Experimental study of overall gas phase mass transfer coefficient and height of transfer unit in countercurrent rotating packed bed

According to dependence of height transfer unit and packed bed dimension to Mass transfer coefficient, this parameter is highlight factor. Since, previous work have been offer limited amount experimental data and focused on the investigated few collection of operational parameter, this study was be important. This work overall mass transfer coefficient and mass transfer unit was determined by used of essential operational parameter and basic concept of chemical reaction. This result was illustrate the influence of absorbent and adsorb concentration and rotor speed and gasliquid flow rate in experimental study of overall mass transfer coefficient and height transfer unit and optimum dimension of packed bed. Also, values of experimental overall mass transfer coefficient were existence in 10-1 to 101 rang that was show accuracy of experimental result.