Determining of a spatial distribution of the electrical contact resistance of an electrochemical cell

Patent metadata

Field	Value
Publication number	US-10162012-B2
Application number	US-201615271732-A
Country	US
Kind code	B2
Filing date	Sep 21, 2016
Priority date	Sep 21, 2015
Publication date	Dec 25, 2018
Grant date	Dec 25, 2018

Abstract

A method for determining a spatial distribution (Rc x,y f ) of a parameter of interest (Rc) representative of a contact resistance between a bipolar plate and an adjacent electrode of an electrochemical cell, in which a spatial distribution (Rc x,y f ) of the parameter of interest (Rc) is determined depending on the spatial distribution (Q x,y e ) of a second thermal quantity (Q c ) estimated beforehand from the spatial distribution (T x,y c ) of a set-point temperature (Tc) and from the spatial distribution (D x,y r ) of a first thermal quantity (D r ).

First claim

The invention claimed is:

1. A method for determining a spatial distribution (Rc x,y f ) of a parameter of interest (Rc) representative of a contact resistance between a given bipolar plate among at least two bipolar plates and an adjacent electrode of an electrochemical cell, said electrochemical cell including two electrodes separated from one another by an electrolyte and placed between the at least two bipolar plates, said electrochemical cell being configured to supply reactive species to the two electrodes and and to remove heat produced by the electrochemical cell in operation, comprising steps of:
i) providing the electrochemical cell, within which the parameter of interest (Rc) has an initial spatial distribution (Rc x,y i ) of one or more values of contact resistance, and within which a spatial distribution of a temperature within the electrochemical cell in operation has at least one local temperature value that is greater than or equal to a preset maximum local temperature value;
ii) defining a spatial distribution (T x,y c ) of a set-point temperature (T c ) within the electrochemical cell in operation, said spatial distribution (T x,y c ) of the set-point temperature (T c ) within the electrochemical cell in operation being such that local temperature values are lower than preset maximum local temperature values, and such that said spatial distribution (T x,y c ) of the set-point temperature (T c ) within the electrochemical cell in operation is such that a local set point temperature gradient is substantially constant;
iii) measuring a spatial distribution (D x,y r ) of a first thermal quantity (D r ) representative of local removal of heat within said electrochemical cell in operation;
iv) estimating a spatial distribution (Q x,y e ) of a second thermal quantity (Q e ) representative of local production of heat within said electrochemical cell in operation, depending on said spatial distribution (T x,y c ) of the set-point temperature (T c ) within the electrochemical cell in operation and on said spatial distribution (D x,y r ) of the first thermal quantity (D r ) representative of the local removal of heat within said electrochemical cell in operation, so that the spatial distribution of the temperature of said electrochemical cell in operation, the first thermal quantity (D r ) of the cell having said measured spatial distribution (D x,y r ) of the first thermal quantity (D r ) representative of the local removal of heat within said electrochemical cell in operation, and the second thermal quantity (Q e ) of the cell having said estimated spatial distribution (Q x,y e ) of the second thermal quantity (Q e ) representative of the local production of heat within said electrochemical cell in operation, is substantially equal to said spatial distribution (T x,y c ) of the set-point temperature (T c ) within the electrochemical cell in operation; and
v) determining the spatial distribution (Rc x,y f ) of the parameter of interest (Rc) depending on the estimated spatial distribution (Q x,y e ) of the second thermal quantity (Q e ),
wherein the step (iv) of estimating the spatial distribution (Q x,y e ) of the second thermal quantity (Q e ) representative of the local production of heat within said electrochemical cell in operation includes:
generating a mesh of a cooling circuit of at least one bipolar plate of the among at least two bipolar plates, the cooling circuit being configured to permit flow of a heat-transfer fluid, and
simulating, numerically by a computer, the second thermal quantity (Q e ) on said mesh, by solving a discrete numerical model expressing the second thermal quantity (Q e ) as a function of the at least one local temperature and of the first thermal quantity (D r ).

