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<br />have submitted [ethnical rzvisions to incorporate ChD disposal standards into their reclamation <br />permits. The [ethnical revisions detail [hz geochemistry of [he CKD, ;round water protection <br />measures and monitorrng, dust convol, and closure and reclamation. The procedure being <br />Followed by the DMG is to incorporate the CKD disposal standards into the permit through the <br />technical revision process, then to includz all areas of [he operation where CKD is generatzd. <br />temporarily stored, or transported into [he permit through an amendment. From a regulatory <br />standpont, approval of the amendment makes thz CKD an onsite rather than an imported waste. <br />From a technical standpoint, [he cement plant must be included in the reclamation permit area in <br />order [o provide regulatory controls over [he genzration of the CKD, z. g., the types of fuel or <br />chemicals used in thz kilning process, which may effect the geochemistry of [he CKD. In <br />particular, if a cement plant were [o begin using alternative fuels such as wood, tires, or wastz <br />oil. the potential changes [o the nature of the CICD should be zvaluated. <br />This mzmo discusses some of the details of CKD generation and disposal at the three <br />Colorado cement plants. A discussion of the geochemistry of cement and CKD are provided for <br />background. <br />The Hotnam-Boettcher operation and the Southdown-Lyons operation have completed waste <br />characterization studies and have established groundwater monitoring programs. The Holnam- <br />Portland operation has completed waste characterization and ;ome groundwater monitoring, and <br />the Division is processing a TR for continued CKD disposal at the Portland plan[. Based on (a) <br />leach test results, (b) chemical analysis of pit water adjacent [o one of the quarries, and (c) CKD <br />wastz handling commitments, groundwater monitoring may be perfunctory in some cases <br />because the potential for off-site damage is limited. The latter point - "CKD waste handling <br />commitments" -was most important m reaching that determination and is discussed in the <br />following sections. <br />PRODUCTIOY, CHENIISTRY, AND PROPERTIES OF CEivIENT <br />Cement is produced by burning limestone and clay at around ?700°F in a horizontal, inclined <br />rotary kiln. It can take up to 2 hours for the raw materials to pass through the kiln depending on <br />its length. Moving down the cylinder, the mixture progresses through four stages of <br />transformation. Initially, fret water is driven off. Next, calcination occurs as bound water and <br />cazbon dioxide are libzrated. After calcination, the limestone has been converted to lime (CaO). <br />In thz third or clinkering stage, Lime and decrepitated clay combine ro form calcium silicates and <br />calcium alurninates (see equations following). The fourth stage involves cooling of the clinker. <br />In some cemzn[ plants, the first three steps all occur in the same kiln; in other plants, the process <br />occurs in szpazate calciners and cement kilns. <br />CaCO; + (SiO~ + AhO; + Fe,O~ + H~O(bound)] + n <br />(limestone) (clayj (haaq <br />--~ 3Ca0 SiO; + 2CaO SiO, + 3CaO AhO; + 4CaO A1,O;~Fe,O; <br />(iricalnum siVic~[e) + (dicalcium sillnte) + (tricnlcium ~luntinme) + (ee~ncalnum aluminofarnte) <br />Compounds on the product side of thz above equation comprise about 90 percent of portland <br />cement. The two calcium silicates form approximately 7~ percent of cement by weight. When <br />water reacts with the two calcium silicates, tobermonte gel and calcium hydroxide are produced. <br />3 <br />