Method to remove organic halogenated molecules from gaseous curr

Gas separation: processes – Electric or electrostatic field – And nonelectrical separation of fluid mixture

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95 69, 95 92, 95110, 95114, 95142, 95143, 95214, 95286, 96 18, 96 27, 96 53, 96 57, 96123, 96128, 96150, 55222, 55235, 552574, 552577, 55258, 55270, B01D 4516, B01D 4710, B01D 5100, B01D 5308

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057256357

ABSTRACT:
Method to remove organic halogenated molecules from gaseous currents arriving as a residue of industrial working processes or not, the gaseous current being delivered into a reactor (16) containing a fluid bed consisting of at least one solid adsorbent element after having undergone at least one filtration followed by a cooling, the gaseous current cooperating with the solid particles with exchange by adsorption between the gaseous current and the solid particles, the reactor (16) achieving a time of contact between the gaseous current and the solid particles at least longer than 3 seconds, the gaseous current which enters the reactor (16) having a temperature lower than 80.degree. C., but advantageously between 30.degree. and 70.degree. C., the cooling of the gaseous current upstream of the reactor (16) being followed by a gas/water or gas/air heat exchanger (13). A plant to carry out the above method includes a reactor having a first input zone (17) and a second zone of exchange by adsorption between the gaseous current and a solid support in the form of fluid-bed particles kept in suspension, and a distribution plate (18) to introduce and distribute the gaseous current defining the second zone of the reactor (16), the reactor (16) having dimensions such as to achieve a passage time at least longer than 3 seconds, the concentration of solid support within the reactor (16) being between 0.1 and 0.5 kg per each cubic meter of gaseous substance.

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Muell Und Abfall, vol. 23, No. 4 1 Apr. 1991 pp. 229-235 Vicinus J. et al. "Abscheidung Von Dioxinen".

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