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w� � tl! � tl• tib � t� t� � � � � � � � � <br /> Table 3 <br /> CATALYTIC OXIDIZER OPERATIONAL DATA <br /> Rutz Grocery <br /> 4491 West Durham ferry Road <br /> Tracy California <br /> TPHg Manual Available Flow Oxidizer Prc Catalyst Catalyst Exhaust TPHg Operational Avg TPHg Period <br /> Sample Sample Operational TPHg Dest Effie Dilution Vacuum(AV) Sensor(V 1) Pressure(P2) Temp (72) Temp (T3) Yield Period Yield Yield <br /> Dale i otation !lours (m m3) (%a) Air Valve (in H ) (%cfm) (in 1120) (° ° Oh/hr) (hrs) (Iblhr) (lbs) <br /> 9128198* Influent 30 370 10%open 21 152 4 675 1 035 02 3 <br /> Effluent <10 >97% <br /> ionigs System restart for full remd anon <br /> 1114198 Influent 6500 3 000 closed 4 75 23 636 649 08 6470 05 341 <br /> Effluent <10 >99% <br /> 1211198 Influent 1 M6 6 500 closed 50 in h2o 118 5 680 801 29 4566 19 848 <br /> Effluent 27 996% <br /> 1!20199 Influent 1,9610 5 100 closed 48 in h2o 125 ]0 680 734 24 8544 26 2 248 <br /> Effluent <10 >99% <br /> Cumulative TPHg Recovery lbs 3,43 <br /> Notes, <br /> TPHg Total Pelrolwm Hydrocarbons as gasoline by EPA Method 8015 <br /> mglm3 milligrams per cubic meter equivalent to micrograms per hler(µg11.) <br /> <ii Compound not detected or assumed less than laboratory reporting limit shown <br /> Data not collected or treasured <br /> * Initial source verification sampling <br /> (REFER TO SVE SYSTEM PROCESS FLOW DIAGRAM) <br /> Influent Sample port at inlet to catalytic oxidizer <br /> Effluent Sample port at catalytic oxidizer exhaust <br /> Avail Vacuum(AV) Vacuum gauge prior to blower <br /> Air Vel(V 1) Flaw velocity gauge inside 3-mch diameter pipe located outside recirculation loop <br /> Ox Press(P2) Oxidizer inlet pressure gauge(0 60 inches water column) <br /> Oxidizer Inlet T(T2) Oxidizer inlet temperature gauge(degrees F)(650°F minimum requned before sod gas is automatically introducted to process stream) <br /> Oxidizer Exhaust T(T2) Oxidizer inlet tLmperature gauge(degrees F)(1 125°F maximum operational temperature auto shut down if exceeded) <br /> TPHg Desi Effie Catox destruction efficiency based upon the following <br /> Equation Effic(%)= [(influent concentration TPHg effluent concentration TPHguinfluent concentration TPHg]x 100 <br /> HC Yield Approximate TAH yield(in ibs/hr)based upon influent analytical data and air flow volume(Q)for a given date <br /> Equation Yield= Influent concentration(mglm3)x Q(scfm)x(mV15 31€13)x 60 minthr x lb1451,592 mg <br /> Yield= lnflui nt concentration(mg/ml)x Q(scfm)x 6 244 E-8 <br /> Opi.rational pLriod Numbi r of hours sin«last me asurLn]Lnt of mllut.nl conUntrattons and air flow(Q) <br /> Ave Yield Average hydrocarbon yield during a given operational period based upon arithmetic average of HC yield at beginning and end of operational period <br /> PLnod Yield The operational period(hours)x average hydrocarbon yield dun ng that penod Note that[his value is an approximation only,and may not account for daily fluctuations in yield <br /> or timcs that the system may be non operational between scheduled site visits <br /> Cumui Recovery Fslimalld total SVE system contaminant recovey since startup <br /> Page I of I <br />