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<br />I <br />I r~'J <br />I <br />I r- <br />! <br />I 00 <br />, i,._ <br />! (.. <br /> c: <br /> <br />have the ability to grow and function at salinities <br />seawater, are able to over-winter or produce a full <br />seven months, and can tolerate extended periods of <br />Each also appears to have multiproduct potential, <br /> <br />These species <br />equivalent to <br />crop within <br />inundation. <br /> <br />Site Selection <br /> <br />Criteria were established to guide the selection of sites for process <br />implementation, The desirable characteristics of a site for STEP <br />operations were identified as open, level terrain, exposed to wind <br />and sun, located within the protective shield of the Grand Valley. A <br />prime determinant is soil composition, principally sands and silt, <br />with minimal clay and organics; this would be classified as marginal, <br />undesirable agricultural land. <br /> <br />Data Limitations <br /> <br />The available data are deficient in the quantitative definition of <br />upper salinity tolerance limits within emergent halophytes, including <br />the impact of high salinity on halophyte growth and <br />evapotranspiration rates, as well as product opportunities. These <br />effects must be known in order to engineer and cost the STEP process <br />facilities; this also applies to the development of operational <br />procedures and mana~ement strategies appropriate for the plants and <br />the process, <br /> <br />The criteria provided as guidelines to DEC during its development of <br />preliminary conceptual engineering designs of the STEP process were <br />the same as given in Table 1, except that evapotranspiration data <br />then available indicated rates at ,75 inches per day could reasonably <br />be expected, based on reports that may not have corrected for oasis <br />and large pond effects. Similarly, short-term salinity tolerance <br />levels were believed near 77,000 mg/l, based on inputs received from <br />professional consultations. While that level may remain achievable, <br />insufficient experience at this concentration is shown by the <br />available literature. IBR thus reduced its expectation to 40,000 <br />mg(l, a value that is readily supportable, bnt after DEC had <br />completed its preliminary design and costing efforts, As a result, <br />the preliminary designs prepared by DEC are based on different <br />performance criteria. It is shown in Chapter Four that the impact <br />of this difference is not on the desi~n concept, but rather on area <br />requirements for pond facilities. <br /> <br />PRELIMINARY CONCEPTUAL ENGINEERING DESIGN <br /> <br />The STEP process flow sheet developed by DEC is shown as Figure 2. <br />This shows that 12,236 acre-feet of saline water is transported <br />annually via pipeline to spray evaporation cooling ponds. The <br />function of these ponds is to regulate the input water temperatgre so <br />as not to exceed the upper temperature threshold (taken us 86 F) of <br />the STEP crops: it is recognized that these ponds may not be needed, <br />Cooled saline waler is input to STEP crop production ponds where <br />water is consumed through evapotranspiration and feeds, chemicals, <br />and materials are prodnced, The output from the production ponds <br />passes into spray evaporation ponds for concentrating to saturated <br />E-:; <br />