SEPARATOR LAYER FOR FLOW BATTERY
BACKGROUND
Flow batteries, also known as redox flow batteries or redox flow cells, are
designed to convert electrical energy into chemical 5 energy that can be stored and
later released when there is demand. As an example, a flow battery may be used with
a renewable energy system, such as a wind-powered system, to store energy that
exceeds consumer demand and later release that energy when there is greater
demand.
10 A typical flow battery includes a redox flow cell that has a negative electrode
and a positive electrode separated by an ion-exchange membrane. A negative fluid
electrolyte (sometimes referred to as the anolyte) is delivered to the negative
electrode and a positive fluid electrolyte (sometimes referred to as the catholyte) is
delivered to the positive electrode to drive electrochemically reversible redox
15 reactions. Upon charging, the electrical energy supplied causes a chemical reduction
reaction in one electrolyte and an oxidation reaction in the other electrolyte. The
separator prevents the electrolytes from freely and rapidly mixing but permits
selected ions to pass through to complete the redox reactions. Upon discharge, the
chemical energy contained in the liquid electrolytes is released in the reverse
20 reactions and electrical energy can be drawn from the electrodes. Flow batteries are
distinguished from other electrochemical devices by, inter alia, the use of externallysupplied,
fluid electrolyte solutions that include reactants that participate in reversible
electrochemical reactions.
25 SUMMARY
A flow battery according to an example of the present disclosure includes an
electrochemical cell that has a first electrode, a second electrode spaced apart from
the first electrode, and a separator layer arranged between the first electrode and the
second electrode. The separator layer is formed of a polymer having a polymer
30 backbone with aromatic groups that are free of unsaturated nitrogen and one or more
polar groups bonded in the polymer backbone.
In a further embodiment of any of the foregoing embodiments, the one or
more polar groups includes an atom selected from the group consisting of sulfur,
oxygen, nitrogen, and combinations thereof.
3
In a further embodiment of any of the foregoing embodiments, the aromatic
groups include nitrogen heterocycles.
In a further embodiment of any of the foregoing embodiments, the polymer
backbone is free of unsaturated nitrogen.
In a further embodiment of any 5 of the foregoing embodiments, the polymer
includes at least one of adsorbed acid groups or aqueous electrolyte that is noncovalently
bonded to the one or more polar groups.
In a further embodiment of any of the foregoing embodiments, the polymer
includes polyetherimide (PEI).
10 In a further embodiment of any of the foregoing embodiments, the polymer
includes polyamide-imide (PAI).
In a further embodiment of any of the foregoing embodiments, the polymer
includes polyetheretherketone (PEEK).
In a further embodiment of any of the foregoing embodiments, the polymer
15 includes polysulfone (PSF).
In a further embodiment of any of the foregoing embodiments, the polymer
includes polyphenylene sulfide (PPS).
In a further embodiment of any of the foregoing embodiments, the polymer is
selected from the group consisting of polyetherimide (PEI), polyamide-imide (PAI),
20 polyetheretherketone (PEEK), polysulfone (PSF), polyphenylene sulfide (PPS), and
combinations thereof.
A further embodiment of any of the foregoing embodiments includes a
supply/storage system external of the electrochemical cell. The supply/storage
system includes first and second vessels, first and second liquid electrolytes in,
25 respectively, the first and second vessels, fluid lines connecting the first and second
vessels to, respectively, the first electrode and the second electrode, and a plurality of
pumps operable to circulate the first and second liquid electrolytes via the fluid lines
between the first and second vessels and the electrochemical cell.
In a further embodiment of any of the foregoing embodiments, the separator
30 layer has an area specific resistance of less than approximately 425 mΩ*cm2.
A separator layer for use in a flow battery, the separator layer being formed of
a polymer having a polymer backbone with aromatic groups that are free of
unsaturated nitrogen, wherein the separator layer has an area specific resistance of
less than approximately 425 mΩ*cm2.
