Control device and method for charging a non-aqueous rechargeable metal-air battery

Abstract

A control device for controlling charging of a non-aqueous metal air battery, the control device being configured to: determine a CO.sub.2 concentration (C.sub.x) and an increase rate (RCO.sub.2) of CO.sub.2 concentration in the battery, charge the battery in case both the CO.sub.2 concentration (C.sub.x) before starting charging exceeds a predetermined CO.sub.2 threshold (C.sub.T) and the increase rate of the CO.sub.2 concentration (RCO.sub.2) during charging is below a predetermined threshold value (ΔC.sub.T/ΔAh.sub.T, ΔC.sub.T/Δt), and stop charging when the increase rate (RCO.sub.2) exceeds the predetermined threshold value (ΔC.sub.T/ΔAh.sub.T, ΔC.sub.T/Δt). Also, a corresponding method of controlling charging of a rechargeable battery.

Claims

1. A control device for controlling charging of a non-aqueous metal air battery, the control device being configured to: determine a CO.sub.2 concentration (C.sub.x) and an increase rate (RCO.sub.2) of CO.sub.2 concentration in the battery, charge the battery in case both the CO.sub.2 concentration (CO before starting charging exceeds a predetermined CO.sub.2 threshold (C.sub.T) and the increase rate of the CO.sub.2 concentration (RCO.sub.2) during charging is below a predetermined threshold value (ΔC.sub.T/ΔAh.sub.T, ΔC.sub.T/Δt), and stop charging when the increase rate (RCO.sub.2) exceeds the predetermined threshold value (ΔC.sub.T/ΔAh.sub.T, ΔC.sub.T/Δt), wherein the battery comprises a gas compartment, at least one cell with an air cathode, a metal anode, and a non-aqueous electrolyte, the gas compartment is configured such that a reactant provided to the cell is controlled, the control device is configured to control feeding of the reactant to the battery, and the control device is configured to determine the CO.sub.2 concentration (C.sub.x) in at least one of the air cathode and the non-aqueous electrolyte, and wherein the control device includes a CO.sub.2 sensor configured to measure the CO.sub.2 concentration (C.sub.x) in the battery, the CO.sub.2 sensor is configured to be arranged in at least one of the air cathode, the non-aqueous electrolyte, and the gas compartment, and the CO.sub.2 sensor is deactivated during discharge of the battery.

2. The control device according to claim 1, further configured to: charge the battery, in case the CO.sub.2 concentration (C.sub.x) in the battery before starting charging does not exceed the predetermined CO.sub.2 threshold (C.sub.T), and in this case, stop charging when the CO.sub.2 concentration in the battery during charging increases such that it exceeds the predetermined CO.sub.2 threshold (C.sub.T).

3. The control device according to claim 1, wherein the increase rate (RCO.sub.2) of CO.sub.2 concentration is a CO.sub.2/capacity relation (ΔC.sub.x/ΔAh.sub.x), the CO.sub.2/capacity relation (ΔC.sub.x/ΔAh.sub.x) being a relation between the increment of CO.sub.2 concentration (ΔC.sub.X) during a predetermined time interval (Δt) and the increment of capacity (ΔAh.sub.x) of the battery during the predetermined time interval (Δt).

4. The control device according to claim 1, wherein the increase rate (RCO.sub.2) of CO.sub.2 concentration is a relation (ΔC.sub.X/Δt) between the increment of CO.sub.2 concentration (ΔC.sub.X) during a predetermined time interval (Δt) and the predetermined time interval (Δt).

5. The control device according to claim 1, the battery additionally comprising a metal anode and a non-aqueous electrolyte, wherein the cell is arranged inside the gas compartment, and the control device is further configured to determine the CO.sub.2 concentration (C.sub.X) in the gas compartment.

6. The control device according to claim 1, wherein the CO.sub.2 sensor is an electrochemical sensor and/or a semiconductor sensor.

7. A battery pack comprising: at least one non-aqueous metal air battery, and a control device according to claim 1.

8. The battery pack according to claim 7, the non-aqueous metal air battery comprising at least one cell with an air cathode, a metal anode and a non-aqueous electrolyte.

9. A vehicle comprising: an electric motor, and a battery pack according to claim 7.

10. A battery charging system comprising: at least one non-aqueous metal air battery, a battery management system for the battery, and a control device according to claim 1.

