Electrochemical cell comprising an electrodeposited fuel

Patent metadata

Field	Value
Publication number	US-10818988-B2
Application number	US-201615076058-A
Country	US
Kind code	B2
Filing date	Mar 21, 2016
Priority date	Mar 19, 2015
Publication date	Oct 27, 2020
Grant date	Oct 27, 2020

Abstract

Provided is a rechargeable electrochemical cell system for generating electrical current using a fuel and an oxidant. The system includes a plurality of electrochemical cells. A controller is configured to apply an electrical current between charging electrode(s) and a fuel electrode with the charging electrode(s) functioning as an anode and the fuel electrode functioning as a cathode, such that reducible metal fuel ions in the ionically conductive medium are reduced and electrodeposited as metal fuel in oxidizable form on the fuel electrode. The controller may selectively apply current to a charging electrode and third electrode between fuel electrodes of separate cells to increase uniformity of the metal fuel being electrodeposited on the fuel electrode. The controller controls a number of switches to apply current to the electrodes and select different modes for the system. Also provided are methods for charging and discharging an electrochemical cell system, and selecting different modes.

First claim

What is claimed:

1. An electrochemical cell system comprising:
a plurality of electrochemical cells, wherein each electrochemical cell comprises:
a set of electrodes comprising:
a fuel electrode;
an oxidant electrode spaced apart from the fuel electrode;
a first charging electrode positioned between the oxidant electrode and the fuel electrode;
a second charging electrode positioned on the side of the oxidant electrode opposite the side facing the fuel electrode;

a third charging electrode positioned between the fuel electrodes of separate electrochemical cells;
the plurality of electrochemical cells being arranged such that the fuel electrode of the set of electrodes in each electrochemical cell is positioned closest to the third charging electrode in the electrochemical cell system;
an ionically conductive medium common to the plurality of electrochemical cells and contacting the set of electrodes of each electrochemical cell; and
a plurality of switches, each switch being associated with one of the electrodes and operatively coupled to a controller, wherein one or more of the first charging electrode and the second charging electrode is electrically connected through a switch and one or more fuel electrodes is electrically connected through a switch, wherein the controller is configured to select between charge modes, wherein the controller is configured to control discharge and charge operations of the cells by controlling an open state and a closed state for each switch of the plurality of switches, such that at least one of the plurality of switches is in an open state and at least one of the plurality of switches is in a closed state during each of the discharge and charge operations, wherein the third charging electrode is configured to be continuously or intermittently electrically connected through a switch, and wherein one of the charge modes is a mode for increasing uniformity of metal fuel being electrodeposited on the fuel electrode, wherein:
one or more first switches associated with each first charging electrode are closed to provide the electrical current to each first charging electrode,
one or more second switches associated with each fuel electrode are closed to provide the electrical current to each fuel electrode, and
a third switch associated with the third charging electrode is continuously or intermittently closed to provide the electrical current to the third charging electrode.

2. The electrochemical cell system according to claim 1 , wherein said controller is configured to:
in a standard charge mode, apply an electrical current between at least one charging electrode and a fuel electrode, with the charging electrode(s) functioning as an anode and the fuel electrode functioning as a cathode, such that reducible metal fuel ions in the ionically conductive medium are reduced and electrodeposited as metal fuel in oxidizable form on the fuel electrode.

3. The electrochemical cell system according to claim 1 , wherein the plurality of electrochemical cells are connected in series.

4. The electrochemical cell system according to claim 3 , wherein one of the charge modes comprises a standard charging mode wherein the one or more first switches associated with each first charging electrode are closed to provide the electrical current to each first charging electrode functioning as an anode and the one or more second switches associated with each fuel electrode are closed to provide the electrical current to each fuel electrode functioning as a cathode.

5. The electrochemical cell system according to claim 4 , further comprising a charging mode for supplementing convective flow within one or more of the electrochemical cells wherein one or more switches associated with each second charging electrode are continuously or intermittently closed to provide the electrical current to each second charging electrode functioning as an anode and the one or more switches associated with each fuel electrode are closed to provide the electrical current to each fuel electrode functioning as a cathode.

6. The electrochemical cell system of claim 5 , wherein the charging mode for supplementing convective flow further comprises the one or more switches associated with each first charging electrode being continuously or intermittently closed to provide the electrical current to each first charging electrode.

7. The electrochemical cell system according to claim 1 , wherein the controller is further configured to: (c) in a discharge mode, connect a fuel electrode to a load such that the fuel electrode functions as an anode and the oxidant electrode functions as a cathode, such that oxidized fuel flows from the fuel electrode to the load and the oxidant reduction electrode reduces any received oxidizer.

8. The electrochemical cell system according to claim 1 , wherein one of the charge modes comprises a mode for supplementing convective flow within one or more of the electrochemical cells, wherein one or more switches associated with each second charging electrode are continuously or intermittently closed to provide the electrical current to each second charging electrode functioning as an anode and the one or more switches associated with each fuel electrode are closed to provide the electrical current to each fuel electrode functioning as a cathode.

9. The electrochemical cell system according to claim 1 , wherein one of the charge modes comprises a parallel charging mode wherein:
the first switch associated with each first charging electrode in the cell system is closed to provide the electrical current to each first charging electrode functioning as an anode,
the second switch associated with each fuel electrode is closed to provide the electrical current to each fuel electrode functioning as a cathode,
the third switch associated with the third charging electrode is closed to provide the electrical current to the third charging electrode functioning as an anode, and
a fourth switch associated with each second charging electrode is closed to provide the electrical current to each second charging electrode functioning as an anode.

10. The electrochemical cell system according to claim 1 , wherein one of the charge modes comprises a mixed mode wherein the first switch associated with each first charging electrode in the cell system is closed to provide the electrical current to each first charging electrode functioning as an anode, and one of the second switches associated with one of the fuel electrodes is closed to provide the electrical current to the one fuel electrode functioning as a cathode while another second switch associated with the other fuel electrode is open.

11. The electrochemical cell system of claim 1 , wherein the fuel electrode comprises a series of permeable electrode bodies arranged in spaced apart relation.

12. The electrochemical cell system of claim 1 , wherein each charging electrode is selected from the group consisting of (a) the oxidant electrode and (b) a third electrode spaced from the fuel electrode and the oxidant electrode.

13. The electrochemical cell system according to claim 1 , wherein said controller is configured to vary the number of charging electrodes to which the electrical current is applied while performing a recharging operation.

14. The electrochemical cell system according to claim 1 , wherein the controller is configured to select between charge modes based on at least one input parameter.

15. The electrochemical cell system according to claim 14 , wherein the controller is operatively connected to a sensor that senses a condition of the electrochemical ce

Assignees

• Nantenergy Inc
• Form Energy Inc

Inventors

• Krishnan Ramkumar
• Friesen Cody
• Hayes Joel
• Trimble Todd
• Friesen Grant

Classifications

• Y02E60/50

  Fuel cells · CPC title

• Y02P70/50

  Manufacturing or production processes characterised by the final manufactured product · CPC title

• H01M50/73

  Electrolyte stirring by the action of gas on or in the electrolyte · CPC title

• H01M10/30

  Nickel accumulators (H01M10/34 takes precedence) · CPC title

• H01M10/06

  Lead-acid accumulators (semi-lead accumulators H01M10/20) · CPC title