Different approaches to modeling the gas phase polymerization of ethylene that have been
considered in the literature are reviewed. It is shown that while simple, well‐mixed models …

Gas phase fluidized bed processes have been widely applied to polyethylene production. In
these processes, the flow, mass transfer, and reaction rate on the microscale and …

Particle size distribution (PSD) is an important parameter in gas-solid fluidized bed. The
change in PSD due to particle attrition can affect the long-term performance of fluidized bed …

Thermal stability is a crucial issue for fluidized-bed ethylene-polymerization reactors,
especially when the particle-aggregation probability increases as a result of the high …

Fluidized bed reactor is one of the main units in gas-phase ethylene polymerization
processes. Due to the complexity in the polymerization kinetics, hydrodynamic behavior and …

To optimize the operating conditions of the industrial fluidized bed reactor with a daily output
of 3 tons of crude ZrCl4, crude ZrCl4 was prepared by carbochlorination using …

This work explores the impact of the inert condensing agent (ICA) n-hexane in the
production of Polyethylene via gasphase condensed mode bed reactor. The gas loaded to …

Two models for the copolymerization of propylene and ethylene in a fluidized bed reactor
(FBR) were developed. A simple model for control; and a more advanced model which …

The prediction of the impact of induced condensing agents (ICAs) during ethylene
polymerization in gas phase reactors is studied. The Sanchez-Lacombe Equation of State …

Surrogate modeling is an efficient alternative for computation-intensive process simulations
in engineering problems. Surrogate model is developed using experimental or computer …