4
In a further embodiment of any of the foregoing embodiments, the separator
layer has an area specific resistance of less than approximately 300 mΩ*cm2.
In a further embodiment of any of the foregoing embodiments, the polymer is
selected from the group consisting of polyetherimide (PEI), polyamide-imide (PAI),
polyetheretherketone (PEEK), polysulfone 5 (PSF), polyphenylene sulfide (PPS),
polystyrene (PS) and combinations thereof.
A flow battery according to an example of the present disclosure includes an
electrochemical cell that has a first electrode, a second electrode spaced apart from
the first electrode, and a separator layer arranged between the first electrode and the
10 second electrode. The first electrode and the second electrode are configured to
operate at a current density of greater than or equal to approximately 100 mA/cm2
and a supply/storage system external of the electrochemical cell. The supply/storage
system includes first and second vessels, first and second liquid electrolytes in,
respectively, the first and second vessels, fluid lines connecting the first and second
15 vessels to, respectively, the first electrode and the second electrode, and a plurality of
pumps operable to circulate the first and second liquid electrolytes via the fluid lines
between the first and second vessels and the electrochemical cell. The separator
layer is formed of a polymer having a polymer backbone with aromatic groups that
are free of unsaturated nitrogen and one or more polar groups bonded in the polymer
20 backbone.
A flow battery according to an example of the present disclosure includes an
electrochemical cell that has a first electrode, a second electrode spaced apart from
the first electrode, and a separator layer arranged between the first electrode and the
second electrode. The separator layer is formed of a polymer having a polymer
25 backbone with triazine groups.
In a further embodiment of any of the foregoing embodiments, the polymer
backbone includes one or more polar groups bonded in the polymer backbone
In a further embodiment of any of the foregoing embodiments, the one or
more polar groups includes an atom selected from the group consisting of sulfur,
30 oxygen, nitrogen, and combinations thereof.
5
BRIEF DESCRIPTION OF THE DRAWINGS
The various features and advantages of the present disclosure will become
apparent to those skilled in the art from the following detailed description. The
drawings that accompany the detailed description can be briefly described as follows.
Figure 5 1 illustrates an example flow battery.
DETAILED DESCRIPTION
Figure 1 schematically shows portions of an example flow battery 20 for
selectively storing and discharging electrical energy. As an example, the flow battery
10 20 can be used to convert electrical energy generated in a renewable energy system to
chemical energy that is stored until a later time when there is greater demand, at
which time the flow battery 20 then converts the chemical energy back into electrical
energy. The flow battery 20 can supply the electric energy to an electric grid, for
example.
15 The flow battery 20 includes a fluid electrolyte 22 that has an
electrochemically active species 24 that functions in a redox pair with regard to an
additional fluid electrolyte 26 that has an electrochemically active species 28. The
electrochemically active species 24/28 include ions of elements that have multiple,
reversible oxidation states in a selected liquid solution, such as but not limited to,
20 aqueous solutions or dilute aqueous acids, such as 1-5M sulfuric acid. In some
examples, the multiple oxidation states are non-zero oxidation states, such as for
transition metals including but not limited to vanadium, iron, manganese, chromium,
zinc, molybdenum and combinations thereof, and other elements including but not
limited to sulfur, cerium, lead, tin, titanium, germanium and combinations thereof. In
25 some examples, the multiple oxidation states can include the zero oxidation state if
the element is readily soluble in the selected liquid solution in the zero oxidation
state. Such elements can include the halogens, such as bromine, chlorine, and
combinations thereof. The electrochemically active species 24/28 could also be
organic molecules that contain groups that undergo electrochemically reversible
30 reactions, such as quinones.
