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The final granule size distribution was also observed to become narrower with increased bed temperature and fluidising air velocity.
With increased bed temperature, the molar stream of phenol in the post-reaction gases decreased (Figure 7) reaching the value about 6 mmol/h at 360°C, which corresponds to 90% consumption of this substrate.
The breakage rate and the extent of granule attrition is also found to decrease with increased bed temperature and increased fluidising air velocity.
The overall granule growth rate is observed to increase relatively with increased bed temperature for a more viscous PEG4000, while a maximum growth is seen for a lower viscosity PEG1500.
The aggregation rate is also observed to increase with increased bed temperature when a higher viscosity binder is used, but reveals a maximum aggregation rate for a less viscous binder.
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For a given superficial gas velocity, the average local particle concentration, the dense phase fraction and the particle concentration in the dense phase decrease with increasing bed temperature.
The results show that fluidization is enhanced and fluctuations of the local two-phase flow structure become more intense with increasing bed temperature.
At constant superficial gas velocities, the averaged local particle concentration, the dense phase fraction and particle concentration in the dense phase decrease with increasing bed temperature, whereas both the frequency of the dilute/dense phase cycle and the ratio of the dilute phase duration to the dense phase duration increase.
The desorption process is achieved by increasing the bed temperature up to 100 °C which increases the internal energy of the gas and allowed the gas molecules to escape from the reactor.
The experimental results show that the effective thermal conductivity increased with increasing the average bed temperature.
The experimental results showed that the keff increased from 0.903 W/m°C to 1.204 W/m°C with the increase of bed temperature from 34.3 °C to 785.4 °C.
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