An efficient computational scheme has been established for obtaining the molecular-weight distributions (MWDs) for Nylon 6 polymerization in homogeneous, continuous-flow stirred-tank reactors (HCSTRs) with water vaporization. A three-step procedure is used: the moment equations are solved by a sequential application of Brown's algorithm, the moments so calculated are used to give an empirical Flory-Schultz distribution and, finally, this empirical distribution is used as a starting guess in Brown's algorithm applied to species mass-balance equations to give the exact MWD. The moment-closure approximations normally used for hutch reactors have been found to work equally well with HCSTRs for residence times of industrial significance
Molecular weight distributions, moments and the polydispersity indices were computed for AB-type con...
The kinetic scheme of nylon-6 polymerization consists of ring opening, polyaddition, step growth, re...
Nylon 6 polymerization in batch reactors has been assumed to consist of important reactions of ring ...
Experimental data of Ogata has been curve-fitted to obtain the forward and reverse rate constants fo...
The reversible polymerization of nylon-6 including ring opening, polycondensation, polyaddition and ...
The reversible polymerization of nylon-6 including ring opening, polycondensation, polyaddition and ...
In recent years, numerical simulation and optimization of chemical reactors in general, and polymeri...
This work presents a comprehensive computer simulation study for the hydrolytic polymerization of ε-...
This work presents a comprehensive computer simulation study for the hydrolytic polymerization of ε-...
The reversible polymerization of nylon 6 including ring opening, polycondensation, polyaddition, and...
This dissertation concerns the development of simulation and optimization technology for industrial,...
Nylou-8 is generally manufactured by the hydrolytic polymerization of e-caprolactam. While the kinet...
Poly(ethylene terephthalate) (PET) formation in homogeneous, continuous-flow-stirred tank reactors (...
Mass- and energy-balance equations that describe the hydrolytic polymerization of nylon-6 in an auto...
The objective of this article is to present an approach to ascertain the molecular weight distributi...
Molecular weight distributions, moments and the polydispersity indices were computed for AB-type con...
The kinetic scheme of nylon-6 polymerization consists of ring opening, polyaddition, step growth, re...
Nylon 6 polymerization in batch reactors has been assumed to consist of important reactions of ring ...
Experimental data of Ogata has been curve-fitted to obtain the forward and reverse rate constants fo...
The reversible polymerization of nylon-6 including ring opening, polycondensation, polyaddition and ...
The reversible polymerization of nylon-6 including ring opening, polycondensation, polyaddition and ...
In recent years, numerical simulation and optimization of chemical reactors in general, and polymeri...
This work presents a comprehensive computer simulation study for the hydrolytic polymerization of ε-...
This work presents a comprehensive computer simulation study for the hydrolytic polymerization of ε-...
The reversible polymerization of nylon 6 including ring opening, polycondensation, polyaddition, and...
This dissertation concerns the development of simulation and optimization technology for industrial,...
Nylou-8 is generally manufactured by the hydrolytic polymerization of e-caprolactam. While the kinet...
Poly(ethylene terephthalate) (PET) formation in homogeneous, continuous-flow-stirred tank reactors (...
Mass- and energy-balance equations that describe the hydrolytic polymerization of nylon-6 in an auto...
The objective of this article is to present an approach to ascertain the molecular weight distributi...
Molecular weight distributions, moments and the polydispersity indices were computed for AB-type con...
The kinetic scheme of nylon-6 polymerization consists of ring opening, polyaddition, step growth, re...
Nylon 6 polymerization in batch reactors has been assumed to consist of important reactions of ring ...