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corrosive species and scaling in wells at olkaria ... - Orkustofnun

corrosive species and scaling in wells at olkaria ... - Orkustofnun

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LogHCl <strong>in</strong> vapour (ppm)<br />

100<br />

10<br />

1<br />

0.1<br />

0.01<br />

0.001<br />

0.0001<br />

1E-005<br />

1E-006<br />

1E-007<br />

1E-008<br />

1E-009<br />

1E-010<br />

OW-901 Olkaria Domes<br />

OW-301 Olkaria West<br />

OW-306 Olkaria West<br />

OW-20 Olkaria East<br />

OW-30 Olkaria East<br />

OW-714 Olkaria North East<br />

OW-34 Olkaria East<br />

OW-709 Olkaria North East<br />

SV-05 Svartsengi<br />

SV-11 Svartsengi<br />

RN-10 Reykjanes<br />

RN-11 Reykjanes<br />

NJ-14 Nesjavellir<br />

NJ-22 Nesjavellir<br />

5 6 7 8 9 10<br />

pH<br />

FIGURE 22: HCl <strong>in</strong> vapour with changes <strong>in</strong> pH<br />

upon several steps of s<strong>in</strong>gle-step adiab<strong>at</strong>ic<br />

boil<strong>in</strong>g of selected <strong>wells</strong> <strong>in</strong> the study areas.<br />

The boil<strong>in</strong>g is from the respective aquifer<br />

temper<strong>at</strong>ure (See Table 4 <strong>in</strong> Appendix A)<br />

well fluids than the well fluids <strong>in</strong> Olkaria <strong>and</strong><br />

Nesjavellir. At Svartsengi they are ~ 10 2 -10 4<br />

times higher than <strong>in</strong> the Olkaria <strong>and</strong> Nesjavellir<br />

w<strong>at</strong>ers.<br />

Changes <strong>in</strong> pH are affected by the concentr<strong>at</strong>ions<br />

of carbon dioxide <strong>in</strong> the <strong>in</strong>itial aquifer w<strong>at</strong>er <strong>and</strong><br />

<strong>in</strong> the Olkaria well w<strong>at</strong>ers, the CO 2<br />

concentr<strong>at</strong>ions are variable. The Olkaria well<br />

w<strong>at</strong>ers have a rel<strong>at</strong>ively high <strong>in</strong>itial pH <strong>in</strong> the<br />

aquifer except for <strong>wells</strong> th<strong>at</strong> are <strong>in</strong> the Olkaria<br />

West sector. Upon boil<strong>in</strong>g by steam loss with<br />

decrease <strong>in</strong> temper<strong>at</strong>ure, the <strong>in</strong>crease <strong>in</strong> pH is<br />

much gre<strong>at</strong>er for <strong>wells</strong> with a high <strong>in</strong>itial<br />

concentr<strong>at</strong>ion of CO 2 <strong>in</strong> the w<strong>at</strong>er <strong>in</strong> Olkaria.<br />

Figure 22 shows decrease <strong>in</strong> the HCl<br />

concentr<strong>at</strong>ions with <strong>in</strong>crease <strong>in</strong> pH upon<br />

adiab<strong>at</strong>ic boil<strong>in</strong>g.<br />

The large <strong>in</strong>crease <strong>in</strong> pH <strong>in</strong> the Olkaria well<br />

w<strong>at</strong>ers with decrease <strong>in</strong> temper<strong>at</strong>ure, contributes<br />

to the low concentr<strong>at</strong>ions of HCl <strong>in</strong> the steam<br />

when the w<strong>at</strong>er boils. The Reykjanes, Svartsengi<br />

<strong>and</strong> Nesjavellir aquifer w<strong>at</strong>ers vary less <strong>in</strong> CO 2<br />

gas concentr<strong>at</strong>ion than the w<strong>at</strong>ers of the Olkaria. The pH of aquifer w<strong>at</strong>er <strong>in</strong> Reykjanes <strong>and</strong> Svartsengi<br />

are similar while <strong>at</strong> Nesjavellir the aquifer pH is higher. The rel<strong>at</strong>ive <strong>in</strong>crease <strong>in</strong> pH with decrease <strong>in</strong><br />

temper<strong>at</strong>ure is gradual <strong>in</strong> Reykjanes, Svartsengi <strong>and</strong> Nesjavellir <strong>wells</strong> upon steam loss. The trends for<br />

decrease <strong>in</strong> HCl concentr<strong>at</strong>ions, when HCl partitions <strong>in</strong>to steam, are similar to those of Olkaria aquifer<br />

fluids. As the w<strong>at</strong>ers cool by steam loss, HCl tends to be reta<strong>in</strong>ed more <strong>in</strong> the liquid <strong>and</strong> less partitions<br />

the steam.<br />

The concentr<strong>at</strong>ions of HCl <strong>in</strong> steam collected <strong>at</strong> the wellheads of selected Olkaria, Reykjanes,<br />

