The concept of process intensification is applied to a CSTR polymerisation reactor, where bulk reactions take place via styrene free-radicals, connected to a semi-flooded horizontal condenser; the aim is to operate the system in a safe and efficient way. The results obtained show that the model developed was able to reproduce the major dynamic characteristics, even with the presence of non-condensable gases. The existence of such gases prevents the reactor from ever reaching a steady-state, as they accumulate in the system, increasing the condenser pressure and the reactor temperature and reducing the area of contact and the mass of liquid in the condenser. To circumvent this problem, the control strategy of this work proposes a regular pur...
We present a comprehensive approach to the simultaneous design and control of a continuous stirred t...
This work studies the optimization and control of a styrene polymerization reactor. The proposed str...
In this paper a dynamic model of the high-pressure polymerisation of ethylene in tubular reactors is...
The concept of process intensification is applied to a CSTR polymerization reactor, where bulk react...
The concept of process intensification is applied to a CSTR polymerization reactor, where bulk react...
The concept of process intensification is applied to a CSTR polymerization reactor, where bulk react...
A thorough model of the high pressure polymerization of ethylene in tubular reactors previously deve...
A polymerization reactor connected to a semi-flooded horizontal condenser is presented. A model of t...
This work studies the optimization and control of a styrene polymerization reactor. The proposed str...
Polymerization process have a nonlinear nature since it exhibits a dynamic behavior throughout the p...
This work studies the optimization and control of a styrene polymerization reactor. The proposed str...
With an annual worldwide production well in excess of 100 million metric tons, synthetic polymers co...
Steady-state multiplicity analysis is used to study the operability of a jacketed exothermic styrene...
In chemical processes, runaway reactions, i.e. exothermic reactions getting out of control, represen...
In chemical processes, runaway reactions, i.e. exothermic reactions getting out of control, represen...
We present a comprehensive approach to the simultaneous design and control of a continuous stirred t...
This work studies the optimization and control of a styrene polymerization reactor. The proposed str...
In this paper a dynamic model of the high-pressure polymerisation of ethylene in tubular reactors is...
The concept of process intensification is applied to a CSTR polymerization reactor, where bulk react...
The concept of process intensification is applied to a CSTR polymerization reactor, where bulk react...
The concept of process intensification is applied to a CSTR polymerization reactor, where bulk react...
A thorough model of the high pressure polymerization of ethylene in tubular reactors previously deve...
A polymerization reactor connected to a semi-flooded horizontal condenser is presented. A model of t...
This work studies the optimization and control of a styrene polymerization reactor. The proposed str...
Polymerization process have a nonlinear nature since it exhibits a dynamic behavior throughout the p...
This work studies the optimization and control of a styrene polymerization reactor. The proposed str...
With an annual worldwide production well in excess of 100 million metric tons, synthetic polymers co...
Steady-state multiplicity analysis is used to study the operability of a jacketed exothermic styrene...
In chemical processes, runaway reactions, i.e. exothermic reactions getting out of control, represen...
In chemical processes, runaway reactions, i.e. exothermic reactions getting out of control, represen...
We present a comprehensive approach to the simultaneous design and control of a continuous stirred t...
This work studies the optimization and control of a styrene polymerization reactor. The proposed str...
In this paper a dynamic model of the high-pressure polymerisation of ethylene in tubular reactors is...