REGULAR NOZZLE FOR THE SEPARATION AND MASS-EXCHANGE APPARATUSES

FIELD: petrochemical industry; equipment for separation and the mass-exchange apparatuses. ^ SUBSTANCE: the invention is pertaining to the field of petrochemical industry, in particular, to the regular nozzle for the separation and mass-exchange apparatuses. The regular nozzle for separation and the...

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Main Authors ZAPOROZHETS EVGENIJ PETROVICH, ZIBERT ROMAN GENRIKHOVICH, AVERKIN ANATOLIJ IVANOVICH, ZIBERT GENRIKH KARLOVICH
Format Patent
LanguageEnglish
Russian
Published 10.10.2006
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Summary:FIELD: petrochemical industry; equipment for separation and the mass-exchange apparatuses. ^ SUBSTANCE: the invention is pertaining to the field of petrochemical industry, in particular, to the regular nozzle for the separation and mass-exchange apparatuses. The regular nozzle for separation and the mass-exchange apparatus is pertaining to the designs of the regular nozzles intended for realization the heat-mass-exchanging and separation processes in the system gas (steam)-liquid. The nozzle contains the turned relatively to each other packets of the sheets with the slant corrugations or the porous prominences crossing in the adjacent sheets. At that and the porosity of the prominences and/or the sheets in the packets is diminishing in the nozzle towards the gas outlet. Besides the prominences and/or the sheets of the packets are made on the gas inlet into the nozzle out of the hydrophilic material, and on the outlet of the nozzle - out of the liophilic material, and the ratio of the pores sizes of the prominences and/or of the sheets of the packets on the inlet and the outlet of the gas are proportional to ratios of the surface tension of the separable liquids in the power of 0.5. The invention allows to up-grade efficiency of the processes of the heat-and-mass exchange and separation by reduction of carryover of the liquid with the increased gas productivity. ^ EFFECT: the invention allows to up-grade efficiency of the processes of the heat-and-mass exchange and separation by reduction of carryover of the liquid with the increased gas productivity. ^ 3 cl, 1 dwg
Bibliography:Application Number: RU20040122455