11. A vehicle comprising: an electric motor, at least one non-aqueous metal air battery, and a control device according to claim 1.

12. The control device according to claim 1, wherein the reactant is O.sub.2.

13. The control device according to claim 1, wherein the reactant is fed to the battery during discharge of the battery.

14. A method of controlling charging of a non-aqueous metal air battery, the battery comprising a gas compartment, at least one cell with an air cathode, a metal anode, and a non-aqueous electrolyte, the gas compartment being configured such that a reactant provided to the cell is controlled, the method comprising the steps of: feeding the reactant to the battery, providing a CO.sub.2 sensor configured to measure a CO.sub.2 concentration (C.sub.x) in the battery, arranging the CO.sub.2 sensor in at least one of the air cathode, the non-aqueous electrolyte, and the gas compartment, the CO.sub.2 sensor being deactivated during discharge of the battery, determining the CO.sub.2 concentration (C.sub.x) in at least one of the air cathode and the non-aqueous electrolyte, determining an increase rate (RCO.sub.2) of CO.sub.2 concentration in the battery, charging the battery in case both the CO.sub.2 concentration (C.sub.x) before starting charging exceeds a predetermined CO.sub.2 threshold (C.sub.T) and the increase rate of the CO.sub.2 concentration (RCO.sub.2) during charging is below a predetermined threshold value, and stopping charging when the increase rate (RCO.sub.2) exceeds the predetermined threshold value (ΔC.sub.T/ΔAh.sub.T, ΔC.sub.T/Δt).

15. The method according to claim 14, further comprising the steps of: charging the battery, in case the CO.sub.2 concentration (C.sub.x) in the battery before starting charging does not exceed the predetermined CO.sub.2 threshold (C.sub.T), and in this case, stopping charging when the CO.sub.2 concentration in the battery during charging increases such that it exceeds the predetermined CO.sub.2 threshold (C.sub.T).

16. The method according to claim 14, wherein the increase rate (RCO.sub.2) of CO.sub.2 concentration is a CO.sub.2/capacity relation (ΔC.sub.x/ΔAh.sub.x), the CO.sub.2/capacity relation (ΔC.sub.x/ΔAh.sub.x) being a relation between the increment of CO.sub.2 concentration (ΔC.sub.X) during a predetermined time interval (Δt) and the increment of capacity (ΔAh.sub.x) of the battery during the predetermined time interval (Δt).

17. The method according to claim 14, wherein the increase rate (RCO.sub.2) of CO.sub.2 concentration is a relation (ΔC.sub.X/Δt) between the increment of CO.sub.2 concentration (ΔC.sub.X) during a predetermined time interval (Δt) and the predetermined time interval (Δt).

18. The method according to claim 14, wherein the CO.sub.2 concentration (C.sub.X) is determined in the gas compartment.

19. A control device for controlling charging of a non-aqueous metal air battery, the control device being configured to: determine a CO.sub.2 concentration (CO and an increase rate (RCO.sub.2) of CO.sub.2 concentration in the battery, charge the battery in case both the CO.sub.2 concentration (C.sub.x) before starting charging exceeds a predetermined CO.sub.2 threshold (C.sub.T) and the increase rate of the CO.sub.2 concentration (RCO.sub.2) during charging is below a predetermined threshold value (ΔC.sub.T/ΔAh.sub.T, ΔC.sub.T/Δt), and stop charging when the increase rate (RCO.sub.2) exceeds the predetermined threshold value (ΔC.sub.T/ΔAh.sub.T, ΔC.sub.T/Δt), wherein the control device includes a CO.sub.2 sensor configured to measure the CO.sub.2 concentration (C.sub.x) in the battery and the CO.sub.2 sensor is deactivated during discharge of the battery.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 shows a schematic representation of a vehicle or a stationary system comprising a control device according to an embodiment of the present disclosure;

(2) FIG. 2a shows a schematic representation of a metal air battery with a cell inside a gas compartment;

(3) FIG. 2b shows a schematic representation of a metal air battery with several cells sharing the same gas compartment;

(4) FIGS. 3a and 3b show exemplary and schematic diagrams of the ideal and the real case of O.sub.2 and CO.sub.2 production during the lifetime of the battery;

(5) FIG. 4 shows a flow chart of the charging control procedure according to an embodiment of the present disclosure;

(6) FIG. 5a to 5c show exemplary and schematic diagrams of different CO.sub.2 concentrations and increase rates in the battery during one charging cycle.

