Laserfiche WebLink
' Site Background Information Chapin Brothers Investements, Inc <br /> . Page 6 of 12 <br /> 1 <br /> FAILED EXTRACTION SYSTEM MAINTENANCEIUPGRADES <br /> ' On 21 July 1997 the 5 horsepower electric motor which serves to power the rotary blower was <br /> removed and delivered to ACE Armature in Stockton Both motor shaft bearings were replaced and <br /> ' minor wear to the contacts were repaired The main rotor shaft was also cleaned and lubricated The <br /> motor was then replaced on the catalytic oxidation unit(SVE unit) <br /> 1 On 05 August 1997 the M-D Pneumatic 3210 rotary lob blower was removed from a King, <br /> Buck/Hasstech (KBH) catalytic oxidation unit(SVE unit) The unit was delivered to Magdeburg <br /> System (the authorized factory service representative) in South San Francisco, for repass and <br /> service The bearings, gaskets and seals were replaced The blowers exhaust valves and solenoid <br /> valves were rebuilt The pump was then tested and painted Major wear was noted to the mechanical <br /> drive shaft bearing and seal(metallic) In the opinion the staff at Magdeburg System this wear was <br /> ' indicative of excessive use and poor maintenance over a long prior of time On 27 August 1997,the <br /> blower was installed and the extraction system began operation <br /> ' On 16 September 1997 a KBH representative visited the site to correct a manufacturing defect in the <br /> SVE unit A temperature controller to the oxidation unit was noted to malfunction,falsely indicating <br /> an excessive temperature in the oxidation chamber, and thereby causing the unit to shut down as a <br /> ' precaution against destruction of the oxidation chamber A new temperature controller was added <br /> to the SVE unit,by KBH <br /> 1 <br /> SPARGING/EXTRACTION SYSTEM OPERATION AND MONITORING <br /> The IAS/SVE system was monitored daily for the first week of operation and weekly thereafter <br /> During each monitoring event, the depth to ground water and percent dissolved oxygen were <br /> ' measured for each monitoring well General system maintenance and adjustments were performed <br /> at this time The sparging flow rate was adjusted to approximately 7 to 10 scfinn and to a minimum <br /> pressure of 15 psi <br /> ' Elevated concentrations of dissolved oxygen were detected in monitoring wells MW-1,MW-2 and <br /> MW-4, as well as observation wells surrounding the ASO-1 well on the site Dissolved oxygen <br /> ' concentrations in the remaining wells,down gradient showed smaller changes The greatest changes <br /> in dissolved oxygen was again observed in monitoring wells closer to the sparging well/points The <br /> dissolved oxygen data is summarized on Table 3 Sparging rates were measured at approximately <br /> ' 7 to 10 scfin during each monitoring event A pressure of approximately 15 was to maintain for the <br /> air sparging flow rate <br /> ' The SVE unit operated at varying rates during the observation period Extraction flow rates were <br /> . calculated to range from 150 to 200 scfm Typically operation averaged at 150 scfin during the <br /> 1 <br /> Advanced GeoEnvironmental,inc. <br />