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Canepa's Car Wash-Soil Vapor Extraction(SVE)System-Vapor Phase Carbon(Authority To Construct Pennit No N-174-2-1) 5
<br /> SVE Carbon System Flo 11 Soil Vapor Concentration(PID measurent)
<br /> b-at-c-7 Technician System on? Influent("H20) Influent(Fdhlin) lnfluent CFhl LEffluent{"H20} Effluent(Ft/Min) Effluent CFM Influent(ppm) Between Tank(prim) Effluent( rn) Nates
<br /> 3/13/2002 MY Started 0.75 to 1.3 3,900 191 3.6 7,600 177 111 0 0
<br /> 31 1 512002 R1YlBA C. on 0.65 to 1.5 3,900 191 3.8 7,800 182 92 1.3 0
<br /> 317-5/2002 Bill C. an 0.4 too.9 3,225 158 3.3 7,300 170 70 0 0,5 slight leak near influent port
<br /> 4/112002 Bill C,. on 0.6 to 0.8 3,338 164 3.2 7,175 167 70 0 1.1 slight leak near influent pull
<br /> 4!9!2002 Bill C. on 0.6 to 0,8 3,338 164 3.2 7,175 167 63 0 0 leak fixed
<br /> 4/15/2002 Bill C. on 0.6 to 0.8 3.338 164 3.7 7,700 179 67 0 0
<br /> 412 1/2002 Bill C. on 0.7 3.325 163 3.8 7,800 182 65 0.7 0.7
<br /> 4/29/2002 Bill C. on 0.7 3,325 163 3.7 7,700 179 59 1 0 0
<br /> 51212002 Rab Y. on 0,6 to D.7 3,100 152 3.8 7,800 182 50 0 D
<br /> 5/6/2002 Bill G. on 0.6 3.200 157 3.7 7,700 179 57 1.3 1.3
<br /> 5113n-002 Bill C on 0.6 3,200 157 3.5 7,500 175 51 0 0
<br /> 5/20/2002 Bill C. on 0,7 3.325 163 3.6 7,600 177 51 0 0
<br /> 5/28/2002 Bill C. on 0.6 3,200 157 3.7 7,700 179 43 0 0
<br /> 614/2002 Bill C. on 0.6 3,200 157 3.8 7,800 182 47 0.6 0.6 4 gal. water in KIO dnma
<br /> 6/11/2002 Bill G. on 0.6 3,200 157 3.8 7,800 182 56.3 0 0
<br /> 6/17/2002 Rob Y. off NM NM -- NM NM NN1 Blower drive belts broken,
<br /> 6/26/2002 Bill C. restart s YsUxn NNI NM NM NM NM Changed belts and lubricants
<br /> 6/27/2002 Bill C. on 0.6 3,200 157 3.5 7,500 175 46 D 0 K/O drums emptied 6121102
<br /> 7/3/2402 Bill Q. on 0,6 3,200 157 3.7 7,700 179 53 0.8 0
<br /> 7/912002 Bill C. on 0.6 3,200 157 3.7 7,700 179 37 0 0
<br /> 7/17/2002 Bill C, on 0.6 3,200 157 3.6 7,600 177 35 1.5 0
<br /> 7/2512002 Bill C. on 06 3,200 157 3.6 7,600 177 34 1.8 0
<br /> 7/30/2002 Bill C. on 0.6 3.200 157 3.6 7,600 1 177 56.2 20.2 O.4 0 gaHons water in K10 tank
<br /> Note:All measurements assume standard temperature and pressure.Flow velocity treasured using a Dwycr 166-6 piton tube.
<br /> Measurement of air velocity assumes dry air at 70 Fahrenheit,.29.9 inches of Hg Barometric Pressure,and a density of air of 0.075 lb/cubic foot.Velocity converted to FtlMin using
<br /> the manufaclurces provided pressure vs.velocity curve.
<br /> The influent duct diameter is 3 inches.
<br /> The effluent duct diameter is 2 inches.
<br /> The influent flow velocity has been observed to fluctuate and therefore,the mean velocity is used to calculate the flow rate.
<br /> NM=Nut measured
<br /> Table of Canepa s Vapor Phase Carbon Treatment SVE System Laboratory Analytical Results _
<br /> Date Sample ID benzene toluene ethyl benzene xylenes MTBE TPH-G OVM(PPM)
<br /> 3/13/2002 1707B=Inlet-3/13/02-1441! 0.75 1.3 0,47 5.2 <l.5 NA Ill
<br /> 3/13/2002 1707B-Mid-3113102.1443 <0.15 <0.15 <0.15 <0.25 <1.5 NA 0
<br /> 6/11/2002 1707B-Inleb6/l1/02 <0,I5 <O.15 0.33 4.0 <1.5 43 56.3
<br /> 6111/2002 170713-Midtanks-6111102 <0.15 <0.15 <0.15 <025 <L5 <15 0
<br /> 6/1112002 1707B-Exhaust-6111/02 <0.15 <0.15 <0.15 <0.25 <1S <15 0
<br /> Note:Air matrix units are reported as ppnty(µIDL).
<br /> NA=Not Analyzed
<br /> Canepa's SVE Vapor Phase Carbon2002 Carbon SVE
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