DESCRIPTION OF THE EMBODIMENTS

(7) Reference will now be made in detail to exemplary embodiments of the disclosure, examples of which are illustrated in the accompanying drawings. Wherever possible, the same reference numbers will be used throughout the drawings to refer to the same or like parts.

(8) FIG. 1 shows a schematic representation of a vehicle or a stationary system 1 comprising a control device 6 according to an embodiment of the present disclosure. In the following a vehicle 1 is described, however a stationary system comprises corresponding elements unless indicated in the to following description. The vehicle 1 may be a hybrid vehicle or an electric vehicle (i.e. a purely electrically driven vehicle). The vehicle 1 comprises at least one electric motor 4, which is powered by a battery or battery pack 2, preferably via an inverter 3. In case of a stationary system an electric distribution board 3 is desirably used instead or in addition to the inverter.

(9) If the vehicle 1 is a hybrid vehicle, it further includes an internal combustion engine. The battery 2 is a metal air battery, in particular a non-aqueous metal air battery. The battery 2 comprises at least one cell which is preferably arranged in a gas compartment. Said gas compartment is desirably configured such that gas provided to the cell (e.g. O.sub.2) and gases emitted by the cell (e.g. O.sub.2, and possibly CO.sub.2) can be controlled.

(10) The battery 2 is connected to a battery management system (BMS) 5 which is configured to charge the battery 2. For this purpose the battery management system 5 may comprise an electric control circuit, as e.g. a power electronics circuit. The battery management system may further comprise or be connected to a connector for external charging by an external power source. The connector may be e.g. a plug or a wireless connector system. In case the vehicle is a hybrid vehicle, the battery management system may further be connected to the electrical generator of the internal combustion engine of the vehicle. Consequently, the battery 2 may be charged, when the internal combustion engine is operating and/or when the vehicle is connected to an external power source. Furthermore the battery 2 may be discharged, in order to operate the vehicle 1, in particular the electric motor 4. The battery 2 may further be discharged in a battery treatment and/or recovery procedure.

(11) In order to control charging and desirably also discharging the vehicle 1 is provided with the control device 6 and one or several sensors 7. For this purpose the control device 6 monitors the battery 2 via the sensors 7 and controls the battery management system 5. The control device 6 and/or the sensors 7 may also be comprised in the battery 2. The control device may be an electronic control circuit (ECU). It may also comprise a data storage. It is also possible that the vehicle comprises a smart battery charging system with a smart battery and a smart charging device. In other words, both the battery and the vehicle may comprise each an ECU which operate together and form together the control device according to the disclosure. Furthermore the control device 6 may be part of a battery charging system. Accordingly said system comprises at least one non-aqueous metal air battery 2, a battery management system (BMS) 5, a control device 6, and desirably also the sensors 7.

(12) The control device 6 may comprise an application specific integrated circuit (ASIC), an electronic circuit, a processor (shared, dedicated, or group), a combinational logic circuit, a memory that executes one or more software programs, and/or other suitable components that provide the described functionality of the control device 6.

(13) As it will be explained in more detail in the following, the sensors 7 comprise in particular at least one CO.sub.2 sensor 8 of a first type, at least one CO.sub.2 sensor 9 of a second type, and/or at least one CO.sub.2 sensor 10 of a third type.

(14) Moreover the sensors 7 may comprise one or more temperature sensors for measuring the temperature of the battery 2, at least one current sensor (Amp sensor), in particular for measuring the state of charge of the battery 2, and at least one further voltage sensor for measuring the voltage of the battery 2. The current sensor desirably measures the current flowing into the battery during charging. The current sensor is desirably configured to measure the increase rate of capacity ΔAh.sub.x of the battery 2 during charging, i.e. in particular in unit A.

(15) In case of use in a metal air battery, where air or dried air is fed to the battery pack, the sensor(s) 7 are desirably de-activated during discharge, since air will be fed to the battery and contain CO.sub.2.

