absorber design parameters

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Packed Scrubber Design Gas-Liquid Equilibrium Operating Line Tower Diameter and Pressure Drop Mass Transfer and Tower Height Tower Internals

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  • Packed Scrubber Design

    Gas-Liquid Equilibrium Operating Line Tower Diameter and Pressure Drop Mass Transfer and Tower Height Tower Internals

  • Packed Scrubber Design

    Gas-Liquid Equilibrium Operating Line Tower Diameter and Pressure Drop Mass Transfer and Tower Height Tower Internals

  • Packed Scrubber Design

    Gas-Liquid Equilibrium Operating Line Tower Diameter and Pressure Drop Mass Transfer and Tower Height Tower Internals

  • Packed Scrubber Design

    Gas-Liquid Equilibrium Operating Line Tower Diameter and Pressure Drop Mass Transfer and Tower Height Tower Internals

  • Two film theory

  • (g/mole) gaspollutant ofweight molecular M(atm) pressure system totalP

    )/m(m interface liquid-gas of area effectivea

    Pa)-m-(moles/h phase gason basedt coefficientransfer -mass overallK)m-(g/h velocity mass lsuperficia gasG'

    (m) resistance phase gas overallon basedunit transfer a ofheight H(m)unit transfer a ofheight HTU

    ))(P)(M(aKG'HHTU

    G

    32e

    2OG

    2OG

    GeOGOG

    where

    Height of a transfer unit

  • Packed Scrubber Design

    Gas-Liquid Equilibrium Operating Line Tower Diameter and Pressure Drop Mass Transfer and Tower Height Tower Internals