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Inst 2014136383
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Inst 2014136383
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6/23/2014 11:50:09 AM
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6/23/2014 11:46:59 AM
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CM City Clerk-City Council
CM City Clerk-City Council - Document Type
Agreement
Document Date (6)
9/16/2013
Recorded Document Type
Stormwater Treatment
Retention
PERM
Document Relationships
Inst 2013362145
(Superseded)
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\City Clerk\City Council\Recorded Documents\2013
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he identified-during inspection. It is useful and often required as Cleaning <br /> part of a permit to keep a record of each inspection. A simple <br /> Cleaning of the CDS systems should be done during dry weather <br /> form for doing so is provided, conditions when no flow is entering the system. Cleanout of <br /> Access to the CDS unit is typically achieved through two manhole the CDS with a vacuum truck is generally the most effective and <br /> access covers. One opening allows for inspection and cleanout convenient method of excavating pollutants from the system. <br /> of the separation chamber(screen/cylinder)and isolated sump. Simply remove the manhole covers and insert the vacuum hose <br /> The other allows for inspection and deanout of sediment into the sump. The system should be completely drained down <br /> captured and retained behind the screen. For units possessing and the sump fully evacuated of sediment. The area outside the <br /> a sizable depth below grade(depth to pipe), a single manhole screen should be pumped out also if pollutant build-up exists in <br /> access point would allow both sump deanout and access behind this area. <br /> the screen. In installations where the risk of petroleum spills is small, liquid <br /> The CDS system should be cleaned when the level of sediment contaminants may not accumulate as quickly as sediment. <br /> has reached 75%of capacity in the isolated sump and/or when However,an oil or gasoline spill should be cleaned out <br /> an appreciable level of hydrocarbons and trash has accumulated. immediately. Motor oil and other hydrocarbons that accumulate <br /> If sorbent material is used, it should be replaced when significant on a more routine basis should be removed when an appreciable <br /> discoloration has occurred. Performance will not be impacted layer has been captured.To remove these pollutants,it may <br /> until 100%of the sump capacity is exceeded however it is be preferable to use adsorbent pads since they are usually less <br /> recommended that the system be cleaned prior to that for easier expensive to dispose than the oil/water emulsion that may be <br /> removal of sediment; The level of sediment is easily determined created by vacuuming the oily layer. Trash can be netted out if <br /> by measuring from finished grade down to the top of the you wish to separate it from the other pollutants. The screen <br /> sediment pile. To avoid underestimating the level of sediment should be power washed to ensure it is free of trash and debris. <br /> in the chamber; the measuring device must be lowered to the <br /> top of the sediment pile carefully. Finer, silty Manhole covers should be securely seated following cleaning <br /> p y ty particles at the top activities to prevent leakage of runoff into the system from above <br /> of the pile typically offer less resistance to the end of the rod and also to ensure proper safety precautions. Confined Space <br /> than larger particles toward the bottom of the pile. Once this <br /> Entry procedures need to be followed. Disposal of all material <br /> measurement is recorded,it should be compared to the as built removed from the CDS system should be done is accordance <br /> drawing for the unit to determine if the height of the sediment with local regulations. In many locations, disposal of evacuated <br /> pile off the bottom of the sump floor exceeds 75%of the total sediments may be handled in the same manner as disposal of <br /> height of isolated sump. sediments removed from catch basins or deep sump manholes. <br /> Check your local regulations for specific requirements on <br /> disposal. <br /> to <br /> 'rte€'i ` s' ' <br /> f 4., .'''4;: t..,; 1)01- -` ` ,: . 9 .' R .'k2 4,4 Ah <br /> r.A <br /> tea. ,„ <br /> i'4:, .� may' - ' _ p 6; ' s 1/ <br /> 9 ;fit ''.4 :„;.1 ,�, <br /> 1, <br /> o,,' ---. <br /> 5 <br />
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