Battery cell stack and redox flow battery

1. A battery cell stack comprising:

a plurality of stacked bipolar plates;

battery cells placed between the individual bipolar plates; and

a current collector plate electrically connected to each of a pair of end bipolar plates located at both ends in the stacking direction among the plurality of bipolar plates,

wherein two members in contact with each other between the current collector plate and the end bipolar plate are made of materials such that, when an accelerated test satisfying the following conditions 1 to 3 is performed, the electrical resistance value between the current collector plate and the end bipolar plate after the accelerated test is 1.05 times or less the electrical resistance value between the current collector plate and the end bipolar plate before the accelerated test:

Condition 1 is that a cycle includes applying pressure over one minute to achieve a predetermined pressure, maintaining the predetermined pressure for one minute, and bringing the predetermined pressure back to the atmospheric pressure over one minute;

Condition 2 is that the predetermined pressure is set to be the atmospheric pressure +0.1 MPa; and

Condition 3 is that the number of cycles is set to 18.

2. The battery cell stack according to claim 1 , wherein the corrosion potential difference between any two members in contact with each other between the current collector plate and the end bipolar plate is 0.35 V or less.

3. The battery cell stack according to claim 2 ,

wherein the current collector plate is provided with a current collector plate covering layer formed on a portion of the surface thereof facing the end bipolar plate,

the end bipolar plate is provided with a bipolar plate covering layer formed on a portion of the surface thereof facing the current collector plate,

the current collector plate covering layer and the bipolar plate covering layer are made of materials such that the corrosion potential difference between the two covering layers is 0.35 V or less, and

the current collector plate and the end bipolar plate are in contact with each other with their respective covering layers therebetween.

4. The battery cell stack according to claim 3 , wherein the current collector plate covering layer is a tin or tin alloy layer, and

the bipolar plate covering layer is a tin or tin alloy layer.

5. The battery cell stack according to claim 2 , further comprising an electrically conductive cushion member which is disposed between and in contact with the current collector plate and the end bipolar plate,

wherein the cushion member is at least one selected from the group consisting of a mesh, a foil, and a felt made of a material such that the corrosion potential difference between the cushion member and the end bipolar plate is 0.35 V or less,

the current collector plate is provided with a current collector plate covering layer formed on a portion of the surface thereof facing the cushion member,

the current collector plate covering layer is made of a material such that the corrosion potential difference between the current collector plate covering layer and the cushion member is 0.35 V or less, and

the current collector plate and the cushion member is in contact with each other with the current collector plate covering layer therebetween.

6. The battery cell stack according to claim 5 , wherein the cushion member contains a carbon material as an electrically conductive material, and

the current collector plate covering layer is a carbon material layer.

7. The battery cell stack according to claim 1 , wherein the corrosion potential difference between the current collector plate and a member in contact with the current collector plate between the current collector plate and the end bipolar plate is 0.45 to 0.55 V.

8. The battery cell stack according to claim 7 , wherein the current collector plate and the end bipolar plate is in direct contact with each other, and

the current collector plate and the end bipolar plate are made of materials such that the corrosion potential difference therebetween is 0.45 to 0.55 V.

9. The battery cell stack according to claim 8 , wherein the current collector plate is made of nickel, a nickel alloy, copper, a copper alloy, silver, a silver alloy, titanium, a titanium alloy, or stainless steel.

10. The battery cell stack according to claim 7 , further comprising an electrically conductive cushion member which is disposed between and in contact with the current collector plate and the end bipolar plate, the cushion member being composed of at least one selected from the group consisting of a mesh, a foil, and a felt,

wherein the current collector plate and the cushion member are made of materials such that the corrosion potential difference therebetween is 0.45 to 0.55 V.

11. The battery cell stack according to claim 10 , wherein the current collector plate is made of nickel, a nickel alloy, copper, a copper alloy, silver, a silver alloy, titanium, a titanium alloy, or stainless steel.

12. A redox flow battery comprising:

the battery cell stack according to claim 1 ;

a positive electrode circulation mechanism which circulates a positive electrode electrolyte to the battery cell stack; and

a negative electrode circulation mechanism which circulates a negative electrode electrolyte to the battery cell stack.