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Computational Fluid Dynamic (CFD) is a technique which helps to optimize the design and operation of fluidized bed combustor and gasifiers.
However, problems such as low thermal efficiency, high emissions, bed agglomeration etc. are still encountered in the operation of fluidized beds.
Accurate predictions of bubble size and velocity are, therefore, essential for the reliable design and successful operation of fluidized bed reactors.
The results could be used to develop a new method of controlling the operation of fluidized beds burning a gaseous fuel.
Thermal properties may be further enhanced by non-conventional design and operation of fluidized beds based on uneven or unsteady (pulsed) fluidization.
"Creative" and non-conventional design and operation of fluidized beds, like those based on uneven or unsteady (pulsed) fluidization, may be beneficial to the enhancement of thermal diffusivity and surface-to-bed heat transfer, improving the potential for application in the very demanding context of CSP with thermal energy storage.
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Therefore the minimum fluidization air velocity to fluidize the sand particles and pressure drop are crucial hydrodynamic parameters for analysing the operation and design of fluidized bed combustors.
The effects of steam injection on stripping efficiency were studied in an effort to improve operation of a fluidized bed stripper.
The decomposition of sulfates present within bottom ashes produced during operation of a fluidized bed combustor is not complete under continuously reducing conditions (2% CO) at 950∘C.
The results in this study assume importance from the standpoint of design and steady operation of multistage fluidized bed reactor with downcomer as an air pollution control system for control of gaseous emissions in the industries.
The air flow rate, particle size of the solids and air distributor type are considered to be the key parameters of the operation of a fluidized bed ash cooler (FBAC).
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