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

28.01.2015 Views

EPRI Proprietary Licensed Material pumps turned off. This mode eliminates pumping losses and self discharge during downtime. When the battery is called into service, a minute or two would be required to start the pumps and transport electrolyte to the stacks. Environmental impact The VRB stacks, plumbing, and tanks, are primarily composed of recyclable plastic materials, and the electrolyte can be refurbished and reused. There are no toxic chemicals that must be disposed of at the end of life, such as found in other electrochemical storage technologies. For this reason, the VRB is promoted as a “green” storage technology. The only chemical in the VRB system is the vanadium electrolyte, ionic vanadium in sulfuric acid at approximately the same concentration found in flooded lead-acid batteries. Its handling and safety requirements are the same as sulfuric acid. The electrolyte is internally contained within industrial-grade HDPE tanks and pressure-rated PVC pipe and fittings. The VRB is placed within a spill containment area compliant with local regulations. As with all storage technologies, every charge/discharge cycle results in some loss of energy due to system inefficiencies. For typical grid-connected applications, this means that from a global perspective, there may be increased air emissions associated with the generation of this lost energy. Of course, for renewable energy applications, there are no air emissions considerations, and in some applications, the VRB serves to increase the utilization of renewable sources. DC Electrical Characteristics In most VRB systems, the DC bus is connected to the cell stack terminals. The DC voltage is determined by the cell count, and is typically 100 V or more. When power requirements exceed the current ratings of a single stack, multiple stacks are connected in parallel. However, other configurations are possible. Stacks can be placed in series to boost DC voltage, but this requires separate electrolyte hydraulic plumbing and storage to minimize ion flow losses (“shunt currents”) that increase with voltage. Cellenium is developing an unconventional power conversion technology in which individual cells are tapped and switched, providing near-sinusoidal outputs with incremental voltage steps equal to the cell voltage. Vanadium Redox Battery 12

EPRI Proprietary Licensed Material Figure 4 Typical flow configuration (Courtesy Telepower Australia) It is likely that future VRB systems will be manufactured in several standard AC configurations to eliminate project-specific engineering costs. Today’s systems, however, include custom-specified PCSs and project specific DC designs. As the battery is charged and discharged, the DC bus varies in voltage. The open circuit voltage varies with the battery state-of-charge, and charging or discharging produces a corresponding increase or decrease in bus voltage. The PCS must be designed to handle the full voltage “window”. At the Stellenbosch demonstration, for example, the DC bus voltage ranged from 650 to 850 VDC (1.08 to 1.42 volts per cell). Since the battery is occasionally fully discharged to 0 VDC (for maintenance and transport), a mechanism such as switched DC resistive loads must be provided to accommodate voltages below the operating range of the PCS. As charged electrolyte is stored in separate anolyte and catholyte tanks, no self-discharge occurs during extended periods of downtime. This would be advantageous in applications such as spinning reserve that require availability of stored energy, but do not require instantaneous power on demand. Under these conditions, the pumps would be powered down, causing the stacks to drain back into the tanks, and the battery would retain its full charge without incurring ongoing parasitic pump losses. It could be restored to full power in a matter of minutes by restarting the pumps and flooding the stacks. While it would be possible to design the hydraulic system to retain active electrolyte in the stacks when the pumps were off, the battery would self-discharge over a period of hours, depending upon the stack (and associated manifold) volume, the number of cells (stack voltage), and the concentration of electrolyte. Furthermore, the energy storage capacity would be negligible. Vanadium Redox Battery 13

EPRI Proprietary Licensed Material<br />

pumps turned <strong>of</strong>f. This mode eliminates pumping losses and self discharge during<br />

downtime. When the battery is called into service, a minute <strong>or</strong> two would be required to<br />

start the pumps and transp<strong>or</strong>t electrolyte to the stacks.<br />

Environmental impact<br />

The VRB stacks, plumbing, and tanks, are primarily <strong>com</strong>posed <strong>of</strong> recyclable plastic<br />

materials, and the electrolyte can be refurbished and reused. There are no toxic<br />

chemicals that must be disposed <strong>of</strong> at the end <strong>of</strong> life, such as found in other<br />

electrochemical st<strong>or</strong>age technologies. F<strong>or</strong> this reason, the VRB is promoted as a “green”<br />

st<strong>or</strong>age technology.<br />

The only chemical in the VRB system is the vanadium electrolyte, ionic vanadium in<br />

sulfuric acid at approximately the same concentration found in flooded lead-acid<br />

batteries. Its handling and safety requirements are the same as sulfuric acid. The<br />

electrolyte is internally contained within industrial-grade HDPE tanks and pressure-rated<br />

PVC pipe and fittings. The VRB is placed within a spill containment area <strong>com</strong>pliant with<br />

local regulations.<br />

As with all st<strong>or</strong>age technologies, every charge/discharge cycle results in some loss <strong>of</strong><br />

energy due to system inefficiencies. F<strong>or</strong> typical grid-connected applications, this means<br />

that from a global perspective, there may be increased air emissions associated with the<br />

generation <strong>of</strong> this lost energy. Of course, <strong>f<strong>or</strong></strong> renewable energy applications, there are no<br />

air emissions considerations, and in some applications, the VRB serves to increase the<br />

utilization <strong>of</strong> renewable sources.<br />

DC Electrical Characteristics<br />

In most VRB systems, the DC bus is connected to the cell stack terminals. The DC<br />

voltage is determined by the cell count, and is typically 100 V <strong>or</strong> m<strong>or</strong>e. When power<br />

requirements exceed the current ratings <strong>of</strong> a single stack, multiple stacks are connected in<br />

parallel. However, other configurations are possible. Stacks can be placed in series to<br />

boost DC voltage, but this requires separate electrolyte hydraulic plumbing and st<strong>or</strong>age to<br />

minimize ion flow losses (“shunt currents”) that increase with voltage. Cellenium is<br />

developing an unconventional power conversion technology in which individual cells are<br />

tapped and switched, providing near-sinusoidal outputs with incremental voltage steps<br />

equal to the cell voltage.<br />

Vanadium Redox Battery 12

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