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2.5 Geochemistry  89
                         ascertained by accurate enthalpy data or by gas geochemistry (Giggenbach, 1980;
                         Bertrami et al., 1985).
                           The geothermal wells, which tap a single liquid phase at temperatures above
                            ◦
                         100 C under reservoir conditions, obviously discharge two-phase liquid–vapor
                         mixtures, which are generated through boiling of the original single liquid phase.
                         Sampling and analysis of both liquid and vapor phases, separated at known
                         pressure and temperature conditions, are required to recalculate the composition
                         of the original single liquid phase (Drummond, 1981). The two phases can be
                         separated by means of a wellhead pressure separator. When samples of separated
                         liquid and vapor phases are collected from a geothermal well, it is necessary to
                         know the separation temperature and/or pressure and the well-bottom temperature
                         and/or pressure and total discharge enthalpy (steam to water ratios).
                           Where boiling (steam separation) occurs there is a partitioning of dissolved
                         elements between the steam and the residual liquid; dissolved gases and other
                         relative volatile components concentrate in the steam and nonvolatile components
                         become concentrated in the liquid in proportion to the amount of steam that
                         separates. When steam separation takes place, the less soluble gases (e.g., N 2 ,
                         H 2 ,CH 4 , and CO) enter preferentially the vapor phase, while the more soluble
                         gases (CO 2 ,H 2 S, and NH 3 ) are retained in part in the aqueous phase (Truesdell,
                         1975).
                           The physical mechanisms of boiling processes are extremely complicated. Two
                         limiting mechanisms of boiling can be recognized (Arnorsson, 2000; Tonani,
                         1970): single-step separation, where the steam, continuously produced by decom-
                         pression of the uprising liquid, remains in contact and in equilibrium with the
                         liquid until it is separated in a unique separation event; and continuous sepa-
                         ration, where the steam is continuously separated from the liquid as soon as it
                         forms. An infinite number of intermediate mechanisms can also exist (multistep
                         separation).
                           However, hot waters ascending from a geothermal reservoir may cool in upflow
                         zones not only conductively and/or by boiling due to depressurization but also by
                         mixing in the upflow with shallow, relatively cold water. Since cold waters are most
                         often lower in dissolved solids than geothermal waters, mixing is often referred to
                         as dilution. Large variations in the temperature and flow rates of thermal springs
                         in a particular field that can be linked with parallel variations in the concentrations
                         of nonreactive components in the water, such as Cl, usually constitute the best
                         evidence that mixing has occurred (Marini and Cioni, 1985).
                           Mixing models have been developed to allow estimation of the hot water
                         component in mixed waters emerging in springs or discharged from shallow drill
                         holes (Truesdell and Fournier, 1977). There are essentially three kinds of mixing
                         model:

                         • the chloride–enthalpy mixing model;
                         • the silica–enthalpy warm spring mixing model;
                         • the silica–carbonate mixing model.
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