Experimental Study on Mass Transfer Performances in a New Rotating Packed Bed

Li Juan He; Jie Qiong Li; Yan Ling Ni; Jun Hua Yi; Wen Fei Wu

doi:10.4028/www.scientific.net/AMR.726-731.2182

Paper Titles

Effects of Temperature and pH on the Transformation of Ferric Arsenate to Scorodite in Acidic Solution
p.2165

Electrical Plasma Technology for Dye Decolorization in a Continuous Reactor System
p.2169

Experiment on Removal Efficiency of Dust Particle Using a Ventilation Test House
p.2173

Experimental Research on the Advanced Treatment of Printing and Dyeing Wastewater by Compounded Biological Filtration Equipment
p.2177

Experimental Study on Mass Transfer Performances in a New Rotating Packed Bed
p.2182

Influence of Sulfide to Nitrate Ratios on Denitrifying Sulfide Removal and Elemental Sulfur Reclamation from Wastewater Containing High Organic Carbon Concentration
p.2186

Kinetic Study of Arsenic(V) Absorption with Al₂O₃Functionalized SBA-15
p.2191

Laboratory Study of the Removal Efficiencies for Ammonium and Total Phosphorus from Runoff Using Layered Filtration Systems
p.2198

Magnesium Removal from Liquors of Laterite Leaching
p.2206

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Experimental Study on Mass Transfer Performances in a New Rotating Packed Bed

Abstract:

Based on the vapor-liquid equilibrium principle, a new rotating packed absorption tower was presented against some traditional gas-liquid countercurrent tower defects. An experimental device was built to test CO₂ absorption efficiency in the packed absorption tower under the given experimental conditions. The experimental results show that the new packed absorption tower can capture the simulated flue gas CO₂ and have a higher efficiency 87.8%.