Laserfiche WebLink
<br />. <br /> <br />^ <br /> <br />.;. <br />N <br />~ <br />~ <br /> <br />, <br />, <br /> <br />. <br /> <br />. <br /> <br />., <br /> <br />'.. <br /> <br />.' <br /> <br />been brought to the surface during the procluction of gas sncl oil. The oil <br />fielcl brines are usually reinjected into the same formation in which they <br />originated, ancl there is presently a consiclerable effort in using the rein- <br />jected brine in the secondary recovery of oil. <br /> <br />Injection wells have also been used for the permanent undergrouncl storage <br />of inclustrial wastes, radioective wastes, "Wastes from small scale c1esalination <br />plants ancl some from advancell waste treatment plants. However, the injection <br />of these wastes has usually been on a fairly low volume at less than 3.16 Ips <br />in wells ancl on a short-term basis, unless some types of unclerground chsmbers <br />had been preparecl. For example, chambers have been made in salt c10mes for <br />waste disposal ancl oil storage in places where the brine prollucecl by the <br />making of these chambers coulcl be c1isposecl by other means. Another method of <br />making. chambers is the use of nuclear explosives which has been demonstrated. <br />in Coloraclo and Wyoming to help in natural gas procluction as part of the <br />... ".Plowshare Program. <br /> <br />Deep well injection is generally not a long-ierm solution to a continuous <br />'1J:isposal progrem. because of reservoir limitation and the need to drill new <br />wells at further ancl further c1istances from the eource. The new wells are <br />very expensive to construct and new piping systems are requirecl. Bouwsr <br />(1974) indicated that well costs, up to about 1,000 meters deep in 1974, were <br />about $160/m. In 1980, these costs "Would be about $265/m. Deeper wells would <br />be much more expensive on a unit cost basis because of the different types of <br />equipment required. In acldition, the pressures involved in t:he injection <br />process often exceed 100 atmospheres, and the pumping power requirement can be <br />large. <br /> <br />(#;\ <br /> <br />{j:< <br /> <br />"I, <br /> <br />Other Brine Disposal Possibilities-- <br />The USDI, WPRS (1980a) is presently assessing several alternatives to the <br />brine disposal problems for their salinity control projects in the Colorado <br />River Basin. One possible alternative which they are examining is supplying <br />the brine water to industries, such as oil shale, for their use. Another <br />possibility is to construct a collection system and convey all of the brine to <br />a suitable salt sink such as Sevier Lake in Utah or even to the Pacific Ocean. <br /> <br />Collection, Treatment, and/or Disposal of Other Saline Flow-- <br />The Upper Colorado River Basin contains a number of natural saline seeps,,., <br />ancl springs which adcl substantial amounts of salt to the river. . Alternatives <br />for eliminating these salts include desalination as discussed earlier ss well <br />as c1irect collection and disposal through evaporation pond to c1eep well injec- <br />tion. The desalination cost-effectiveness for the nature saline springs ancl <br />seeps are the same as c1escribed for the treatment of agricultural return <br />flows. <br /> <br />",.~ <br /> <br />,"", <br /> <br />Hagan (1971) ancl EPA (1971) estimated that the salinity contribution from <br />point sources in the Upper Colorado River Basin is about 9 percent of the <br />total salt loacl at Lee's Ferry, Arizona. The majority of these point sources <br />are thermal springs, and Iorns et al. (1965) calculated that the annual dis- <br />charge anll dissolved solids concentration by all the thermal springs in the <br />upper basin to ba 7,287 ha-m ancl 491,500 .Mgm, respectively. Divicling the <br />flow and concentrations due to thermal springs among the three c1ivisions is <br /> <br />67 <br />