The first fluid electrolyte 22 (e.g., the negative electrolyte) and the second
fluid electrolyte 26 (e.g., the positive electrolyte) are contained in a supply/storage
system 30 that includes first and second vessels 32/34 and pumps 35. The fluid
electrolytes 22/26 are delivered using the pumps 35 to at least one electrochemical
6
cell 36 of the flow battery 20 through respective feed lines 38 and are returned from
the cell 36 to the vessels 32/34 via return lines 40. The feed lines 38 and the return
lines 40 connect the vessels 32/34 with first and second electrodes 42/44. Multiple
cells 36 can be provided as a stack.
The cell 36 includes the first electrode 5 42, the second electrode 44 spaced
apart from the first electrode 42, and a separator layer 46 arranged between the first
electrode 42 and the second electrode 44. For example, the electrodes 42/44 are
porous carbon structures, such as carbon paper or felt. The electrodes 42/44 may
each be configured for operation at relatively high current densities, such as but not
limited to, current density greater than or equal to approximately 100 mA/cm210 .
In general, the cell or cells 36 can include bipolar plates, manifolds and the
like for delivering the fluid electrolytes 22/26 through flow field channels to the
electrodes 42/44. The bipolar plates can be carbon plates, for example. It is to be
understood however, that other configurations can be used. For example, the cell or
15 cells 36 can alternatively be configured for flow-through operation where the fluid
electrolytes 22/26 are pumped directly into the electrodes 42/44 without the use of
flow field channels.
The fluid electrolytes 22/26 are delivered to the cell 36 to either convert
electrical energy into chemical energy or, in the reverse reaction, convert chemical
20 energy into electrical energy that can be discharged. The electrical energy is
transmitted to and from the cell 36 through an electric circuit 48 that is electrically
coupled with the electrodes 42/44.
The separator layer 46 prevents the fluid electrolytes 22/26 from freely and
rapidly mixing but permits selected ions to pass through to complete the redox
25 reactions while electrically isolating the electrodes 42/44. In this regard, the fluid
electrolytes 22/26 are generally isolated from each other during normal operation,
such as in charge, discharge and shutdown states.
In particular, due to the highly oxidative and acidic environment in flow
batteries in comparison to gaseous fuel cells, there are only a few materials (e.g.,
30 perfluorosulfonic acid) that are useful as a separator layer or ion exchange
membrane. Materials that may be effective in the less severe environment of a
gaseous fuel cell are degraded by the oxidative and acidic environment in flow
batteries and suffer from inadequate ion conductivity (e.g., proton conductivity)
and/or ion selectivity (e.g., blocking permeation of vanadium or other
7
electrochemically active ion species that can reduce energy efficiency). In this
regard, as discussed further below, the disclosed separator layer 46 is formed of a
polymer that may be stable in the oxidative and acidic environment in the flow
battery 20 and that may have good ion conductivity and ion selectivity, among other
5 properties.
In addition to ion conductivity and ion selectivity, the separator layer 46 has
properties such as ionic resistance, area specific resistance, and electric conductivity
and resistivity. The ionic resistance is measured, in ohms (Ω), between the opposed
surfaces of the separator layer 46. The ionic resistance is a function of the thickness
10 of the separator layer 46, the cross-sectional area, and the bulk resistivity. The (ionic)
area specific resistance is a function of the ionic resistance and cross-sectional area.
The area specific resistance can be calculated, in units of amperes per area squared,
by the equation RAS = R*A, where RAS is the area specific resistance, R is ionic
resistance, and A is cross-sectional area.
15 As an example, the separator layer 46 is formed of a polymer that has a
polymer backbone with aromatic groups that are free of (i.e., exclude) unsaturated
nitrogen and that has one or more polar groups that are bonded within the polymer
backbone. Such polar groups may be located between the cyclic groups, but are not
limited to such locations. The aromatic groups may provide the separator layer 46
20 with good chemical stability in the oxidative and acidic environment of the flow
battery 20, while the polar groups may provide permanent dipoles that are noncovalently
bonded to adsorbed acid groups and/or aqueous electrolyte that serve to
facilitate ion conductivity. As examples, the one or more polar groups can include,
but are not limited to, groups that have one or more high electronegative atoms
25 selected from sulfur, oxygen, nitrogen, and combinations thereof. In further
examples, the polar groups include one or more of the chemical structures: C O C,
C=O, N C=O, S=O, S=O=S, or C S.
