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Handbook of air conditioning and refrigeration / Shan K

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● To eliminate or to reduce indoor gaseous contaminants such as combustion products, VOCs, <strong>and</strong><br />

objectable odors<br />

● According to the ASHRAE St<strong>and</strong>ard 62-1999, to reduce the concentration <strong>of</strong> the known <strong>and</strong><br />

specifiable contaminants in recirculating <strong>air</strong> to the required concentration level based on indoor<br />

<strong>air</strong> quality procedures to achieve acceptable <strong>air</strong> quality<br />

Activated Carbon Adsorbers<br />

GAC Performance<br />

IMPROVING INDOOR AIR QUALITY 24.9<br />

Brown et al. (1994) reported that mean concentrations <strong>of</strong> VOCs in various <strong>of</strong>fice buildings<br />

ranged from 0.18 to 4.15 mg/m 3 with a new building having a total VOC concentration as high as<br />

39.3 mg/m 3 . For each individual compound, its mean concentration was about 0.05 mg/m 3 . Granular<br />

activated carbon (GAC) is one <strong>of</strong> the most widely used adsorbents for indoor gaseous contaminants.<br />

Adsorption (physical adsorption) is a surface phenomenona. In an adsorption process, the molecule<br />

<strong>of</strong> the gaseous contaminant<br />

● Must be transported from the carrier <strong>air</strong>stream across the boundary layer that surrounds the adsorber<br />

granule<br />

● Must diffuse into the pore <strong>of</strong> the adsorbent <strong>and</strong> occupy the surface<br />

● Must be bound to the surface<br />

Adsorption is different from absorption in which the gaseous contaminant is dissolved in or reacts<br />

with the absorbing medium, which can be either a porous solid or a liquid.<br />

As discussed in Sec. 15.16, removal efficiency, adsorption capacity, <strong>and</strong> service life are important<br />

performance parameters for GAC. Toluene has been used as a surrogate for indoor VOCs for the<br />

testing <strong>of</strong> GAC performance. An increase in relative humidity generally reduces the adsorption <strong>of</strong><br />

VOC on GAC. This may affect some compounds more than others, <strong>and</strong> it becomes more significant<br />

at low VOC concentrations. When the concentration <strong>of</strong> the contaminant downstream <strong>of</strong> the adsorber<br />

rises until its concentration is the same as that <strong>of</strong> the upstream, the penetration at this time is called<br />

breakthrough penetration.<br />

In addition to the adsorption capacity <strong>and</strong> the removing efficiency discussed in Sec. 15.16, the<br />

performance parameter breakthrough time t b is defined as the elapsed time between the start <strong>of</strong><br />

challenge <strong>and</strong> the time when the penetrating concentration reaches the specified breakthrough fraction,<br />

10 percent breakthrough time t 10% or 50 percent breakthrough time t 50%.<br />

Another performance parameter is called capacity at t b which is expressed as the ratio <strong>of</strong> the<br />

mass <strong>of</strong> contaminant collected at a particular breakthrough time to the mass <strong>of</strong> the GAC bed, in<br />

percentage.<br />

Van Osdell <strong>and</strong> Sparks (1995) reported the performance <strong>of</strong> GAC challenged with toluene at various<br />

concentrations at 77°F (25°C) <strong>and</strong> 50 percent relative humidity as follows:<br />

Challenge concentration ppm 0.44 1.1 9.2 71.7<br />

Challenge concentration, mg/m 3 1.7 4.0 34 270<br />

Carbon bed mass, g 24.1 23.1 23.4 25.8<br />

t 10%, h 625 344 72 11.9<br />

t 50%, h 750 422 88 15.0<br />

Capacity at t 10%, percent 6.6 9.2 16.2 18.8<br />

Capacity at t 50%, percent 7.9 11.3 19.7 23.8

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