The reversible polymerization of nylon-6 including ring opening, polycondensation, polyaddition and cyclization reactions as well as the reaction with monofunctional acids, has been modelled. Molecular weight distributions and their moments have been obtained for various initial conditions and at two temperatures, 235° and 265°C, for a batch reactor. The cyclic oligomer concentrations have also been computed. It is found that even though the cyclization step has little influence on the monomer conversion, it does affect the molecular weight distribution and its moments
A theoretical model is developed for the effect of segmental diffusion on reversible step growth pol...
Nylou-8 is generally manufactured by the hydrolytic polymerization of e-caprolactam. While the kinet...
To model the reversible novolac polymerization, five reactive species A to E have been defined. Mole...
The reversible polymerization of nylon-6 including ring opening, polycondensation, polyaddition and ...
The reversible polymerization of nylon 6 including ring opening, polycondensation, polyaddition, and...
A detailed model incorporating mass balance and moment equations and appropriate closure conditions ...
Experimental data of Ogata has been curve-fitted to obtain the forward and reverse rate constants fo...
An efficient computational scheme has been established for obtaining the molecular-weight distributi...
A parametric study of the molecular weight distribution and its moments has been made on the irrever...
The kinetic scheme of nylon-6 polymerization consists of ring opening, polyaddition, step growth, re...
Molecular weight distributions, moments and the polydispersity indices were computed for AB-type con...
This study deals with the hydrolytic step-growth polymerization of e-caprolactam to produce nylon-6 ...
In recent years, numerical simulation and optimization of chemical reactors in general, and polymeri...
Nylon 6 polymerization in batch reactors has been assumed to consist of important reactions of ring ...
Reversible AB-type polycondensations have been simulated in a batch reactor where the monomer reacts...
A theoretical model is developed for the effect of segmental diffusion on reversible step growth pol...
Nylou-8 is generally manufactured by the hydrolytic polymerization of e-caprolactam. While the kinet...
To model the reversible novolac polymerization, five reactive species A to E have been defined. Mole...
The reversible polymerization of nylon-6 including ring opening, polycondensation, polyaddition and ...
The reversible polymerization of nylon 6 including ring opening, polycondensation, polyaddition, and...
A detailed model incorporating mass balance and moment equations and appropriate closure conditions ...
Experimental data of Ogata has been curve-fitted to obtain the forward and reverse rate constants fo...
An efficient computational scheme has been established for obtaining the molecular-weight distributi...
A parametric study of the molecular weight distribution and its moments has been made on the irrever...
The kinetic scheme of nylon-6 polymerization consists of ring opening, polyaddition, step growth, re...
Molecular weight distributions, moments and the polydispersity indices were computed for AB-type con...
This study deals with the hydrolytic step-growth polymerization of e-caprolactam to produce nylon-6 ...
In recent years, numerical simulation and optimization of chemical reactors in general, and polymeri...
Nylon 6 polymerization in batch reactors has been assumed to consist of important reactions of ring ...
Reversible AB-type polycondensations have been simulated in a batch reactor where the monomer reacts...
A theoretical model is developed for the effect of segmental diffusion on reversible step growth pol...
Nylou-8 is generally manufactured by the hydrolytic polymerization of e-caprolactam. While the kinet...
To model the reversible novolac polymerization, five reactive species A to E have been defined. Mole...