In further examples, the aromatic groups of the polymer backbone include
six-carbon atom rings and/or aromatic groups with nitrogen heterocycles. Since the
30 aromatic groups are free of unsaturated nitrogen, the nitrogen heterocycles are also
free of unsaturated nitrogen. Although not limited, such nitrogen heterocycles may
include a five-atom ring that has one nitrogen atom and four carbon atoms. As will
be appreciated, other aromatic groups and aromatic groups with nitrogen
heterocycles according to Hückel's rule may additionally or alternatively be used.
8
Furthermore, the flow battery 20 generally operates at much lower
temperatures (e.g., less than 100°C, but typically less 50°C) than some types of fuel
cells (e.g., greater than 200°C). Thus, the selected polymer need not have the high
temperature stability that is required in fuel cell membranes. For instance, the glass
transition temperature of the selected polymer need only 5 be greater than the expected
operating temperature of the flow battery 20 (greater than 50°C or 100°C).
In further examples, the polymer of the separator layer 46 is selected from
polyetherimide (PEI), polyamide-imide (PAI), polyetheretherketone (PEEK),
polysulfone (PSF), polyphenylene sulfide (PPS), or combinations thereof. It is to be
10 understood that the example polymers herein include the molecular formula of the
polymer and any isomers based upon the formula. Additionally, a combination could
be in the form of blends, alloys, and co-, ter-, quatrenary- (etc.) polymers, where at
least a portion of the component is of the polymers listed subsequently. Shown
below are example structures of the polymer of the separator layer 46, with adsorbed
15 acid groups or aqueous electrolyte, represented at “A,” that are non-covalently
bonded to the one or more of the polar groups:
Polyetherimide:
Polyamide-imide:
20
Polyetheretherketone:
Polysulfone:
A
A
A
A
9
Polyphenylene sulfide:
.
In another example, the separator layer 46 is formed of a polymer that has a
polymer backbone with triazine groups. A triazine group is a nitrogen heterocycle
that includes three nitrogen atoms in an aromatic 5 ring. In further examples, the
polymer backbone may also include one or more polar groups as discussed herein
above that are bonded within the polymer backbone. The triazine groups may provide
the separator layer 46 with good chemical stability in the oxidative and acidic
environment of the flow battery 20, while the polar groups may provide permanent
10 dipoles that are non-covalently bonded to adsorbed acid groups and/or aqueous
electrolyte that serve to facilitate ion conductivity.
In further examples, the separator layer 46 has a thickness of less than
approximately 125 micrometers or less than 100 micrometers, based on the flow
battery 20 operating at an average current density above approximately 100 mA/cm2
(e.g., greater than 200 mA/cm215 ). In a further example, the area specific resistance is
less than approximately 425 mΩ*cm2, based on the flow battery 20 operating at an
average current density above approximately 100 mA/cm2 (e.g., greater than 200
mA/cm2). In further examples, the separator layer 46 has an area specific resistance
of less than approximately 425 mΩ*cm2 and the polymer of the separator layer 46 is
20 selected from polyetherimide (PEI), polyamide-imide (PAI), polyetheretherketone
(PEEK), polysulfone (PSF), polyphenylene sulfide (PPS), polystyrene, or
combinations thereof.
In a further example, the area specific resistance of the separator layer 46 is
less than approximately 300 mΩ*cm2, based on the flow battery 20 operating at an
average current density above approximately 100 mA/cm2 25 (e.g., greater than 200
mA/cm2) and the use of aqueous electrolytes 22/26. In a further example, the ion
conductivity of the separator layer 46 is greater than or equal to 0.05 S/cm.