Svartsengi <strong>and</strong> Nesjavellir <strong>wells</strong> are shown <strong>in</strong> Table 5 of Appendix A. HCl concentr<strong>at</strong>ions <strong>in</strong> Olkaria<br />

<strong>and</strong> Nesjavellir are very low 3×10 -8 - 3×10 -6 ppm <strong>and</strong> 5×10 -6 - 1×10 -5 ppm, respectively. At Svartsengi<br />

<strong>and</strong> Reykjanes these are 6×10 -4 -1.5×10 -3 ppm <strong>and</strong> 2×10 -1 -7×10 -1 ppm, respectively. The concentr<strong>at</strong>ions<br />

of HCl <strong>in</strong> the separ<strong>at</strong>ed steam conveyed to the power plant <strong>at</strong> Olkaria are very low, 10 -8 -10 -6 ppm. At<br />

Svartsengi they are about 5×10 -5 - 10 -4 ppm but as high as 0.1 ppm <strong>at</strong> Reykjanes. The high values <strong>at</strong><br />

Reykjanes are due to the high Cl content of the aquifer w<strong>at</strong>er <strong>and</strong>, <strong>in</strong> particular the high pressures <strong>in</strong><br />

the steam separ<strong>at</strong>ors. All these concentr<strong>at</strong>ions are considerable lower than measured Cl concentr<strong>at</strong>ions<br />

<strong>in</strong> the steam of many vapour-dom<strong>in</strong><strong>at</strong>ed geothermal systems e.g. <strong>in</strong> dry steam from well KG-12 <strong>at</strong><br />

Krafla, Icel<strong>and</strong> (Truesdell, 1991). Yet, corrosion <strong>at</strong> Reykjanes due to condens<strong>at</strong>ion of high pressure<br />

steam may be a problem. Condens<strong>at</strong>ion need not occur dur<strong>in</strong>g conductive he<strong>at</strong> loss. At temper<strong>at</strong>ures<br />

higher than th<strong>at</strong> correspond<strong>in</strong>g to maximum steam enthalpy, condens<strong>at</strong>ion will occur by pressure drop<br />

to the maximum enthalpy value. If the discharge is almost dry steam <strong>corrosive</strong> liquid w<strong>at</strong>er could be<br />

produced <strong>in</strong> this way. At Reykjanes corrosion <strong>in</strong> pipel<strong>in</strong>es due to production of HCl may not occur<br />

due to form<strong>at</strong>ion of stable sulphide scales <strong>and</strong> the HCl could be scrubbed. The quantity of this scale is<br />

limited except from sal<strong>in</strong>e w<strong>at</strong>ers. Stable sulphide scale form<strong>at</strong>ion <strong>at</strong> Reykjanes has been reported by<br />

Hardardóttir et al. (2001, 2004). In steam pipel<strong>in</strong>es made of carbon steel, th<strong>in</strong> co<strong>at</strong><strong>in</strong>gs of stable<br />

sulphide, carbon<strong>at</strong>es, silic<strong>at</strong>es or metastable sulphide phases are known to form a protective co<strong>at</strong><strong>in</strong>g<br />

th<strong>at</strong> tends to prevent corrosion of cas<strong>in</strong>g <strong>and</strong> other m<strong>at</strong>erial th<strong>at</strong> would otherwise be a problem due to<br />

CO 2 <strong>and</strong> HCl. Other scales th<strong>at</strong> form protective co<strong>at</strong><strong>in</strong>g are carbon<strong>at</strong>es. At sufficiently low pH <strong>in</strong><br />

condens<strong>at</strong>es conta<strong>in</strong><strong>in</strong>g HCl, phases of protective sulphides <strong>and</strong> carbon<strong>at</strong>es can become unstable <strong>and</strong><br />

dissolve <strong>and</strong> corrosion can be <strong>in</strong>duced.<br />

26

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