Add to ORKGThe steady state structure of non-isothermal free radical solution polymerizaton in a continuos stirred tank reactor is analyzed. With mean residence time as a bifurcation parameter, five regions of steady states are identified. The effect of reactor operating conditions on the structure and the stability of steady state is discussed
A detailed kinetic model for the novolac-type phenol-formaldehyde polymerization has been proposed i...
Experimental data of Ogata has been curve-fitted to obtain the forward and reverse rate constants fo...
The synthesis of copolymers with a narrow chemical composition distribution (CCD) often requires a t...
Steady state behavior of a continuous stirred tank reactor is analyzed for styrene polymerization wi...
Methodologies are developed for studying the steady-state operation of propylene polymerization in c...
This article explores the non-linear behaviour of isothermal and non-isothermal plug-flow reactor (P...
Nonlinear dynamics of continuous stirred tank reactors for free radical polymerization of styrene ha...
Using the authors' previously developed method for the general kinetic analysis of non-linear irreve...
The step growth polymerization of RAf type multifunctional monomers (with A reacting with A) in casc...
This article describes the influence of gel effect in the free radical polymerization of methyl meth...
This article describes the influence of gel effect in the free radical polymerization of methyl meth...
Mathematical models of reactors for the polymerization of methylmethacrylate (MMA) and propylene hav...
Crosslinking radical polymerisation in a continuously stirred tank reactor has been studied by means...
Molecular weight distributions, moments and the polydispersity indices were computed for AB-type con...
A detailed kinetic model for the novolac-type phenol-formaldehyde polymerization has been proposed i...
A detailed kinetic model for the novolac-type phenol-formaldehyde polymerization has been proposed i...
Experimental data of Ogata has been curve-fitted to obtain the forward and reverse rate constants fo...
The synthesis of copolymers with a narrow chemical composition distribution (CCD) often requires a t...
Steady state behavior of a continuous stirred tank reactor is analyzed for styrene polymerization wi...
Methodologies are developed for studying the steady-state operation of propylene polymerization in c...
This article explores the non-linear behaviour of isothermal and non-isothermal plug-flow reactor (P...
Nonlinear dynamics of continuous stirred tank reactors for free radical polymerization of styrene ha...
Using the authors' previously developed method for the general kinetic analysis of non-linear irreve...
The step growth polymerization of RAf type multifunctional monomers (with A reacting with A) in casc...
This article describes the influence of gel effect in the free radical polymerization of methyl meth...
This article describes the influence of gel effect in the free radical polymerization of methyl meth...
Mathematical models of reactors for the polymerization of methylmethacrylate (MMA) and propylene hav...
Crosslinking radical polymerisation in a continuously stirred tank reactor has been studied by means...
Molecular weight distributions, moments and the polydispersity indices were computed for AB-type con...
A detailed kinetic model for the novolac-type phenol-formaldehyde polymerization has been proposed i...
A detailed kinetic model for the novolac-type phenol-formaldehyde polymerization has been proposed i...
Experimental data of Ogata has been curve-fitted to obtain the forward and reverse rate constants fo...
The synthesis of copolymers with a narrow chemical composition distribution (CCD) often requires a t...