In an additional example, the separator layer 46 has an electronic area specific
resistance of greater than approximately 1 x 104 Ω*cm2. Electronic area specific
30 resistance is similar to ionic area specific resistance but utilizes electric resistance
rather than ionic resistance in the calculation. In a further example, the separator
layer 46 has a per-cycle selectivity of greater than 99.995% based on use of
10
dissimilar electrolytes 22/26. Per-cycle selectivity is defined as the number of moles
of desired ion passed over a full charge/discharge cycle divided by the sum of the
number of moles of desired ion passed and the number of moles of reactant or other
species that can lead to degradation or a loss of current efficiency per
5 charge/discharge cycle.
The separator layer 46 can be fabricated using a technique that is capable of
producing a relatively uniform, thin layer of the polymer. Example techniques may
include, but are not limited to, solution casting, blade coating, spin coating, dip
molding, melt pressing, extruding, and sol-gel processing.
10 In additional examples, the fabrication technique is adapted to adjust a
balance between ion conductivity and selectivity. For example, where the polymer in
an as-fabricated state has low ion conductivity and high selectivity, the technique
may be adapted to sacrifice a portion of the selectivity in order to obtain better
conductivity. In this regard, the separator layer 46 can be fabricated with a controlled
15 porosity. The porosity permits greater uptake of acid groups (e.g., acid electrolyte),
which may non-covalently bond at the permanent dipoles of the polar groups of the
polymer to increase ion conductivity. While such porosity enhances conductivity, it
may also decrease selectivity by providing greater free volume through which
electrochemically active ions can migrate.
20 One example of an adapted fabrication technique includes inclusion of a
sacrificial additive, such as powder and/or liquid additives, in a solution casting
material. The sacrificial additive is mixed into and dispersed through the solution
casting material. Upon casting and drying/curing, the additive remains in the
separator layer 46. However, the additive is active with regard to the liquid
25 electrolyte used in the flow battery 20 such that the additive either dissolves or reacts
once exposed to the liquid electrolyte. The reaction or dissolution serves to remove
the additive from the separator layer 46, thereby leaving a controlled porosity in the
separator layer 46 for uptake of acid groups from the electrolyte. As examples, the
additive may include, but is not limited to, oxalic acid, polyethylene glycol, or
30 combinations thereof. The separator layer 46 may this be fabricated in a “dry” state
without any adsorbed liquid electrolyte and subsequently installed into the flow
battery 20 in the dry state, which facilitates greater toleration of stresses from
handling and compression during installation.
11
The reaction or dissolution of the powder may consume protons from the
liquid electrolyte; however, the effect on the liquid electrolyte will be low and can be
accounted for in initially formulating the liquid electrolyte to have a higher
concentration of the active species that are affected.
Although a combination of features 5 is shown in the illustrated examples, not
all of them need to be combined to realize the benefits of various embodiments of
this disclosure. In other words, a system designed according to an embodiment of
this disclosure will not necessarily include all of the features shown in any one of the
Figures or all of the portions schematically shown in the Figures. Moreover, selected
10 features of one example embodiment may be combined with selected features of
other example embodiments.
The preceding description is exemplary rather than limiting in nature.
Variations and modifications to the disclosed examples may become apparent to
those skilled in the art that do not necessarily depart from this disclosure. The scope
15 of legal protection given to this disclosure can only be determined by studying the
following claims.

WE CLAIM:
1. A flow battery comprising:
an electrochemical cell including a first electrode, a second electrode spaced
apart from the first electrode, and a separator 5 layer arranged between the first
electrode and the second electrode,
wherein the separator layer is formed of a polymer having a polymer
backbone with aromatic groups that are free of unsaturated nitrogen and one or more
polar groups bonded in the polymer backbone.
10
2. The flow battery as recited in claim 1, wherein the one or more polar groups
includes an atom selected from the group consisting of sulfur, oxygen, nitrogen, and
combinations thereof.