(16) In case of use in a metal air battery, where air is fed to the battery via a selective membrane retaining CO.sub.2 outside of the battery, the CO.sub.2 sensor(s) does not need to be de-activated during discharge but may be de-activated. Correspondingly, in case of use in Metal-O.sub.2 configuration where O.sub.2 is fed to the battery via a tank for example or another system, the CO.sub.2 sensor(s) does not need to be de-activated during discharge but may be de-activated.

(17) FIG. 2a shows a schematic representation of a metal air battery 2 with a cell inside a gas compartment 11. The gas compartment 11 is configured to encase one cell. Hence, in case the battery 2 comprises several cells, each of said cell has its own gas compartment 11. The cell is composed mainly of a metal anode 12, a (desirably non-aqueous) electrolyte (and/or separator) 14 and an air cathode 13. The electrolyte 14 is desirably placed between the anode 12 and the cathode 13. Further, the anode 12 and the cathode 13 comprise respectively an anode collector 15 and a cathode collector 16 on their outer surfaces. The anode collector 15 and the cathode collector 16 are connected to an electrical circuit.

(18) The anode 12 desirably comprises or consists of Lithium (Li). In the cathode 13, O.sub.2 is desirably the main reactant. The air cathode may be a Gas Diffusion Electrode (denoted GDE). For example, it might be composed typically of Carbon or any other conductive materials (gold, nickel . . . ), a binder and sometimes a catalyst. The catalyst may be in a solid form and contained in the air cathode. The catalyst may also be a soluble catalyst which is dissolved in certain ratio in the electrolyte and acts as a redox mediator (e.g. Tetratiafulvalene (TTF) or Iodine). In both cases, it is expected from the catalyst that they will facilitate the decomposition of the ideal discharge product being typically Li.sub.2O.sub.2. This Li.sub.2O.sub.2 is supposed to be decomposed during the charge to form back Li.sup.+ and O.sub.2. The cathode is usually a support for O.sub.2 reaction.

(19) A CO.sub.2 sensor 8 of the first type may be positioned and configured such that it measures CO.sub.2 in the air cathode 13, in particular the CO.sub.2 concentration dissolved in the air cathode. In such case the CO.sub.2 is detected in its gas form.

(20) Alternatively or additionally a CO.sub.2 sensor 9 of the second type may be placed in the electrolyte/separator 14. In such case the sensor 9 is positioned and configured such that it measures CO.sub.2 dissolved in the electrolyte.

(21) Alternatively or additionally a CO.sub.2 sensor 10 of the third type may be placed in the electrolyte/separator 14. In such case the sensor 10 is positioned and configured such that it measures CO.sub.2 dissolved in the electrolyte. Gas is usually soluble to a certain extend in some solution, i.e. the solvent of the electrolyte. When the solubility reaches a certain maximum, CO.sub.2 gas will be formed and create bubbles escaping from the electrolyte through the cathode and the gas compartment 11 then.

(22) FIG. 2b shows a schematic representation of a metal air battery 2 with several cells sharing the same gas compartment 11. The cells are arranged inside said gas compartment. In FIG. 2b two cells are shown, however, also a higher number of cells my be comprised by the battery. As it is shown the cell and the sensors 8 to 10 correspond to those of FIG. 2a. In case of a non-aqueous metal air battery using 2-compartment cells, where two different types of electrolytes will be used at anode side and cathode side, the CO.sub.2 sensor of the second type is desirably positioned and configured such that it measures CO.sub.2 in the compartment side of the cathode. Accordingly, only one of the sensors 10 shown in FIG. 2b may be used in the whole battery.

(23) Generally, the ideal reaction should be as follows: During discharge O.sub.2 is consumed to form ideal product Li.sub.2O.sub.x:2 Li+x/2 O.sub.2.fwdarw.Li.sub.2O.sub.x. This reaction is actually taking place in several steps in which the first one is related to the formation of O.sub.2.sup.− radicals as follows: O.sub.2+e.sup.−.fwdarw.O.sub.2.sup.−. During charge O.sub.2 is released: Li.sub.2O.sub.x.fwdarw.2 Li+x/2 O.sub.2.

(24) Nevertheless, during electrochemical processes of the battery, it can happen that some side reactions take place (for example O.sub.2.sup.− radicals react with the solvent molecules of the electrolyte and lead to the formation of side reactions products such as Lithium Carbonate (Li.sub.2CO.sub.3), Li formate, Lithium acetate, etc.). As a result, during the charging process it can happen that CO.sub.2 gas is released. In such case, bad re-chargeability of the battery occurs and poor capacity retention is observed.

