Although the idea of a lithium–air battery was around long before 1996, the risk-to-benefit ratio was perceived as too high to pursue. Indeed, both the negative (lithium metal) and the positive (air or oxygen) electrodes are the reasons why, respectively, rechargeable lithium-metal batteries failed to reach the market in the 1970s (the lithium-ion battery in a mobile device uses a LiC6-graphite compound on the negative electrode, not a lithium metal). Nevertheless, due to a perceived lack of other alternatives to high specific energy rechargeable batteries, and due to some initially promising results from academic labs, both the number of patents and of free-domain publications related to lithium–oxygen (including Li–air) batteries began growing exponentially in 2006. However, the technical difficulties facing such batteries, especially recharging times, nitrogen and water sensitivity, and the intrinsic poor conductivity of the charged Li2O2 species are major challenges.
In general lithium ions move between the anode and the cathode across the electrolyte. Under discharge, electrons follow the external circuit to do electric work and the lithium ions migrate to the cathode. During charge the lithium metal plates onto the anode, freeing O2 at the cathode. Both non-aqueous (with Li2O2 or LiO2 as the discharge products) and aqueous (LiOH as the discharge product) Li-O2 batteries have been considered. The aqueous battery requires a protective layer on the negative electrode to keep the Li metal from reacting with water.
Lithium metal is the typical anode choice. At the anode, electrochemical potential forces the lithium metal to release electrons via oxidation (without involving the cathodic oxygen). The half-reaction is:
Li ⇌ Li+ + e−
Lithium has high specific capacity (3,840 mAh/g) compared with other metal–air battery materials (820 mAh/g for zinc, 2,965 mAh/g for aluminium). Several issues affect such cells.
The main challenge in anode development is preventing the anode from reacting with the electrolyte. Alternatives include new electrolyte materials or redesigning the interface between electrolyte and anode. Lithium anodes risk dendritic lithium deposits, decreasing energy capacity or triggering a short circuit.
The effects of pore size and pore size distribution remain poorly understood.
Upon charging/discharging in aprotic cells, layers of lithium salts precipitate onto the anode, eventually covering it and creating a barrier between the lithium and electrolyte. This barrier initially prevents corrosion, but eventually inhibits the reaction kinetics between the anode and the electrolyte. This chemical change of the solid–electrolyte interface (SEI) results in varying chemical composition across the surface, causing the current to vary accordingly. The uneven current distribution furthers branching dendrite growth and typically leads to a short circuit between the anode and cathode.
In aqueous cells problems at the SEI stem from the high reactivity of lithium metal with water.
At the cathode during charge, oxygen donates electrons to the lithium via reduction. Mesoporous carbon has been used as a cathode substrate with metal catalysts that enhance reduction kinetics and increase the cathode's specific capacity. Manganese, cobalt, ruthenium, platinum, silver, or a mixture of cobalt and manganese are potential metal catalysts. Under some circumstances manganese-catalyzed cathodes performed best, with a specific capacity of 3,137 mA·H/g carbon and cobalt-catalyzed cathodes performed second best, with a specific capacity of 2414 mA·H/g carbon. Based on the first pore-scale modeling of lithium–air batteries, the micro-structure of the cathode significantly affects battery capacity in both non-pore-blocking and pore-blocking regimes.
Most Li–air battery limits are at the cathode, which is also the source of its potential advantages.
Atmospheric oxygen must be present at the cathode, but contaminants such as water vapor can damage it.
Incomplete discharge due to blockage of the porous carbon cathode with discharge products such as lithium peroxide (in aprotic designs) is the most serious.
Catalysts have shown promise in creating preferential nucleation of Li2O2 over Li2O, which is irreversible with respect to lithium.
Li–air performance is limited by the efficiency of the reaction at the cathode, because most of the voltage drop occurs there. Multiple chemistries have been assessed, distinguished by their electrolyte. This discussion focuses on aprotic and aqueous electrolytes as solid-state electrochemistry is poorly understood.
In a cell with an aprotic electrolyte lithium oxides are produced through reduction at the cathode:
Li+ + e− +O2 + * → LiO2*
Li+ + e− +LiO2* →Li2O2*
where "*" denotes a surface site on Li2O2 where growth proceeds, which is essentially a neutral Li vacancy in the Li2O2 surface.
Lithium oxides are insoluble in aprotic electrolytes, which leads to cathode clogging.
Efforts in Li–air batteries have focused on four electrolytes: aqueous acidic, aqueous alkaline, non-aqueous protic, and aprotic.
In a cell with an aqueous electrolyte the reduction at the cathode can also produce lithium hydroxide:
A conjugate base is involved in the reaction. The theoretical maximal Li–air cell specific energy and energy density are 1,400 W·h/kg and 1,680 W·h/L, respectively.
Water molecules are involved in the redox reactions at the air cathode. The theoretical maximal Li–air cell specific energy and energy density are 1,300 W·h/kg and 1,520 W·h/L, respectively.
New cathode materials must account for the accommodation of substantial amounts of LiO2, Li2O2 and/or LiOH without causing the cathode pores to block and employ suitable catalysts to make the electrochemical reactions energetically practical.
