Page 299 - Materials Chemistry, Second Edition
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282       Practical Design Calculations for Groundwater and Soil Remediation



               (b)  To determine the heat content of the air containing 800 ppmV
                   xylene, we have to determine the mass concentration of xylene
                   in the air first (which has been previously determined in
                   Example 7.3):
                            800 ppmV of xylene = (800)(0.27 × 10 )
                                                            –6
           	                                 	= 2.16 × 10  lb xylene/ft  air
                                                                   3
                                                       –4
                   Use Equation (7.15) to determine the heating value of the off-gas:
                     Heatingvalue (inBtu/scf)
                         = 19,015 Btu/lb  × (2.16  × 10 −4  lb/scf)= 4.11 Btu/scf

               (c)  Use Equation (7.16) to convert the heating value into Btu/lb:

                   Heatingvalue of an airstreamcontainingxylenes (inBtu/lb)
                       = 4.11 Btu/scf  ÷ 0.0739 lb/scf = 55.6 Btu/lb


              Discussion:
                1.  The heating value of xylene calculated from the Dulong’s for-
                   mula, 19,015 Btu/lb, is essentially the same as that found in the
                   literature, 18,650 Btu/lb.
                2.  The weight percentage of C is 90.57%, and a value of 90.57, not
                   0.9057, should be used in the Dulong’s formula.



           7.3.3   Dilution Air
           Some waste air streams contain enough organic compounds to sustain
           burning (i.e., no auxiliary fuel is required, which means cost savings).
           That is why direct incineration is favorable for treating air with high
           organic concentrations. However, for hazardous air pollutant streams, the
           concentration of flammable vapors to a thermal incinerator is generally
           limited to 25% of the lower explosive limit (LEL), imposed by insurance
           companies for safety concerns. Vapor concentrations up to 40% to 50% of
           the LEL may be permissible if on-line monitoring of VOC concentrations
           and automatic process control and shutdown are employed. Table 7.2 lists
           the LELs and upper explosive limits (UELs) of some combustible com-
           pounds in air.
             When the off-gas has VOC content larger than 25% percent of the LEL (i.e.,
           in most of the initial stages of the SVE-based cleanup projects), dilution air
           must be used to lower the COC concentration to below 25% of its LEL prior
           to incineration [3]. The 25% LEL corresponds to a heat content of 176 Btu/lb
           or 13 Btu/scf in most cases.
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