15 3. The flow battery as recited in claim 1, wherein the aromatic groups include
nitrogen heterocycles.
4. The flow battery as recited in claim 1, wherein the polymer backbone is free
of unsaturated nitrogen.
20
5. The flow battery as recited in claim 1, wherein the polymer includes at least
one of adsorbed acid groups or aqueous electrolyte that is non-covalently bonded to
the one or more polar groups.
25 6. The flow battery as recited in claim 1, wherein the polymer includes
polyetherimide (PEI).
7. The flow battery as recited in claim 1, wherein the polymer includes
polyamide-imide (PAI).
30
8. The flow battery as recited in claim 1, wherein the polymer includes
polyetheretherketone (PEEK).
13
9. The flow battery as recited in claim 1, wherein the polymer includes
polysulfone (PSF).
10. The flow battery as recited in claim 1, wherein the polymer includes
5 polyphenylene sulfide (PPS).
11. The flow battery as recited in claim 1, wherein the polymer is selected from
the group consisting of polyetherimide (PEI), polyamide-imide (PAI),
polyetheretherketone (PEEK), polysulfone (PSF), polyphenylene sulfide (PPS), and
10 combinations thereof.
12. The flow battery as recited in claim 1, further comprising a supply/storage
system external of the electrochemical cell, the supply/storage system including first
and second vessels, first and second liquid electrolytes in, respectively, the first and
15 second vessels, fluid lines connecting the first and second vessels to, respectively, the
first electrode and the second electrode, and a plurality of pumps operable to circulate
the first and second liquid electrolytes via the fluid lines between the first and second
vessels and the electrochemical cell.
20 13. The flow battery as recited in claim 1, wherein the separator layer has an area
specific resistance of less than approximately 425 mΩ*cm2.
14. A separator layer for use in a flow battery, the separator layer being formed of
a polymer having a polymer backbone with aromatic groups that are free of
25 unsaturated nitrogen, wherein the separator layer has an area specific resistance of
less than approximately 425 mΩ*cm2.
15. The separator layer as recited in claim 14, wherein the separator layer has an
area specific resistance of less than approximately 300 mΩ*cm2.
30
16. The separator layer as recited in claim 14, wherein the polymer is selected
from the group consisting of polyetherimide (PEI), polyamide-imide (PAI),
polyetheretherketone (PEEK), polysulfone (PSF), polyphenylene sulfide (PPS),
polystyrene (PS) and combinations thereof.
14
17. A flow battery comprising:
an electrochemical cell including a first electrode, a second electrode spaced
apart from the first electrode, and a separator layer arranged between the first
electrode and the second electrode, and the first electrode and the second electrode
are configured to operate at a current 5 density of greater than or equal to
approximately 100 mA/cm2; and
a supply/storage system external of the electrochemical cell, the
supply/storage system including first and second vessels, first and second liquid
electrolytes in, respectively, the first and second vessels, fluid lines connecting the
10 first and second vessels to, respectively, the first electrode and the second electrode,
and a plurality of pumps operable to circulate the first and second liquid electrolytes
via the fluid lines between the first and second vessels and the electrochemical cell,
wherein the separator layer is formed of a polymer having a polymer
backbone with aromatic groups that are free of unsaturated nitrogen and one or more
15 polar groups bonded in the polymer backbone.
18. A flow battery comprising:
an electrochemical cell including a first electrode, a second electrode spaced
apart from the first electrode, and a separator layer arranged between the first
20 electrode and the second electrode,
wherein the separator layer is formed of a polymer having a polymer
backbone with triazine groups.
19. The flow battery as recited in claim 18, wherein the polymer backbone
25 includes one or more polar groups bonded in the polymer backbone.
20. The flow battery as recited in claim 19, wherein the one or more polar groups
includes an atom selected from the group consisting of sulfur, oxygen, nitrogen, and
combinations thereof.