Although most studies agree that Li2O2 is the final discharge product of non-aqueous Li-O2 batteries, considerable evidence that its formation does not proceed as a direct 2-electron electro-reduction to peroxide O2−2 (which is the common pathway for O2 reduction in water on carbon) but rather via a one–electron reduction to superoxide O−2, followed by its disproportionation:
Pt/C seems to be the best electrocatalyst for O2 evolution and Au/C for O2 reduction when Li2O2 is the product. Nevertheless, "the performance of rechargeable lithium–air batteries with non-aqueous electrolytes is limited by the reactions on the oxygen electrode, especially by O2 evolution. Conventional porous carbon air electrodes are unable to provide mAh/g and mAh/cm2 capacities and discharge rates at the magnitudes required for really high energy density batteries for EV applications." The capacity (in mAh/cm2) and the cycle life of non-aqueous Li-O2 batteries is limited by the deposition of insoluble and poorly electronically conducting LiOx phases upon discharge. (Li3O4 is predicted to have a better Li+ conductivity than the LiO2 and Li2O2 phases). This makes the practical specific energy of Li-O2 batteries significantly smaller than the reagent-level calculation predicts. It seems that these parameters have reached their limits, and further improvement is expected only from alternative methods.
The aqueous–aprotic or mixed Li–air battery design attempts to unite advantages of the aprotic and aqueous battery designs. The common feature of hybrid designs is a two-part (one part aqueous and one part aprotic) electrolyte connected by a lithium-conducting membrane. The anode abuts the aprotic side while the cathode is in contact with the aqueous side. A lithium-conducting ceramic is typically employed as the membrane joining the two electrolytes.
The use of a solid electrolyte (see Fig. 3) is one such alternative approaches that allows for a combination of a lithium metal anode with an aqueous cathode. Ceramic solid electrolytes (CSEs) of the NASICON family (e.g., Li1−xAxM2−x(PO4)3 with A ∈ [Al, Sc, Y] and M ∈ [Ti, Ge]) has been studied. Compatible with water at alkaline pH and having a large electrochemical window (see Figs. 3,4), their low Li+ ion conductivity near room temperature (< 0.005 S/cm, >85 Ω cm2) makes them unsuitable for automotive and stationary energy storage applications that demand low cost (i.e., operating current densities over 100 mA/cm2). Further, both Ti and Ge are reduced by metallic Li, and an intermediate layer between the ceramic electrode and the negative electrode is required. In contrast, solid polymer electrolytes (SPEs) can provide a higher conductivity at the expense of a faster crossover of water and of other small molecules that are reactive toward metallic Li. Among the more exotic membranes considered for Li-O2 batteries is single-crystal silicon.
As of 2013, many challenges confronted designers. Generally, they fall into either surface passivation or pore clogging, which are confronted below.
Long-term battery operation requires chemical stability of all cell components. Current cell designs show poor resistance to oxidation by reaction products and intermediates. Many aqueous electrolytes are volatile and can evaporate over time. Stability is hampered in general by parasitic chemical reactions, for instance those involving reactive oxygen.
Most Li–air battery limits are at the cathode, which is also the source of its potential advantages. Most prominent is incomplete discharge due to blockage of the porous carbon cathode with discharge products such as lithium peroxide (in aprotic designs). Several modes of precipitates were modeled. A parameter, Da, was defined to measure the variations of temperature, species concentration and potentials.
In addition to the blockage of electron flow via the formation of an insulating product, cycling Li-air batteries results in the clogging of pores meant for oxygen diffusion. The chemistry of a standard Li-air battery will inevitably produce lithium peroxide, but the effects of pore size and pore size distribution remain poorly understood. However, the modulation of pore size has resulted in drastic effects on cell capacity.
Catalysts have shown promise in creating preferential nucleation of Li2O2 over Li2O, which is irreversible with respect to lithium.
Atmospheric oxygen must be present at the cathode, but contaminants such as water vapor can damage it.
Significant drops in cell capacity with increasing discharge rates are another issue. The decrease in cell capacity is attributed to kinetic charge transfer limits. Since the anodic reaction occurs very quickly, the charge transfer limits are thought to occur at the cathode.
The research towards deciphering the impacts of pore size and distribution remain ongoing, but some conclusions have been made, especially regarding sets of pores smaller than 100nm. In cells using cathodes made from Super P and Ketjen Black, for example, conclusions have been made linking to discharge being stopped in Li-air batteries due to the loss of surface area near the air inlet. As the battery is used, Lithium peroxide deposits along the walls of pores, gradually sealing them.
The reason for this focus on pores smaller than 100nm is because smaller pores seem to be preferable in spite of their small size being easy to seal up with discharge products. To avoid the challenges in pore clogging, select amounts of large cracks or cavities are recommended in order to ensure that airflow remains in the battery even after a lot of lithium peroxide deposition into pores.
Li–air cells are of interest for electric vehicles, because of their high theoretical specific and volumetric energy density, comparable to petrol. Electric motors provide high efficiency (95% compared to 35% for an internal combustion engine). Li–air cells could offer range equivalent to today's vehicles with a battery pack one-third the size of standard fuel tanks assuming the balance of plant required to maintain the battery was of negligible mass or volume.
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