Catalytic Hydrodechlorination of 2,4-Dichlorophenol Using Co-Current Down Flow Contactor Reactor

Catalytic Hydrodechlorination

  • Asim Rehman Institute of Chemical Engineering and Technology, University of The Punjab, Quaid-e-Azam Campus, Lahore 54590, Pakistan
  • Muhammad Nawaz School of Chemical Engineering, The University of Faisalabad, Faisalabad, Pakistan
  • Arshad Chughtai School of Chemical and Materials Engineering, National University of Sciences and Technology, H-12 Islamabad, Pakistan
  • Muhammad Arif Butt Institute of Chemical Engineering and Technology, University of The Punjab, Quaid-e-Azam Campus, Lahore 54590, Pakistan
  • Abdul Sattar Institute of Chemical Engineering and Technology, University of The Punjab, Quaid-e-Azam Campus, Lahore 54590, Pakistan
Keywords: catalytic hydrodechlorination, 2,4-dichlorophenol, palladium, carbon, co-current downflow contactor reactor

Abstract

In this study, a new prospective regarding application of gas liquid reactions in the presence of catalyst was studied for pollution abatement in the novel reactor. Catalytic hydrodechlorination (CHDC)
of 2,4-dichlorophenol (2,4-DCP) in aqueous system was carried out under the operating conditions at 25- 75 °C, 1 atm in co-current down flow contactor reactor. Under these reaction conditions complete conversion  of 2,4-DCP into less toxic products (phenol and cyclohexanone) was achieved using 5% Pd/C catalyst. At typical temperature the hydrodechlorination reaction of 2,4-DCP was completed after 10 min. 2,4-DCP was converted to 96.19% of phenol and 3.81% of cyclohexanone using 0.4 g/L of 5% Pd/C catalyst. The increase in initial concentration of 2,4-DCP resulted in the increase in time for the dechlorination of 2,4- DCP. The calculated activation energy values amounted to 43 KJ/mol for the CHDC of 2,4-DCP exhibiting that this reaction occurs mainly under the surface reaction rate controlled condition.

Published
2015-04-25