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New York/ New Jersey Harbor: Alternative Methods for Ex ... - CLU-IN

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water mixture is heated to 172 to 185°F, a span of temperatures which corresponds to the<br />

range of boiling points of typical azeotrope solvent-water mixtures (2-8). As a result,<br />

when the azeotrope is heated to these temperatures, it volatilizes. The azeotrope vapor is<br />

then condensed into waste oil and a 2-layer liquid, which consists of a top layer of<br />

solvent and an aqueous bottom layer. An oil polisher is used to remove the residual<br />

solvent present in the waste oil. The polished waste oil is sent to an off-site facility to be<br />

incinerated or disposed of in some other manner (Cardoni, interview). The solvent layer<br />

of the azeotrope can be decanted off of the aqueous layer and used in the extraction<br />

process. The water layer is drained from the vessel and is steam stripped to remove<br />

residual solvents (Metcalf & Eddy, 2-9).<br />

The wastewater layer is transported to a stripper column where any residual solvents are<br />

removed by steam stripping. Organic compounds with lower boiling points can be<br />

isolated by injecting steam into the sediment. Other organic compounds can be removed<br />

from the wastewater or condensate by feeding water, just below the azeotropic boiling<br />

point through the feed preheater. A portion of this feedwater vaporizes upon entering the<br />

top of the column, and the remainder is stripped of residual solvents by upflowing steam<br />

(2-10). The vapors produced by the stripping process are condensed and used again as<br />

solvent in the extraction process.<br />

The continuous solvent extraction process is identical to the batch solvent extraction<br />

process, with a few modifications. The sediment must be screened to 1/8“ instead of<br />

1/4“. Also, instead of periodically decanting the solvent and water azeotropic layer from<br />

the sediment after extraction, the continuous process separates the two layers without<br />

interruption during extraction. In the continuous process, the sediment is allowed to<br />

escape through the bottom of the column, and the solvent is removed through the top of<br />

the column. The solvent recovery, organic separation, and water stripping steps are the<br />

same <strong>for</strong> both extraction processes.<br />

The final step in the process, the SOLFIX solidification and stabilization step, involves<br />

the addition of Portland cement to the sediment. As mentioned in The Process portion of<br />

36

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