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Packed Tower Absorber

Jun 04, 2018

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Jaz Santos
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    Packed Scrubber Design

    Basics

    Gas-Liquid Equilibrium

    Operating Line Tower Diameter and Pressure Drop

    Mass Transfer and Tower Height

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    In absorption processes, gaseous

    contaminants are removed from a gasstream by transferring them to a liquid.

    That liquid is usually water or an aqueous

    solution that contains chemicals selected

    to react with the absorbed contaminants.

    Most systems operate with collection

    efficiencies of 70 percent to over 99

    percent

    Packed bed systems are typically used for

    highly water soluble gases such as HCl orHF or NH3

    Spray towers are usually used on power

    plants due to their lower pressure drop

    Absorption Basics

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    The most important factor affecting collection

    efficiency is the solubility of the contaminantin the liquid.

    Gases are more soluble in cold liquids than

    in hot liquids and less soluble in liquids with

    low pH.

    The liquid surface area and the time

    available for diffusion of the gaseous

    contaminants into the liquid are also

    important factors affecting performance

    Solubility

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    There are many equipment designs for contacting theliquid with the contaminated gas stream. The most

    common ones are:

    spray towers, tray towers,

    packed beds, and

    spray dryers.

    Types of Absorbers

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    Packed Scrubber Design

    Basics

    Gas-Liquid Equilibrium

    Operating Line Tower Diameter and Pressure Drop

    Mass Transfer and Tower Height

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    Packed Scrubber Design

    Basics

    Gas-Liquid Equilibrium

    Operating Line Tower Diameter and Pressure Drop

    Mass Transfer and Tower Height

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    Packed Scrubber Design

    Basics

    Gas-Liquid Equilibrium

    Operating Line Tower Diameter and Pressure Drop

    Mass Transfer and Tower Height

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    Packed Scrubber Design

    Basics

    Gas-Liquid Equilibrium

    Operating Line Tower Diameter and Pressure Drop

    Mass Transfer and Tower Height

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    Two film theory

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    For a highly soluble gas such as HCl or HF in

    water, m = 0. Then Nog simplifies to:

    1

    2

    1ln ln

    1O G

    YN

    Y

    In this case, to achieve 99% removal:

    1ln 4 .6

    0 . 01

    O GN

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    (g/mole)gaspollutantofweightmolecularM

    (atm)pressuresystemtotalP

    )/m(minterfaceliquid-gasofareaeffectivea

    Pa)-m-(moles/hphasegasonbasedtcoefficientransfer-massoverallK

    )m-(g/hvelocitymasslsuperficiagasG'

    (m)resistancephasegasoverallonbasedunittransferaofheightH

    (m)unittransferaofheightHTU

    ))(P)(M(aK

    G'HHTU

    G

    32

    e

    2

    OG

    2

    OG

    GeOG

    OG

    where

    Height of a transfer unit

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    D d P f

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    There are several operating problems that can occur in absorption systems.

    The most common of these include the following:

    Inadequate liquid flow

    Low inlet liquid pH

    Poor gas-liquid contact

    Inadequate chemical feed rate

    Excessive liquid temperature

    Plugged beds or mist eliminators

    Corrosion

    Decreased Performance

    D d P f

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    To determine if an adsorption system is working properly,

    field personnel should observe if possible:

    Outlet Gas Stream Contaminant Measurement

    not likely available

    Temperature Difference between the Gas Inlet and

    Outlet,

    Liquid Flow Rate and Liquid Pressures.

    Pressure Drop, and Stack Opacity

    Decreased Performance