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• <br />have submitted technical revisions to incorporate CKD disposal standards into their reclamation <br />permits. The technical revisions detail the geochemistry of the CKD. ,round water protec[ion <br />measures and monitoring, dust control, 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 include all areas of the operation where CKD is generated, <br />temporarily stored, or transported inro the permit through an amendmen[. From a regulatory <br />standpoint, approval of the amendment makes the CKD an onsue rather than an imporred waste. <br />From a technical standpoint, the cement plant must be included in the reclamation permit area m <br />order to provide regulatory controls over the generation of the CKD, e.g., the types of fuel or <br />chemicals used in [he kilning process, which may effect the geochemistry of [he CKD. In <br />particular. if a cement plan[ were to begin using alternative fuels such as wood, tires, or waste <br />oil, the potential changes to the nature of the CKD should be evalua[ed. <br />This memo 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 CICD are provided for <br />background. <br />The Holnam-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 some groundwater monitoring, and <br />the Division is processing a TR for continued CKD disposal at [he Portland plant. Based on (a) <br />leach test results, (b) chemical analysis of pit water adjacent to one of the quarries, and (c) CKD <br />waste handling commitments, groundwater monitoring may be perfunctory in some cases <br />because the potential for off-site damage is limited. The latter point - "GIGO waste handling <br />comritments" -was most important in reaching that determination and is discussed in the <br />following sections. <br />PRODUCTION, CHENIISTRY, AND PROPERTIES OF CEMENT <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, free water is driven off. Next, calcination occurs as bound water and <br />carbon dioxide are liberated. After calcination, the limestone has been converted to lime (Ca0). <br />in the third or clinkering stage, lime and decrepitated clay combine to Form calcium silicates and <br />calcium aluminates (see equations following). The fourth stage involves cooling of the clinker. <br />In some cement plants, the firs[ three steps all occur in the same kiln; in other plants, the process <br />occurs in separate calciners and cement kilns. <br />CaCO; + [SiO, + AhO; + Fe,O} + H,O(bound)] + n <br />(limestone) (clay) (heat) <br />-~ 3CaO~SiO, + 2CaO SiO, + 3CaO A1;03 + =4CaO AhO; Fe;O; <br />(mcatcium silicate) + (dicalnum silicate) + Qncalaum aluminate) + (tetracalcium aluminokniie) <br />Compounds on the product side of the above equation comprise about 90 percent of portland <br />cement. The two calcium silicates form approximately 75 percent of cement by weight. When <br />water reacts with the two calcium silicates, tobermorite gel and calaum hydroxide are produced. <br />3 <br />