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10_chap_wang.qxd  05/05/2004  5:10 pm  Page 414
                    414                                                    Lawrence K.Wang et al.

                       The emission stream flow rate per adsorbing bed (Q' ) is obtained by dividing the HAP
                                                                 e,a
                       emission stream by the number of beds adsorbing (NA):
                                           Q'   = Q /NA
                                             e,a   e,a
                                           Q'  = 15,363 acfm /2 = 7,681.5 acfm
                                             e,a
                       To determine the diameter and length of vessel, assume an emission stream bed velocity
                       (U ) of 85 ft/min.
                         e
                                    D = 0.127 (2,390 lbs) (85 ft/min)/ 7,681.5 acfm = 3.4 ft
                                     v
                                                     2
                                    L = 7.87 (Q'  / U ) / C'                                   (6)
                                     v         e,a  e    req
                                                                 2
                                    L = 7.87 (7,681.5 acfm /85 ft/min) /2,390 lb = 27 ft
                                     v
                                     S =π D (L + D /2)                                         (8)
                                           v  v    v
                                     S =π (3.4 ft) (27 ft + (3.4/2)) = 307 ft 2
                       The vessel diameter and length are somewhat unrealistic. Increasing the bed velocity, U ,
                                                                                             e
                       to 100 ft/min will increase the diameter and shorten the length. It may be beneficial to
                       contact a vendor to obtain assistance in selecting size of the vessel.

                    Example 4

                       Outline the methodology for the determination of the pretreatment requirements of a gas-
                       phase carbon adsorption system.

                       Solution
                       The methodology for determining the carbon adsorption pretreatment requirements for an
                       emission stream is outlined in the following three steps:

                       Step 1: Cooling Consideration
                                                   T =___________ºF
                                                    e
                       When the temperature of the emission stream is higher than 130ºF, a heat exchanger is
                       needed to lower the temperature to below 130ºF or less. Refer to a suitable reference for
                       the calculation procedures.

                       Step 2: Dehumidification Consideration
                                                   R   =________%
                                                    hum
                       When the relative humidity is above 50% and the HAP concentration is less than 1000
                       ppmv, a condenser may be used to cool and condense the water vapor in the emission
                       stream, which will reduce the relative humidity of the emission stream.

                       Step 3: High VOC Concentration Consideration
                                                 HAP =________ppmv
                                                     e
                       When the flammable vapors are present in the emission stream, they must be limited to
                       below 25% of their LEL.
                                                LEL=_______ppmv (see Table 2)
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