(25) Accordingly, during charging of the battery as described above, it is possible that an unwanted product such as CO.sub.2 gas is evolved instead of or in addition to the expected O.sub.2 gas. This CO.sub.2 is detrimental for the battery since it contributes to the degradation of the battery.

(26) Furthermore, this CO.sub.2 is an indication that the battery is overcharging and usually is linked with a strong increase of voltage which is an indication of an unsafe use of the battery.

(27) As an example, for a small scale Li—O.sub.2 battery made with a cathode of approximately 1 mg carbon nanotubes (CNT), using 150 μL of electrolyte, having a capacity of >1000 mAh/-gCNT, during 1.sup.st discharge in total 7000 nmol of O.sub.2 can be consumed while <1000 nmol of CO.sub.2 should be released. The gas production rate of O.sub.2 for such battery will be in the range of <100 nmol O.sub.2/min, or <80 nmol O.sub.2/min, or <60 nmol O.sub.2/min. In the meantime, the gas production rate of CO.sub.2 for such battery will be in the range of <25 nmol CO.sub.2/min, or <20 nmol CO.sub.2/min or <15 nmol CO.sub.2/min or preferentially even below. It is clear that if the cathode size is greater, the amount of O.sub.2 and CO.sub.2 possibly produced will be different and then the sensor(s) specificities and accuracies will need to be adapted accordingly after experimental determination. Hence, the sensors 7 should be configured such that they detect CO.sub.2 gas in such dimensions. Generally, the sensors 7 should be configured such that they detect CO.sub.2 as gas and/or as CO.sub.2 dissolved in a non-aqueous media, or they should detect CO.sub.2 in presence of other gas (O.sub.2 especially). The sensors should be as small as possible (especially for automotive applications where volume matters). The detected level of CO.sub.2 should be expressed in ppm (ppm or % volume). The range should depend on the capacity of the battery.

(28) FIGS. 3a and 3b show exemplary and schematic diagrams of the ideal and the real case of O.sub.2 and CO.sub.2 production during the lifetime of the battery. FIG. 3a shows an ideal case, where no CO.sub.2 is produced during lifetime of the battery, i.e. the CO.sub.2 concentration in the battery during the charge cycles of the battery life is constantly zero. Accordingly, the concentration of the necessary reactant O.sub.2 is constantly high during the lifetime of the battery. However in a real case as shown in FIG. 3b, the concentration of CO.sub.2 increases during lifetime of the battery, i.e. during the charge cycles of the battery life. At the same time the concentration of O.sub.2 decreases during the lifetime of the battery.

(29) FIG. 4 shows a flow chart of the charging control procedure according to an embodiment of the present disclosure. The procedure may be carried out by the control device 6.

(30) In step S1 the procedure is started. The start may be triggered by a determination of the control device that charging of the battery is necessary (e.g. due to a low state of charge) and/or by the fact that charging becomes possible (e.g. due to operation of the internal combustion engine or due to a connection to an external electrical power source).

(31) In step S2 the concentration of CO.sub.2 is measured. Based on this measurement result it is determined in step S3 whether the measured CO.sub.2 concentration exceeds a predetermined CO.sub.2 concentration threshold. In case it does not, charging is started in step S4 and the conventional charging control procedure (i.e. case 1) is carried out.

(32) In step S5 the CO.sub.2 concentration is measured again, however now during charging. Based on this measurement result it is determined in step S6 whether the measured CO.sub.2 concentration exceeds the predetermined CO.sub.2 concentration threshold C.sub.T. In case it does not, charging is continued in step S7 and it is returned to step S5. Hence, as long as the measured CO.sub.2 concentration does not exceed the predetermined CO.sub.2 concentration and the battery is not yet fully charged, the loop S5 to S7 is continuously run, i.e. the CO.sub.2 concentration is continuously monitored during charging. The loop may be repeated every 5 or 10 seconds or once per minute.

(33) In case the measured CO.sub.2 concentration exceeds the predetermined CO.sub.2 concentration in step S6, or in case the battery is fully charged, charging is stopped in step S8.

(34) The predetermined CO.sub.2 concentration threshold C.sub.T is the threshold concentration of CO.sub.2 which is desirably determined experimentally in advance depending on the battery specifications (type, size, volume, packaging, shape, etc.) and applications (automotive, stationary, etc.).

