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A Feasibility Study - Aaltodoc - Aalto-yliopisto

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Cost of water (€/m³)<br />

5<br />

4,5<br />

4<br />

3,5<br />

3<br />

2,5<br />

2<br />

1,5<br />

1<br />

0,5<br />

0<br />

Figure 45. Cost of water (€/m³) on Site 2.<br />

At the nominal pump capacity of 0,03 m³/s, there are 8 pressure vessels and 56 RO<br />

membranes, with a nominal output of 1400 m³/day. The cost breakdown of Site 2 at a<br />

nominal pump capacity of 0,03 m³/s is presented in Table 7.<br />

9.6 Site 3<br />

Cost of Water (€/m3)<br />

Load factor (%)<br />

0<br />

0 0,05 0,1 0,15 0,2 0,25 0,3<br />

WaveRoller nominal pump capacity (m³/s)<br />

Table 7. Cost breakdown of Site 2 with a nominal pump capacity of 0,03 m³/s.<br />

Capital expenses (€) Operational expenses (€)<br />

WEC 1 800 000 90 000<br />

RO 450 000 30 000<br />

Total 2 250 000 120 000<br />

Annual 210 000 120 000<br />

Site 3 has a good wave climate, with an average wave power of 16 kW/m. The<br />

performance and retention curves of Site 3 have been given in the Appendix B. The<br />

calculation presented in this Chapter follows the calculation method described in<br />

Chapter 9.1. The average recovery rate in all the calculations on Site 3 has been 28,5 %<br />

and the average permeate TDS is 134 mg/l, which is well below the limit of 500 mg/l.<br />

The permeate production on Site 3 is basically constantly increasing. The permeate<br />

production is highest at 1685 m³/day at the end of the study range with a nominal pump<br />

capacity of 0,24 m³/s, with a load factor of 0,76. The fact that the permeate production<br />

increases even though the load factor constantly decreases signifies that the wave power<br />

resource on Site 3 is of a suitable type for the <strong>Aalto</strong>RO process. Still the peak<br />

production is less than in Site 1 (1996 m³/day). The permeate production of Site 3 is<br />

presented in Figure 46.<br />

63<br />

1,2<br />

1<br />

0,8<br />

0,6<br />

0,4<br />

0,2<br />

Load factor

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