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1321 - Office of Legacy Management - U.S. Department of Energy

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FDF Subcontract No. 98SC000001<br />

IT Project No. 773481<br />

I <strong>1321</strong><br />

Description <strong>of</strong> opaption & process<br />

IssueDatc 2/13/98 Rev.B<br />

The following sections discuss management <strong>of</strong> the five site water categories given above.<br />

Routing <strong>of</strong> water to the Clearwell (part <strong>of</strong> the request to the Ohio EPA explained above) is<br />

included in these sections where appropriate.<br />

2.8.1 Process Wastewater<br />

The following is a list <strong>of</strong> process wastewater sources:<br />

Cooling tower blowdown water<br />

Water purged from the APC system oivwater separator<br />

BackwasWrecycle water fiom the IT WTS.<br />

These streams will remain relatively constant throughout operations at the site and are not<br />

expected to change during the various excavation phases. The sections below describe the<br />

method by which the water will be collected and transferred to the WTS, the expected flow rate,<br />

and notes on the chemical composition <strong>of</strong> each stream.<br />

2.8.1.1 Cooling Tower Blowdown Water<br />

A blowdown stream from the cooling tower in the dryer system will be routed to the Clearwell<br />

for subsequent treatment by the WTS. This stream is expected to be approximately 40,320 gpd<br />

and is not expected to contain contaminants at levels higher than the BSL WAC.<br />

2.8.1.2 OiYWater Separator Discharge<br />

Process water generated by the APC system associated with the thermal dryer will be combined<br />

and routed through an oiywater separator for removal <strong>of</strong> any free-phase organics. The aqueous<br />

stream fiom the oiYwater separator will be pumped to the fluent tank in the WTS. This stream<br />

is not expected to exceed 47,520 gpd.<br />

2.8.1.3 Backwashhtecycle Water from the WTS<br />

Water generated during the backwashing <strong>of</strong> the sand filter and ion exchange beds in the WTS is<br />

piped to flow directly to the Clearwell. The line pressure supplied by the backwash will be<br />

sufficient to transfer the water to the Clearwell, no additional pump is necessary. The average<br />

flow <strong>of</strong> backwash water fiom the WTS to the Clearwell is approximately 15,000 gpd. This<br />

--<br />

stream will have a high suspended solids concentrati6.<br />

KN/39571WPRAPIEUEL.W2-20-98(909 m)lDl/NE 17<br />

*<br />

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