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First International Conference on MOLDAVIAN RISKS – FROM ...

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<str<strong>on</strong>g>First</str<strong>on</strong>g> <str<strong>on</strong>g>Internati<strong>on</strong>al</str<strong>on</strong>g> <str<strong>on</strong>g>C<strong>on</strong>ference</str<strong>on</strong>g> <strong>on</strong> <strong>MOLDAVIAN</strong> <strong>RISKS</strong> - <strong>FROM</strong> GLOBAL TO LOCAL SCALE<br />

16-19 May 2012, Bacau, Romania<br />

AVOIDING <strong>RISKS</strong> IN SOLID-GAS DEPOLLUTION BY<br />

CONTROLLING PARAMETERS IN FLUIDIZED BED<br />

Gabriela Muntianu 1 , Ileana Denisa Nistor 1 , Cosmin Jinescu 2 ,<br />

Gholamreza Djelveh 3<br />

1 “Vasile Alecsandri” University of Bacau, Department of Chemical and Food Engineering,<br />

Romania<br />

2 Politehnica University of Bucharest, Departament of Mechanical Engineering, Romania<br />

3 ENSCCF, LGCB, BP 206, Clerm<strong>on</strong>t Universite´, France<br />

Corresp<strong>on</strong>ding author: Ileana Denisa Nistor, denisanistor@yahoo.com; dnistor@ub.ro<br />

Abstract: The paper aims to avoid possible and emerging risk in gas depolluti<strong>on</strong> processes.<br />

To achieve this desiderate the main technological parameters used in gas-solid depolluti<strong>on</strong><br />

processes with process intensificati<strong>on</strong> by using fluidizati<strong>on</strong> bed are studied. The use of the<br />

fluidizati<strong>on</strong> bed as intensificati<strong>on</strong> technique in gas depolluti<strong>on</strong> provides higher<br />

performance but also inc<strong>on</strong>veniences in the bed granular structure. At higher flow<br />

velocities of the fluidizati<strong>on</strong> agent gas bubbles that are distributed uniformly in the column<br />

appear and their diameter increases slightly with the gas velocity. Gas bubbles create a<br />

str<strong>on</strong>g turbulence in the bed, which induces a str<strong>on</strong>g mixing of solid phase and determines<br />

permanent fluctuati<strong>on</strong>s of the fluidized bed height. Al<strong>on</strong>g with the increasing gas flow,<br />

pist<strong>on</strong>s appear, leading to turbulent fluidizati<strong>on</strong> regime. Bed structure vitiati<strong>on</strong>s, pist<strong>on</strong>s<br />

and total or intermediate channels appear as particular aspect of n<strong>on</strong>-homogeneous<br />

fluidizati<strong>on</strong>. The structure of the fluidizati<strong>on</strong> bed that is the main characterizati<strong>on</strong> index of<br />

this technique also represents the main obstacle that limits the applicati<strong>on</strong>s in gas<br />

remediati<strong>on</strong>. Practical applicati<strong>on</strong>s of fluidized bed and the difficulties created by the<br />

uneven structure of the bed, directed the research efforts towards the realizati<strong>on</strong> of a<br />

fluidized homogeneous structure, increasing the efficiency of this technique in the<br />

remediati<strong>on</strong> of gasses. Homogeneous fluidizati<strong>on</strong> is characterized by a single and uniform<br />

distributi<strong>on</strong> of solid particles in bed and a uniform expansi<strong>on</strong> of it. The distance between<br />

solid particle increases with the velocity of the flow agent and the homogeneous fluidized<br />

bed can be assimilated as a boiling liquid. Hydrodynamic parameters c<strong>on</strong>trolled in the<br />

fluidized bed were diameter and density of solid particles, velocity of the fluidizati<strong>on</strong> agent<br />

and the ratio between the height of fixed bed and diameter of fluidizati<strong>on</strong> column. The<br />

paper proposes combining the advantages possessed by the natural clays (calcium and<br />

sodium clay) as solid particles through the fluidizati<strong>on</strong> technique in order to improve the<br />

gas remediati<strong>on</strong> process.<br />

Keywords: process intensificati<strong>on</strong>, fluidizati<strong>on</strong> properties, solid particle, fixed bed, fluidized bed.<br />

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