corrosive species and scaling in wells at olkaria ... - Orkustofnun
corrosive species and scaling in wells at olkaria ... - Orkustofnun
corrosive species and scaling in wells at olkaria ... - Orkustofnun
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product may contribute as well as the presence of equilibrium steam <strong>in</strong> the aquifer. In calcul<strong>at</strong><strong>in</strong>g<br />
aqueous <strong>species</strong> distribution <strong>in</strong> the aquifer w<strong>at</strong>er such equilibrium steam was assumed not to be<br />
present. Calcul<strong>at</strong>ed vari<strong>at</strong>ion <strong>in</strong> the calcite s<strong>at</strong>ur<strong>at</strong>ion st<strong>at</strong>e upon adiab<strong>at</strong>ic boil<strong>in</strong>g is considerably more<br />
accur<strong>at</strong>e than calcul<strong>at</strong>ion of the absolute s<strong>at</strong>ur<strong>at</strong>ion st<strong>at</strong>e. Upon boil<strong>in</strong>g degass<strong>in</strong>g of the w<strong>at</strong>er with<br />
respect to CO 2 generally causes an <strong>in</strong>itially calcite s<strong>at</strong>ur<strong>at</strong>ed w<strong>at</strong>er to become supers<strong>at</strong>ur<strong>at</strong>ed. This is<br />
particularly the case with w<strong>at</strong>ers high <strong>in</strong> CO 2 such as <strong>in</strong> Olkaria West <strong>and</strong> where aquifer temper<strong>at</strong>ures<br />
are around 200°C but CO 2 solubility <strong>in</strong> w<strong>at</strong>er <strong>at</strong> m<strong>in</strong>imum around 200°C. In rel<strong>at</strong>ively high<br />
temper<strong>at</strong>ure <strong>and</strong> low CO 2 w<strong>at</strong>ers, such as <strong>at</strong> Nesjavellir, early boil<strong>in</strong>g may only cause limited<br />
degass<strong>in</strong>g <strong>and</strong> not calcite supers<strong>at</strong>ur<strong>at</strong>ion. Prolonged depressuriz<strong>at</strong>ion boil<strong>in</strong>g, which leads to a<br />
decrease <strong>in</strong> fluid temper<strong>at</strong>ure, decreases the calcite s<strong>at</strong>ur<strong>at</strong>ion <strong>in</strong>dex due to the retrograde solubility of<br />
calcite with respect to temper<strong>at</strong>ure. This often causes boiled geothermal w<strong>at</strong>ers to be calcite<br />
unders<strong>at</strong>ur<strong>at</strong>ed. Calcite <strong>scal<strong>in</strong>g</strong> is not expected to be a problem <strong>at</strong> Olkaria <strong>and</strong> Nesjavellir <strong>and</strong> neither<br />
<strong>at</strong> Svartsengi <strong>and</strong> Reykjanes if the first depth level of boil<strong>in</strong>g is outside <strong>wells</strong> i.e. <strong>in</strong> the produc<strong>in</strong>g<br />
aquifers.<br />
Scal<strong>in</strong>g tests <strong>at</strong> Nesjavellir showed th<strong>at</strong> <strong>at</strong> high temper<strong>at</strong>ures of the wellheads of <strong>wells</strong> NJ-14 <strong>and</strong> NJ-<br />
22, the two phase fluids deposited scales th<strong>at</strong> were dom<strong>in</strong>antly sulphide phases <strong>in</strong> well NJ-14 fluids<br />
<strong>and</strong> mixed sulphides <strong>and</strong> oxides <strong>in</strong> the case of well NJ-22. The scales were essentially amorphous to<br />
X-rays. There were however, some <strong>in</strong>dic<strong>at</strong>ions of some m<strong>in</strong>eral phases <strong>in</strong> the scales such as<br />
chalcopyrite <strong>and</strong> clayey m<strong>at</strong>erial. Separ<strong>at</strong>ed w<strong>at</strong>ers after the he<strong>at</strong> exchangers, entry to the retention<br />
tank <strong>and</strong> <strong>at</strong> the <strong>in</strong>jection well deposited ma<strong>in</strong>ly amorphous silica but there are also some <strong>in</strong>dic<strong>at</strong>ions of<br />
the presence of clays <strong>in</strong> the scales. The r<strong>at</strong>e of deposition of ~0.261 mm/yr was highest <strong>at</strong> the entry to<br />
the retention tank <strong>and</strong> much lower of ~ 0.0168 mm/yr <strong>at</strong> the <strong>in</strong>jection well. Silica polymeris<strong>at</strong>ion<br />
occurs <strong>in</strong> the retention tank <strong>and</strong> this reduces the r<strong>at</strong>e of silica deposition <strong>at</strong> the <strong>in</strong>jection well. At entry<br />
to the retention tank, the high r<strong>at</strong>e of deposition could be due to supers<strong>at</strong>ur<strong>at</strong>ion by monomeric silica<br />
which causes a higher r<strong>at</strong>e of precipit<strong>at</strong>ion (Yanagase et al., 1970; Rothbaum, 1979). An <strong>in</strong>termedi<strong>at</strong>e<br />
test site between the steam separ<strong>at</strong>ors <strong>and</strong> the wellheads could be chosen to <strong>in</strong>vestig<strong>at</strong>e the type of<br />
scales th<strong>at</strong> would form.<br />
The solute content of the w<strong>at</strong>er discharged from the <strong>at</strong>mospheric silencer of Olkaria well OW-34 is<br />
high The discharge enthalpy of the well fluids is close to th<strong>at</strong> of dry steam lead<strong>in</strong>g to extensive<br />
evapor<strong>at</strong>ion of the w<strong>at</strong>er fraction <strong>in</strong> the discharge by depressuriz<strong>at</strong>ion boil<strong>in</strong>g to a low pressure. This<br />
extensive evapor<strong>at</strong>ion is thought to be the cause of the high salt content of the w<strong>at</strong>er discharged <strong>at</strong><br />
<strong>at</strong>mospheric pressure as well as the extensive amorphous silica scale form<strong>at</strong>ion.<br />
A solution to this <strong>scal<strong>in</strong>g</strong> problem <strong>in</strong>volves mix<strong>in</strong>g of the discharge of well OW-34 with separ<strong>at</strong>ed<br />
br<strong>in</strong>e or condens<strong>at</strong>e from another well e.g. well R-3 where separ<strong>at</strong>ed br<strong>in</strong>es from the Olkaria II plant<br />
are be<strong>in</strong>g re-<strong>in</strong>jected to lower the discharge enthalpy of OW-34. This will reduce the amount of<br />
evapor<strong>at</strong>ion of w<strong>at</strong>er <strong>in</strong> well OW-34. Theoretical calcul<strong>at</strong>ions based on mass balance equ<strong>at</strong>ions,<br />
chloride concentr<strong>at</strong>ion of spent br<strong>in</strong>e be<strong>in</strong>g re-<strong>in</strong>jected <strong>in</strong> well R-3 <strong>and</strong> th<strong>at</strong> of well OW-34 for<br />
purposes of dilut<strong>in</strong>g the w<strong>at</strong>er have been tried. In this way aqueous silica concentr<strong>at</strong>ions will not build<br />
up to the same extent <strong>and</strong> amorphous silica deposition will be reduced or <strong>in</strong>hibited.<br />
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