Handbook of Energy Storage for Transmission or ... - W2agz.com
Handbook of Energy Storage for Transmission or ... - W2agz.com
Handbook of Energy Storage for Transmission or ... - W2agz.com
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EPRI Proprietary Licensed Material<br />
plumbing, structural elements, power electronics, and controls would have longer useful<br />
lifetimes. It is possible to replace only the stacks, and keep the remainder <strong>of</strong> the system<br />
in place.<br />
Efficiency<br />
Several losses must be accounted <strong>f<strong>or</strong></strong> in characterizing the VRB per<strong>f<strong>or</strong></strong>mance:<br />
• Trans<strong>f<strong>or</strong></strong>mer losses. Most utility scale and industrial PCSs are designed with<br />
outputs around 480 VAC. To connect to utility distribution voltages, a<br />
trans<strong>f<strong>or</strong></strong>mer must be installed resulting in losses <strong>of</strong> a few percent. Even <strong>f<strong>or</strong></strong> nonutility<br />
systems, isolation trans<strong>f<strong>or</strong></strong>mers are installed to prevent DC injection into<br />
the AC grid.<br />
• PCS losses. Whether charging <strong>or</strong> discharging, power flow through the PCS is<br />
subject to losses related to voltage drops across the switching devices. PCS<br />
throughput efficiency depends somewhat on load and PCS design, but is typically<br />
in the 92-96% range.<br />
• Battery DC losses. The energy to charge the battery is typically 20% greater<br />
than the energy delivered during discharge. Internal battery losses include voltaic<br />
losses such as ionic flow resistance and coulombic losses such as cell-to-cell shunt<br />
currents (stray ionic flow through the stack manifold). Actual DC losses depend<br />
on rate <strong>of</strong> charge and discharge (the system is slightly m<strong>or</strong>e efficient at lower<br />
rates).<br />
• Pumping losses. Pumping power is a relatively constant auxiliary load that is<br />
drawn whenever electrolyte must be supplied to the stacks, i.e., during charge and<br />
discharge. In some applications such as backup power, it is possible to charge the<br />
battery, then turn the pumps <strong>of</strong>f <strong>f<strong>or</strong></strong> long periods <strong>of</strong> time. The actual efficiency<br />
penalty <strong>f<strong>or</strong></strong> pumping depends upon the operation <strong>of</strong> the pumping, the frequency <strong>of</strong><br />
cycling, and the pump design. At the 250 kW Stellenbosch demonstration in<br />
South Africa (see below), four pumps each drew 2.2 kW (8.8 kW total).<br />
The “round trip” (“turnaround”) efficiency – including trans<strong>f<strong>or</strong></strong>mer losses during charge,<br />
PCS losses during charge, battery DC losses, PCS losses during discharge, trans<strong>f<strong>or</strong></strong>mer<br />
losses during discharge, and pumping losses – is on the <strong>or</strong>der <strong>of</strong> 70%.<br />
Response Time<br />
The battery can is capable <strong>of</strong> transitioning from zero output to full output in<br />
microseconds – virtually instantaneously – provided the stacks are primed with reactants.<br />
However, the power electronics respond within milliseconds, and the response time <strong>of</strong> the<br />
controls and <strong>com</strong>munications (sensing the load requirements and signaling the PCS to<br />
take action) can be even longer.<br />
Where response time is imp<strong>or</strong>tant, the control system must be programmed to keep the<br />
pumps on and electrolyte flowing through the stacks. This requirement imposes a small<br />
per<strong>f<strong>or</strong></strong>mance penalty due to the constant auxiliary losses <strong>of</strong> the pumps. If response time<br />
is not critical, such as in peak shaving applications, then the stacks can be drained and the<br />
Vanadium Redox Battery 11