TRL Energy Storage System Features
TRL CIR
Salient performance features
|
Capital
Equipment Cost |
< $5/KWh and ~ $200/kW in production |
|
Cycle
Life |
greater
than 100,000 cycles |
|
Materials |
no
rare, hazardous or scarce materials |
|
Configuration |
full-flow
electrolyte, or static and sealed |
|
Operating
|
10 to
180 deg F |
|
Maintenance |
essentially
none required |
|
Energy
Density |
10 to 22
Wh/lb, 1 to 1.4 kWh/ft3 |
|
|
2 to 5 kW/ft3 |
|
Energy
Efficiency |
85% to
90% |
|
Charge
Retention |
indefinitely
long for full-flow version in off mode |
Additional
Advantages
Completely
reversible operation
No memory or
fatigue problems
Can be left
unattended indefinitely
Virtually no
operational failure modes
Among
the many application possibilities for the ESD system, the following are listed.
For Full Flow
Configuration
Wind energy storage
Solar
photo-voltaic
Emergency
standby power source
UPS
systems
Load
leveling
For Static
Electrolyte, Sealed
Small portable appliances & communication systems
On-line
for computers and controls
User end
storage for power peaking on demand
Hybrid vehicle peak electric power and propulsion
Full Flow and
Static Electrolyte System Comparisons
Redox cells with two electrolytes and all liquid reagents can be designed
and operated as either static electrolyte systems or full flow electrolytes. In
the first case the electrolytes remain in their respective compartments
(negative and positive sides of a cell with a barrier or membrane separating
the two compartments) as in conventional batteries.
The static electrolyte version of the redox cell offers the advantages of
simplicity in design, no mechanically moving parts, and easily sealed. However,
the energy and power densities of any particular cell design is a compromise
because inter electrode cell spacing will affect both coulombic capacity as
well as internal cell resistance and reagent availability for discharge. Also,
charge retention time is significantly smaller because of ionic and molecular
diffusion across the membrane separator.
In the full flow configuration the two electrolytes are circulated from
reservoirs into and out of their respective cell compartments through
appropriate manifolds and pumps as shown in the figure below.
The advantages of the flowing electrolyte design approach include;
In some applications the advantages of full flow redox may justify the
necessary additional complexity and mechanisms.
In striving for the realization of a very long life secondary battery one
of the developmental paths that has been followed is the use of reagents that
remain in solution at all times. In other words, no deposition or removal or
change of composition or structure of solid reagents at electrode surfaces in
the energy storing process. There are very few choices of chemical components
that have all the properties necessary to make it a practical electrochemical
process. Virtually all workable
materials combinations have the singular drawback of having dissimilar
materials on opposite electrolytes. And, since these reagents are in solution
there is the inexorable transport of catholyte materials into the anolyte
region and vice versa. In most cases there is no direct method of returning
these unwanted components from one electrolyte to their origin.
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