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<br /> <br /> <br />1 <br /> <br />t <br /> <br />I <br />i~ <br />t:~t f3atier <br />April s, zvuz <br />Page 4 Sc.i~s~~w~-~~<LCl.4 <br />been achieved, reportedly without adverse surface and subsurface ~ rbsidence effects. "fhe <br />estimated shape and size of the active Panel I cavities are shown in I~ig re 4. Cavity shapes in <br />the ligure represent nahcolilc recovery confined to the I3oies I3ed. Sli~Jllly nan'ower caverns are <br />expected if recovery has occurred above the Upper Qoies Qed (U[3f3j. While the actual size and <br />shape of the cavities at any one location is uncertain, ligure 4 provides a~'rsa~rttrb}c~"estimate of <br />the global shape of the cavities based on fhe historical location of injection and recovery points <br />and the anticipated variation oFliqua• solvency along the solution stream. <br />Panel 2 Mining Plans <br />Planned extraction ratios will remain nominally the same (40%4) for most Panel 2 <br />solution mining. Locally, however, higher extraction ratios are possible. Like Panel 1, cavities <br />are located on 220-ft centers separated by intervening strip pillars (Pigw~e 1). Plans call for <br />intersecting the four westernmost Panel 2 cavities with Cavity #lA to take advantage of existing <br />development and enhance production. In the vicinity of the cavity intersections, potential exists <br />for attaining volumetric extraction ratios substantially larger than previously achieved or <br />considered by previous designs (i.e. >40%). <br />Cavity growth is illustrated in figures 5 and 6 for the plamted flow scheme. Carly plans <br />are to double the current injection rate (450-500 gpm to 900-1000 gpm in well WRNM lA-4I-[) <br />to support two production wells (WRNM lA-SFI and proposed well SH). Figure 5 illustrates the <br />possibility of substantial cavity growth resulting from increased solvent flow immediately <br />downstream from the primary injection point. Further downstream, the flow will be split <br />between cavities #lA and #5. Cavern growth is likely to diminish substantially downstream of <br />this point due to halved flow rates and increased saturation of the solution stream. Later-stage <br />cavity growth is described by Figure 6. The fgure illustrates the potential for very large cavities <br />after all four western Panel 2 wells have been brought into production. <br />Notably, the potential for very high extraction and large cavities is not exclusive to the <br />flow scheme described in fhe figures. Similar potential exists for other flow schemes which <br />might utilize Cavity #lA and/or high flow rates for long periods of time. However, cavity size <br />for any plan is practically limited by diminishing dissolution efficiency with increasing cavity <br />width. Mechanisms governing dissolution efficiency include thermal loss, flow channelization, <br />face blinding, ore burial under insolubles, and flow restrictions resulting from roof collapse. For <br />these and other reasons, the likelihood of attaining very high extraction ratios decreases rapidly <br />beyond a certain limit. This effect is described schematically in Figure 7. The complexity of the <br />dissolution process and natural geologic variability make auy estimate of this practical limit <br />uncertain. However, experience in Panel 1 suggests such a limit exceeds the current design <br />target of 40%4, giving rise to the possibility of attaining very high extraction ratios for any one of <br />a variety of flow schemes should economics alone control resource recovery. <br />' In the event that very high extraction ratios are achieved, Uiere will be increased risk of <br />disturbing the overlying USDW aquifers and Mahogany oil shale resource. Geoteclmical <br />consequences of very high to complete extraction include increased caving and fracturing in the <br />. overburden and subsurface/surface subsidence. These effects are likely to extend greater <br />Agapito Associates, hie. <br />