A commonly used energy-efficient nylon 6 reactor is simulated under steady-state conditions. The effects of various operating conditions and parameters, e.g., feed composition, temperature and flow rate, heat transfer coefficients, and reactor dimensions, on the temperature and molecular weight profiles are studied. A temperature maximum is observed in the reactor under usual conditions of operation. The maximum value of the temperature is sensitive to the feed conditions, and one has to ensure that degradation reactions speeded up at high temperatures do not affect product characteristics. The model and the numerical technique used are fairly simple and account for most of the important features of industrial reactors. Hence, these can be ...
The mathematical modelling of a bench-scale reactor is presented. The formulation of the mass and he...
The operation of an industrial semi-batch reactor is modeled and the flow of one reactant is investi...
This paper describes the development of a dynamic simulator model for a jacketed batch reactor equip...
A commonly used energy-efficient nylon 6 reactor is simulated under steady-state conditions. The eff...
Mass- and energy-balance equations that describe the hydrolytic polymerization of nylon-6 in an auto...
An industrial semibatch Nylon 6 reactor has been modeled and then optimized. The model developed ...
This work presents a comprehensive computer simulation study for the hydrolytic polymerization of ε-...
Optimal jacket-fluid temperature profiles for tubular Nylon 6 reactors (in the presence of radial gr...
In recent years, numerical simulation and optimization of chemical reactors in general, and polymeri...
AbstractThis paper deals with the model based of an industrial low-density polyethylene (LDPE) tubul...
The parametric sensitivity of an industrial autothermal nylon 6 reactor was studied. The sensiti...
The paper presents some results concerning analysis and simulation of steady-state and dynamic behav...
Optimal temperature profiles for nylon 6 polymerization in plug-flow reactors have been obtained wit...
A three-stage isothermal nylon 6 reactor with a kinetic scheme incorporating ring opening, polyconde...
The design of a Polyamide6 process via stationary simulation is described. The main motivation was t...
The mathematical modelling of a bench-scale reactor is presented. The formulation of the mass and he...
The operation of an industrial semi-batch reactor is modeled and the flow of one reactant is investi...
This paper describes the development of a dynamic simulator model for a jacketed batch reactor equip...
A commonly used energy-efficient nylon 6 reactor is simulated under steady-state conditions. The eff...
Mass- and energy-balance equations that describe the hydrolytic polymerization of nylon-6 in an auto...
An industrial semibatch Nylon 6 reactor has been modeled and then optimized. The model developed ...
This work presents a comprehensive computer simulation study for the hydrolytic polymerization of ε-...
Optimal jacket-fluid temperature profiles for tubular Nylon 6 reactors (in the presence of radial gr...
In recent years, numerical simulation and optimization of chemical reactors in general, and polymeri...
AbstractThis paper deals with the model based of an industrial low-density polyethylene (LDPE) tubul...
The parametric sensitivity of an industrial autothermal nylon 6 reactor was studied. The sensiti...
The paper presents some results concerning analysis and simulation of steady-state and dynamic behav...
Optimal temperature profiles for nylon 6 polymerization in plug-flow reactors have been obtained wit...
A three-stage isothermal nylon 6 reactor with a kinetic scheme incorporating ring opening, polyconde...
The design of a Polyamide6 process via stationary simulation is described. The main motivation was t...
The mathematical modelling of a bench-scale reactor is presented. The formulation of the mass and he...
The operation of an industrial semi-batch reactor is modeled and the flow of one reactant is investi...
This paper describes the development of a dynamic simulator model for a jacketed batch reactor equip...