(35) In case it is determined in step S3 that before starting charging the measured CO.sub.2 concentration exceeds the predetermined CO.sub.2 concentration threshold, charging is started in step S9 and the charging control procedure according to case 2 is carried out. In this procedure charging is controlled based on the determined increase rate of CO.sub.2 concentration ΔC.sub.x.

(36) In step S10 the CO.sub.2 concentration C.sub.x1 and the capacity of the battery Ah.sub.x1 are measured at a first time point.

(37) Subsequently, in step S11 the CO.sub.2 concentration C.sub.x2 and the capacity of the battery Ah.sub.x2 are measured at a second time point, i.e. after a predetermined time interval Δt of e.g. 1, 5 or 10 minutes.

(38) In step S12 the increment of CO.sub.2 concentration ΔC.sub.x is determined, i.e. ΔC.sub.x=C.sub.x2−C.sub.x1. Furthermore the increment of capacity ΔAh.sub.x is determined or measured, i.e. ΔAh.sub.x=Ah.sub.x2−Ah.sub.x1.

(39) In step S13, the relation of ΔC.sub.x/ΔAh.sub.x is determined which provides the increase rate RCO.sub.2 of CO.sub.2 concentration. Furthermore it is determined, whether the relation ΔC.sub.x/ΔAh.sub.x exceeds a predetermined relation threshold ΔC.sub.T/ΔAh.sub.T.

(40) In case it does not, charging is continued in step S14 and it is returned to step S10. Hence, as long as the measured relation ΔC.sub.x/ΔAh.sub.x does not exceed the predetermined relation threshold ΔC.sub.T/ΔAh.sub.T and the battery is not yet fully charged, the loop S10 to S14 is continuously run, i.e. the CO.sub.2 concentration increase rate in view of the capacity increase rate is continuously monitored during charging. The loop may be repeated every 5 or 10 seconds or once per minute.

(41) In case the relation ΔC.sub.x/ΔAh.sub.x determined in step S13 exceeds the predetermined relation threshold ΔC.sub.T/ΔAh.sub.T or in case the battery is fully charged, charging is stopped in step S15.

(42) The predetermined relation threshold ΔC.sub.T/ΔAh.sub.T is the threshold rate of formation of CO.sub.2 which is desirably determined in advance depending on the battery specifications (type, size, volume, packaging, shape, etc.) and applications (automotive, stationary, etc.).

(43) According to an alternative embodiment the same procedure is applied as described above in context of FIG. 4 but with the following differences in steps S10 to S13:

(44) In steps S10 and S11 the CO.sub.2 concentrations C.sub.x1 and C.sub.x2 are measured at a first and a second time point but not necessarily the capacity of the battery Ah.sub.x1 and Ah.sub.x2.

(45) In step S12 the increment of CO.sub.2 concentration ΔC.sub.x is determined, i.e. ΔC.sub.x=C.sub.x2−C.sub.x1.

(46) In step S13, the increase rate RCO.sub.2 of CO.sub.2 concentration is determined as a relation ΔC.sub.x/Δt. Hence, in this alternative embodiment the increase rate of CO.sub.2 concentration ΔC.sub.x per time interval Δt is determined. Furthermore it is determined, whether the relation ΔC.sub.x/Δt exceeds a predetermined relation threshold ΔC.sub.T/Δt.

(47) It should be noted that in the charging control procedure according to case 2 CO.sub.2 will be released and will deteriorate the battery but in a moderate way. However, if only a moderate amount of CO.sub.2 is given to the battery, the battery can still work even if it deteriorates a bit. Only if a too strong amount of CO.sub.2 is given to the battery, the battery might become completely inoperable.

(48) According to a first example, in case the battery will use air as a source of O.sub.2, CO.sub.2 present in the air will enter the battery during the discharge process. In such case, during the charge it is possible that the sensor(s) will detect CO.sub.2 present in the battery. But even in this case, the battery should be able to be charged. The charging control procedure according to case 2 will then apply to charge the battery.

