pyrolysis of low density polyethylene (ldpe) by equilibrium fluid catalytic cracking (fcc) was studied in a stirred reactor under different process parameters. in this work, the effect of process parameters such as degradation temperature (420-510°c), catalyst/polymer ratio (0-60%), carrier gas type (h2, n2, ethylene, propylene, ar and he), residence time and agitator speed (0-300 rpm) on the c...

The paper shows the results of two-phase mixing hydrodynamics simulation in first reactor crystallization cascade. research were obtained using ANSYS Fluent CFD code. distributions velocity and liquid mixture components volume fractions obtained. time full averaging

Pyrolysis of low density polyethylene (LDPE) by equilibrium fluid catalytic cracking (FCC) was studied in a stirred reactor under different process parameters. In this work, the effect of process parameters such as degradation temperature (420-510°C), catalyst/polymer ratio (0-60%), carrier gas type (H2, N2, ethylene, propylene, Ar and He), residence time and agitator speed (0-300 rpm) on the c...

Abstract The technique and technology of movement displacement the powder product inside drum dryer with a paddle agitator have been developed. Theoretical studies were carried out to assess effect system forces on rotating when in opposite direction is exposed it, which allowed estimating throughput capability drying unit. It established that, an increase speed mixing product, increases. resul...