Performance of a pilot-scale cross-flow rotating packed bed in removing VOCs from waste gas streams

Chia Chang Lin*, Tzu Ying Wei, Shu Kang Hsu, Wen Tzong Liu

*Corresponding author for this work

Research output: Contribution to journalJournal Article peer-review

56 Scopus citations

Abstract

This study investigates the feasibility of applying a pilot-scale cross-flow rotating packed bed (RPB) to absorb volatile organics compounds (VOCs) from waste gas streams. Isopropyl alcohol (IPA) was used as a model VOC herein. The overall volumetric gas-side mass transfer coefficient (KGa) was determined at various values of operating parameters including rotor speed, gas flow rate and liquid flow rate. The results demonstrated that a cross-flow RPB can yield the KGa values of about 81-165 1/s, corresponding to a removal efficiency of 95% at a gas flow rate ranged from 150 to 300 m3/h, indicating that the mass transfer efficiency of a cross-flow RPB is greater than that of a countercurrent-flow RPB. Consequently, a cross-flow RPB is an effective absorber for removing VOCs from waste gas streams.

Original languageEnglish
Pages (from-to)274-279
Number of pages6
JournalSeparation and Purification Technology
Volume52
Issue number2
DOIs
StatePublished - 12 2006

Keywords

  • Absorption
  • Cross-flow
  • Isopropyl alcohol
  • Mass transfer
  • Rotating packed bed
  • Volatile organics compounds

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