(49) According to a second example, in case a Li-Air (O.sub.2) battery uses an electrolyte like Propylene carbonate or other carbonates or a mixture of electrolyte containing carbonates, etc., Li.sub.2CO.sub.3 will be (partially) the discharge product (instead of Li.sub.2O.sub.2). When Li.sub.2CO.sub.3 decomposes, it forms CO.sub.2 in majority (less/no O.sub.2). However, charging can still be controlled with the charging control procedure according to case 2.

(50) According to a third example, in case the Li-Air (O.sub.2) battery uses a more suitable electrolyte (e.g. DME (Dimethoxyethane, also known as glyme, monoglyme, dimethyl glycol, ethylene glycol dimethyl ether) but does not contain a catalyst, Li.sub.2O.sub.2 is the main discharge product. But still it may be difficult to decompose Li.sub.2O.sub.2 without a catalyst in order to form O.sub.2. Then the potential of the battery will raise and there may be a competition between the Li.sub.2O.sub.2 decomposition to form O.sub.2 and the electrolyte decomposition to form CO.sub.2. Then it is possible that C.sub.x>C.sub.T. However, charging can still be controlled with the charging control procedure according to case 2.

(51) FIG. 5a to 5c show exemplary and schematic diagrams of different CO.sub.2 concentrations and increase rates in the battery during charging (i.e. one charging cycle). The diagrams show the development of the CO.sub.2concentration C.sub.x versus the development of the capacity Ah.sub.x during charging, i.e. during a charging cycle. As can be seen in FIG. 5a to 5c, the CO.sub.2 concentration may generally increase (with an increasing capacity) during charging according to a charging curve form, as CO.sub.2 may be produced during the charging.

(52) FIG. 5a shows a first scenario where the CO.sub.2 concentration C.sub.x before starting charging is below a predetermined CO.sub.2 threshold C.sub.T. Accordingly, the charging control procedure according to case 1 of FIG. 4 is carried out.

(53) FIG. 5b shows a second scenario where the CO.sub.2 concentration C.sub.x before starting charging already exceeds a predetermined CO.sub.2 threshold C.sub.T. Accordingly, the charging control procedure according to case 2 of FIG. 4 is carried out. In other words, during charging the relation ΔX.sub.x/ΔAh.sub.x is determined.

(54) FIG. 5c shows the second scenario of FIG. 5b and a third scenario which generally corresponds to the second scenario of FIG. 5b. In both scenarios, the CO.sub.2 concentration C.sub.x before starting charging already exceeds a predetermined CO.sub.2 threshold C.sub.T. Accordingly, the charging control procedure according to case 2 of FIG. 4 is carried out. During charging the relation ΔC.sub.x/ΔAh.sub.x is determined and compared to a predetermined relation threshold ΔC.sub.T/ΔAh.sub.T (indicated as thin continuous line). Accordingly, any relation ΔC.sub.x/ΔAh.sub.x having a smaller slope than the predetermined relation threshold is allowed. In the present scenario, the battery of the second scenario has a greater relation ΔC.sub.x/ΔAh.sub.x (bold continuous line) and the battery of the third scenario a smaller relation (ΔC.sub.x/ΔAh.sub.x)′ (thin dashed line). However, in both examples the relations ΔC.sub.x/ΔAh.sub.x and (ΔC.sub.x/ΔAh.sub.x)′ do not exceed the predetermined relation threshold ΔC.sub.T/ΔAh.sub.T and hence charging is carried out until the battery is fully charged.

(55) Throughout the disclosure, including the claims, the term “comprising a” should be understood as being synonymous with “comprising at least one” unless otherwise stated. In addition, any range set forth in the description, including the claims should be understood as including its end value(s) unless otherwise stated. Specific values for described elements should be understood to be within accepted manufacturing or industry tolerances known to one of skill in the art, and any use of the terms “substantially” and/or “approximately” and/or “generally” should be understood to mean falling within such accepted tolerances.

(56) Where any standards of national, international, or other standards body are referenced (e.g., ISO, etc.), such references are intended to refer to the standard as defined by the national or international standards body as of the priority date of the present specification. Any subsequent substantive changes to such standards are not intended to modify the scope and/or definitions of the present disclosure and/or claims.

(57) Although the present disclosure herein has been described with, reference to particular embodiments, it is to be understood that these embodiments are merely illustrative of the principles and applications of the present disclosure.

(58) It is intended that the specification and examples be considered as exemplary only, with a true scope of the disclosure being indicated by the following claims.