Analyzing a liquid-solid phase countercurrent two- and three-stage adsorption process with the Freundlich equation.
Adsorbent consumption advantages of a countercurrent two- and three-stage process are described. The Freundlich equation and equilibrium-stage were used to deduce these adsorption processes; it was proved that large adsorbent savings were obtained from operations of these systems in most cases. Microporous activated carbon was prepared from plum kernels with KOH chemical activation. Isotherm equilibrium adsorptions of three dyes (BB1, MB, and AB74) and three phenols (phenol, 4-CP, and 2,4-DCP) were used to explain both the superior adsorption capability of activated carbon and the advantages of analyzing adsorption system operations with the Freundlich equation, and to calculate the countercurrent two- and three-stage adsorption processes and explain the design procedures. A continuous-flow countercurrent three-stage adsorption process was developed to provide for design in practical application.
Tseng
Ru-Ling
RL
Department of Safety, Health and Environmental Engineering, National United University, Miao-Li 360, Taiwan.
Wu
Feng-Chin
FC
D000327:Adsorption; D002244:Carbon / Q000737:chemistry*; D004396:Coloring Agents / Q000737:chemistry; D004563:Electrochemistry; D006878:Hydroxides / Q000737:chemistry; D008855:Microscopy, Electron, Scanning; D010636:Phenols / Q000737:chemistry; D016062:Porosity; D017680:Potassium Compounds / Q000737:chemistry; D013816:Thermodynamics
D004396:Coloring Agents; D006878:Hydroxides; D010636:Phenols; D017680:Potassium Compounds; D002244:Carbon; C029943:potassium hydroxide