4.7 Article

Temperature and solid properties effects on gas-liquid mass transfer

期刊

CHEMICAL ENGINEERING JOURNAL
卷 162, 期 2, 页码 743-752

出版社

ELSEVIER SCIENCE SA
DOI: 10.1016/j.cej.2010.05.064

关键词

Bubble column; Mass transfer; Absorption; Multiphase reactors; Particles; Temperature

资金

  1. Fundacao para a Ciencia e Tecnologia [SFRH/BPD/45637/2008]
  2. Fundação para a Ciência e a Tecnologia [SFRH/BPD/45637/2008] Funding Source: FCT

向作者/读者索取更多资源

The knowledge about the effect of solid phase properties, at different temperatures, on gas-liquid transfer and the respective physical mechanisms has been poorly studied. In the present work, the temperature and solid properties (size and density) effects on the gas-liquid mass transfer characteristics in a bubble column were experimentally evaluated. Gas-liquid-solid systems formed by air/water/polyvinyl chloride (PVC) beads and air/water/expandable polystyrene (EPS) beads were used. For each system, volumetric liquid side mass transfer coefficient, k(L)a, was determined under different temperatures (20-35 degrees C), superficial gas velocities (up to 7.2 mm/s), solids sizes (210, 549 and 591 mu m) and concentration (up to 5 vol.%). The results show that the temperature plays an important role on mass transfer phenomena as k(L)a increases as temperature is increased. However, temperature does not have, significantly, influence on the solids effect on k(L)a. In what concerns the effect of the solids on k(L)a, a negative effect of their presence is observed being this effect more pronounced for the largest particles (for PVC). In addition, for the same solid size, a decrease in k(L)a occurs when the solid loading increases (observed in both cases, PVC and EPS). Complementary, bubble/particle interaction studies, using an image analysis technique, were also done aiming a better understanding of the effects of the two types of particles - PVC and EPS - on k(L)a values, being clearly confirmed that physical (e.g. density) and chemical properties of the solids are important parameters to be taken into account on mass transfer and hydrodynamic studies. Based on theoretical models for k(L) and a, an empirical correlation for k(L)a dependence on the experimental variables was developed. The experimental results were fitted with a mean deviation of 5%, that is similar to the experimental error (5%). (C) 2010 Elsevier B.V. All rights reserved.

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