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The TCLP procedure continues to be the primary hazardous materials toxicity and treatment <br />evaluation method utilized by the EPA. However, with the more recent development of the <br />SPLP extraction procedure, and the methodology behind its development, the SPLP has become <br />increasingly popular as a method of evaluating the potential leaching of hazardous constituents <br />from site materials. <br />The SPLP extraction procedure was initially brought about as a result of a lawsuit brought <br />against the EPA by the Edison Electric Institute, the National Mining Association and several <br />other petitioners to challenge the validity of the TC Rule and the TCLP procedure. The lawsuit <br />stated that the mining industry disposed of their waste in their own on-site landfills and that <br />mixing with municipal wastes did not occur. Therefore, organic acids would not contact the <br />mining wastes and the TCLP would not apply. In connection with this lawsuit, the mining <br />industry petitioned to use the SPLP method to evaluate the potential for leaching of metals from <br />the on-site landfills. <br />The SPLP method was designed by the mining industry to evaluate the potential for leaching <br />metals into the indigenous and surrounding ground and surface waters. This extraction method <br />provides a more realistic assessment of the metal mobility under actual field conditions and <br />simulates the leaching efforts of acid rain / snow. This leaching fluid is intended to simulate <br />precipitation. It is generally the chosen method when evaluating the fate and transport of metals <br />in a properly engineered waste disposal facility when municipal solids are excluded. <br />The SPLP extraction procedure is performed in a similar manner to the TCLP, with the exception <br />of a different leaching fluid composition and method of leaching fluid selection. The SPLP <br />procedure is performed by initially selecting one of two leaching fluids for the analysis. <br />However, the method for selection of the appropriate leaching fluid does not depend on a <br />hydrochloric acid buffering capacity test as in the TCLP procedure. Rather the SPLP leaching <br />fluid is chosen based on the region of the country that the sample was obtained. Specifically, <br />samples obtained fi•oni sites east of the Mississippi require the, use of Leaching Fluid #1 (LF 1), <br />and sites west of the Mississippi require the use of Leaching Fluid #2 (LF 2). LF 1 is composed <br />of deionized water adjusted to a pH value of 4.20:1-- 0.05 s.u. with a 60/40 mixture of sulfuric and <br />nitric acids. LF 2 consists of deionized water adjusted to a pH value of 5.00 :L 0.05 s.u. with a <br />60/40 mixture of sulfuric and nitric acids. The pH values for each of the two leaching fluids are <br />based on the average pH values for the eastern and western United States. The eastern United <br />States typically experiences more acidic precipitation due to air pollution impacts from heavy <br />industrialization and coal utilization. The precipitation in the western United States is typically <br />less acidic since there is less industrialization and smaller population densities, thereby less <br />automobiles. <br />After leaching fluid selection, the sample is extracted in a rotary extractor over a period of 18 2 <br />hours, at which time the extraction is terminated and the sample is filtered. After filtering the <br />leachate is subjected to analyses in a similar manner as the TCLP. <br />The current regulatory trend is an increase in the use of the SPLP leaching method due to more <br />realistic conditions that the test represent. The EPA will mandate, not legislate the use of the <br />SPLP extraction method in on-site disposal of metals waste that does not include municipal