more efficient for PET reactors compared to the finite difference method; the use of ten collocation points gives results which are close to the exact solution
A mathematical model for the continuous prepolymerization of BHET to PET, carried out in a series of...
Polyethylene terephthalate (PET) is a major polymer with diverse applications. The chemistry of synt...
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...
A mathematical model has been developed to compute the molecular weight distribution (MWD) in the po...
The polycondensation step of poly(ethylene terephthalate) (PET) formation is assumed to include vari...
Poly(ethylene terephthalate) (PET) formation in homogeneous, continuous-flow-stirred tank reactors (...
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...
A comprehensive mathematical model for the finishing stages of polyethylene terephthalate (PET) synt...
A new comprehensive model for solid-state polycondensation (SSP) of polyethylene terephthalate (PET)...
The polycondensation of PET through ester interchange is a process strongly limited by mass transpor...
A mathematical model of a continuous polycondensation reactor used in the finishing stages is develo...
The tranesterification step of the polyethylene terephthalate (PET) formation consists of several si...
Aspects related to the engineering of polyethylene terephthalate (PET) manufacture have been reviewe...
A mathematical model for the continuous prepolymerization of BHET to PET, carried out in a series of...
Polyethylene terephthalate (PET) is a major polymer with diverse applications. The chemistry of synt...
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...
A mathematical model has been developed to compute the molecular weight distribution (MWD) in the po...
The polycondensation step of poly(ethylene terephthalate) (PET) formation is assumed to include vari...
Poly(ethylene terephthalate) (PET) formation in homogeneous, continuous-flow-stirred tank reactors (...
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...
A comprehensive mathematical model for the finishing stages of polyethylene terephthalate (PET) synt...
A new comprehensive model for solid-state polycondensation (SSP) of polyethylene terephthalate (PET)...
The polycondensation of PET through ester interchange is a process strongly limited by mass transpor...
A mathematical model of a continuous polycondensation reactor used in the finishing stages is develo...
The tranesterification step of the polyethylene terephthalate (PET) formation consists of several si...
Aspects related to the engineering of polyethylene terephthalate (PET) manufacture have been reviewe...
A mathematical model for the continuous prepolymerization of BHET to PET, carried out in a series of...
Polyethylene terephthalate (PET) is a major polymer with diverse applications. The chemistry of synt...
This work presents the analysis of a slurry polymerization stirred tank reactor for the production o...