A Feasibility Study - Aaltodoc - Aalto-yliopisto
A Feasibility Study - Aaltodoc - Aalto-yliopisto
A Feasibility Study - Aaltodoc - Aalto-yliopisto
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flow rates. However they generally have high capital costs. The situation is more or less<br />
reversed with centrifugal devices.<br />
Based on Table 5 alone, the choice of an appropriate ERD for <strong>Aalto</strong>RO would be very<br />
difficult, since weighing the advantages and disadvantages of positive displacement<br />
devices and centrifugal devices is hard. Therefore, the selection process is simplified by<br />
excluding those ERDs that are designed for electricity production, since it is not a target<br />
in <strong>Aalto</strong>RO. To clarify the differences between the two ERD types, one example of each<br />
is chosen: the hydraulic turbocharger for centrifugal devices and the Clark pump for<br />
positive displacement devices.<br />
The basic configuration of the Clark pump is that it pressurizes a portion of the feed<br />
water while the high-pressure pump pressurizes the remaining part of the feed water.<br />
Figure 32 presents the basic configuration of the Clark pump. Basically this means that<br />
the high-pressure pump can be of smaller size but that it has to be able to pressurize up<br />
to the desired pressure level. On the other hand, the hydraulic turbocharger operates by<br />
increasing the pressure of the entire volume flow rate of the feed water. Thus, the highpressure<br />
pump needs to be able to handle the entire volume flow rate but it does not<br />
need to be able to pressurize to the desired pressure level (Jatzlau 2011).<br />
Figure 32. Basic configuration of a Clark pump. Adapted from (Jatzlau 2011).<br />
The operating principle of <strong>Aalto</strong>RO agrees well with the hydraulic turbocharger, but not<br />
with the Clark pump. This is mainly due to the fact that the “high-pressure pump” of<br />
<strong>Aalto</strong>RO is the WEC at the bottom of the sea, while the ERD will be situated onshore.<br />
If the Clark pump would be chosen, it would require another standard high-pressure<br />
pump for the entire system to operate. This would increase the capital costs and also<br />
complicate the system without sufficient increases in production.<br />
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