Sentence examples for bed condition from inspiring English sources

Experiments were also conducted in the packed bed condition and also for empty channel flow.

A model is derived for a fluidised bed that enables its steady state particulate expansion to be predicted as a function of superficial velocity from the initial (packed bed) condition to the final fully expanded (single suspended particle) state.

Starting the system from a saturated bed condition leads to a different steady state, with significantly different profiles of both concentration and temperature and a less pure final product.

It was found that the low and mild temperature at 500 ∼ 550 °C would bring the dynamic equilibrium between the rate of CH4 decomposition and the rate of carbon diffusion over Ni catalyst for continuous precipitation of CNTs in the micro-fluidized bed condition.

In this fixed bed condition the gas flowing across the sand particles does not have enough velocity, which was less than the minimum fluidization velocity at all obtained pressures to move the solid particles.

Nearly isothermal bed conditions could be established without using sand as bed material.

The gasifier was successfully operated and isothermal bed conditions maintained at temperatures up to 750 °C.

Regarding reactor configuration, preliminary testing under fluid bed conditions proved quite promising.

The experiments were carried out both under fluidized bed and fixed bed conditions to point out qualitative differences.

The riser and fuel reactor were operated at circulated fluidized bed and bubbling fluidized bed conditions, respectively and the control of solid circulation between two reactors was done by two loop seals operated in bubbling fluidized bed conditions.

Characteristics of incipient fluidization are analysed in relation to variations in the initial packed bed conditions.