2. The method according to claim 1 , wherein the parameter of interest (Rc) is an electrical contact resistance of the electrochemical cell, the first thermal quantity (D r ) is representative of the local removal of the heat produced by the electrochemical cell in operation, and the second thermal quantity (Q e ) is representative of the local production of heat by the electrochemical cell in operation.

3. The method according to claim 1 , wherein the at least two bipolar plates are formed from two sheets that are bonded to each other, each sheet of said two sheets including embossments having an external face defining a circuit configured to distribute the reactive species, the embossments of the sheets together having internal faces, which are opposite the external faces, defining a cooling circuit including cooling channels in fluid communication with one another between an inlet and an outlet of the cooling circuit.

4. The method according to claim 1 , wherein the step v) of determining the spatial distribution (Rc x,y f ) of the parameter of interest (Rc) further depends on a preset overall electrical power value of the electrochemical cell.

5. The method according to claim 1 , wherein the first thermal quantity (D r ) is the measured effective local flow rate of heat-transfer fluid flowing in cooling circuit of at least one bipolar plate of the electrochemical cell, and the second thermal quantity (Q e ) is the local heat flux produced by the electrochemical cell in operation.

6. The method according to claim 5 , wherein the step v) of determining the spatial distribution (Rc x,y f ) of the parameter of interest (Rc) further includes:
a) a first sub-step of estimating the spatial distribution (I e ) of the density of an electrical signal produced by the electrochemical cell in operation, from the estimated spatial distribution (Q x,y e ) of the local heat flux; and
b) a second sub-step of determining the spatial distribution (Rc x,y f ) of the parameter of interest (Rc), from a local density of the electrical signal.

7. A method for producing an electrochemical cell, including steps of:
i) considering a reference electrochemical cell including two electrodes separated from each other by an electrolyte and placed between bipolar plates configured to supply reactive species to the electrodes and to remove heat produced by the electrochemical cell in operation, the bipolar plates having an initial thickness spatial distribution (e x,y PB,i ), the electrochemical cell having a parameter of interest (Rc) representative of the electrical contact resistance, said parameter of interest (Rc) being spatially distributed with an initial distribution (Rc x,y i );
ii) determining a spatial distribution (Rc x,y f ) of the parameter of interest (Rc), using the method according to claim 1 ; and
iii) producing said electrochemical cell from the reference electrochemical cell such that the parameter of interest (Rc) has the determined spatial distribution (Rc x,y f ).

8. The method for producing an electrochemical cell according to claim 7 , wherein a thickness spatial distribution (e x,y PB,f ) of a thickness of at least one of the bipolar plates is determined depending on the determined spatial distribution (Rc x,y f ).

9. The method for producing an electrochemical cell according to claim 8 , wherein said at least one of the bipolar plates has a local thickness e x,y PB,f different than a nominal plate thickness substantially equal to an initial thickness e x,y PB,f of said at least one of the bipolar plates in zones identified using said determined spatial distribution (Rc x,y f ) of the electrical contact resistance.

10. A method for producing an electrochemical reactor, including steps of:
i. considering a reference electrochemical reactor including a stack of electrochemical cells clamped and compressed between two end plates, each of the electrochemical cells compris

Assignees

• Commissariat Energie Atomique

Inventors

• Poirot-Crouvezier Jean-Philippe
• Nandjou Dongmeza Fredy-Intelligent
• Robin Christophe
• Gerard Mathias
• Micoud Fabrice

Classifications

• H01M8/0247

  characterised by the form (characterised by a channel configuration H01M8/0258) · CPC title

• H01M8/0254

  corrugated or undulated · CPC title

• H01M8/0432

  Temperature; Ambient temperature · CPC title

• H01M8/04574

  Current · CPC title

• H01M8/04902

  of the individual fuel cell · CPC title