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09_chap_wang.qxd  05/05/2004  5:01 pm  Page 393
                    Catalytic Oxidation                                                       393

                                                                3
                       D           Density of emission stream (lb/ft )
                        e
                       DE          destruction efficiency (%)
                                                        3
                       D           Density of fuel gas (lb/ft )
                        f
                       EC          Equipment cost ($)
                       F           Fan power requirement (kWh/yr)
                        p
                       h           Emission stream desired heat content (Btu/scf)
                        d
                       h           Emission stream heat content (Btu/lb or Btu/scf)
                        e
                       h           Supplementary fuel heating value (Btu/lb)
                        f
                       HR          Heat recovery in heat exchanger (%)
                       HRS         Operating hours per year (h/yr)
                       ∆P          Pressure drop (in. H O)
                                                    2
                       P           System pressure drop (in. H O)
                                                           2
                       Power       Fan power requirement (kW-h)
                       PEC         Purchased equipment cost ($)
                       Q           Flow rate of combined gas stream (scfm)
                        com
                       Q           Dilution air required (scfm)
                        d
                       Q           Emission stream flow rate (scfm)
                        e
                       Q           Supplementary fuel gas flow rate (scfm)
                        f
                       Q           Flue gas flow rate (scfm)
                        fg
                       Q           Actual flue gas flow rate (acfm)
                        fg,a
                                                                     −1
                       SV          Space velocity through catalyst bed (h )
                       TCC         Total capital cost ($)
                       T           Temperature of gas stream entering catalyst bed (ºF)
                        ci
                       T           Temperature of flue gas leaving catalyst bed (ºF)
                        co
                       T           Emission stream temperature (ºF)
                        e
                       T           Temperature of emission stream exiting heat exchanger (ºF)
                        he
                       t           Residence time (s)
                       r
                       T           Reference temperature (77ºF)
                        r
                       V           Waste gas flow rate (scfm)
                                                                  3
                       V           Volume of required catalyst bed (ft )
                        bed
                    REFERENCES
                     1. US EPA,  Survey of Control  Technologies for Low Concentration Organic  Vapor Gas
                        Streams EPA-456/R-95-003 US Environmental Protection  Agency,  Washington, DC,
                        1995.
                     2. US EPA, Handbook: Control Techniques for Hazardous Air Pollutants. EPA 625/9-86-014
                        (NTIS PB91-228809) US Environmental Protection Agency, Washington, DC, 1986.
                     3. US EPA,  Polymer Manufacturing Industry—Background Information for Proposed
                        Standard. EPA 450/3-85-019a (NITS PB88-114996). US Environmental Protection Agency,
                        Washington, DC, 1985.
                     4. US EPA Afterburner Systems Study. EPA-R2-72-062 (NTIS PB212560). US Environmental
                        Protection Agency, Washington, DC, 1972.
                     5. US EPA, Parametric Evaluation of VOC/HAP Destruction Via Catalytic Incineration. EPA-
                        600/2-85-041 (NTIS PB85-191187). US Environmental Protection Agency,  Washington,
                        DC, 1985.
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