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Tytuł artykułu

Influence of aeration on zeolite suspension microfiltration

Wybrane pełne teksty z tego czasopisma
Identyfikatory
Warianty tytułu
Konferencja
XVth International Conference of Young Geologists Her'lany 2014 : Międzybrodzie Żywieckie, Poland, May, 8th-10th 2014
Języki publikacji
EN
Abstrakty
EN
The effects of air injection under various conditions on the experimental results were investigated on microfiltration apparatus. In the experiments zeolite from the area of Nizny Hrabovec was used. Different patterns of flow in the microfiltration system under changing conditions were monitored. The particular flows were photographed and evaluated. If the particles in suspension are of larger dimensions than the membrane pores, the particles settle slowly and accumulate on the membrane surface and form a highly concentrated layer. Due to the formation of this layer the accumulation of solute at the membrane wall and thus sometimes irreversible clogging of the membrane occurs (Vera et al. 2000). The sedimentation of particles on the surface and in the pores of the membrane results in a reduction in the flow and growth of energy consumption. However, there is great potential to reduce this concentration polarization and fouling. At present, two-phase flow studies are of experimental nature and focus mainly on improving the conditions in filtration (Mikulasek et al. 2002). The injection of gas helps to reduce concentration polarization layer so that it improves the hydrodynamic conditions near the surface of the membrane. The results of the study suggest that the improvement of the flow should be achieved by providing appropriate conditions, using the multi-phase microfiltration, low liquid velocity, by mean speed of the gas injected (Qian etal. 2012). The use of a two-phase flow is considered to be the preferred method to overcome the concentration polarization. During the process gas is directly injected at a given pressure and speed into the feed (Bakalar 2013). Cui & Wright (1996) observed improvement in flow of up to 320% if used two-phase flow with gas injected into the suspension in their experiments. Under normal circumstances gas-liquid two-phase vertical flow exhibits different flow patterns including dispersed bubble flow, slug-flow, churn flow, and annular flow as the gas to liquid ratio increases. Bubble flow occurs when the bubbles are significantly less than (e.g. < 60%) the tube or channel size. The bubble behaviour is similar to the bubbles in a stationary liquid. Slug-flow (also called plug-flow) occurs when the gas flows as large bullet-shaped bubbles approaching the diameter of the tube or channel size (Cui & Wright 1996, Vera et al. 2000).
Słowa kluczowe
Wydawca
Rocznik
Strony
125--126
Opis fizyczny
Bibliogr. 6 poz.
Twórcy
autor
  • Technical University of Kosice, Faculty of Mining, Ecology, Process Control and Geotechnologies; Letnd 9, 042 OO Kosice, Slovakia
autor
  • Technical University of Kosice, Faculty of Mining, Ecology, Process Control and Geotechnologies; Letnd 9, 042 OO Kosice, Slovakia
autor
  • Technical University of Kosice, Faculty of Mining, Ecology, Process Control and Geotechnologies; Letnd 9, 042 OO Kosice, Slovakia
Bibliografia
  • 1. Bakalar T., 2013. Heavy metal ions removal from aqueous solutions by a hybrid adsorption and microfiltration process. Eger, Liceum Kiado.
  • 2. Cui Z.F. & Wright K.I.T., 1996. Flux enhancements with gas sparging in downwards crossflow ultrafiltration: performance and mechanism. Journal of Membrane Science, 117, 109-116.
  • 3. Mikulasek P., Pospisil P., Dolecek P. & Cakl J., 2002. Gas-liquid two-phase flow in microfiltration mineral tubular membranes: relationship between flux enhancement and hydrodynamic parameters. Desalination, 146, 103-109.
  • 4. Qian G., Zhou J. Zhang J., Chen C, Jin R. & Liu W., 2012. Microfiltration performance with two-phase flow. Separation and Purification Technology, 98, 165-173.
  • 5. Vera L., Delgado S. & Elmaleh S., 2000. Dimensionless numbers for the steady-state flux of cross-flow microfiltration and ultrafiltration with gas sparging. Chemical Engineering Science, 55, 3419-3428.
  • 6. Vera L, Villarroel R., Delgado S. & Elmaleh S., 2000. Enhancing microfiltration through an inorganic tubular membrane by gas sparging. Journal of Membrane Science, 165, 47-57.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-ebe43b93-949d-4815-8cad-b2c2eb55ff88
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