The need for improved electrical storage devices has led to the extensive study of LiFePO4 as the cathode material for lithium ion batteries. The low-cost, low toxicity and relatively high theoretical specific capacity of these materials has made them especially interesting to researchers seeking to provide practical energy storage solutions. However, these efforts have not proven successful, as the materials have not shown the long life cycles required in practical commercial applications. Specifically, investigations of LiFePO4 as the cathode material for lithium ion batteries have failed to produce a cathode material that maintain a high specific capacity over numerous charge/discharge cycles as is required in commercial applications.
For example, in a recent paper entitled “Preparation of nano-structured LiFePO4/graphene composites by co-precipitation method” Y. Ding, Y. Jiang, F. Xu, J. Yin, H. Ren, Q. Zhuo, Z. Long, P. Zang, Electrochemistry Communications 12 (2010) 10-13 the authors recognize that graphene materials with superior electrical conductivities and high surface area would be advantageous for applications in energy storage. The authors then describe a method for making LiFePO4/graphene composites by a co-precipitation method. Finally, the authors show the results of the material under the charge/discharge conditions typical of commercial applications. Unfortunately, after as few as 80 charge/discharge cycles, the authors report that the cells retain only about 97% of their initial specific capacity. This level of degradation is unacceptable in applications that require hundreds, if not thousands, of charge/discharge cycles.
Another recent paper entitled “A facile method of preparing mixed conducting LiFePO4/graphene composites for lithium-ion batteries” Li Wang, Haibo Wang, Zhihong Liu, Chen Xiao, Shanmu Dong, Pengxian Han, Zongyi Zhang, Xiaoying Zhang, Caifeng Bi, Guanglei Cui, Solid State Ionics 181 (2010) 1685-1689 describes the preparation of a LiFePO4/graphene mixed conducting network through a hydrothermal route followed by heat treatment. This composite showed a 5% drop in the specific capacity after fewer than 60 charge/discharge cycles.
Accordingly, those having ordinary skill in the art recognize a need for LiFePO4/graphene composites that maintain their specific capacity over large numbers of charge/discharge cycles, particularly when used in lithium-ion batteries. The present invention fills that need.
The present invention is thus a cathode comprising nano-structured carbon in electrical communication with LiMPO4, where M is a transition metal ion. The cathode of the present invention has sufficient structural stability to maintain at least 90 percent of the specific capacity of the cathode over 500 charge/discharge cycles. More preferably, the cathode of the present invention has sufficient structural stability to maintain at least 95 percent of the specific capacity of the cathode over 500 charge/discharge cycles. Even more preferably, the cathode of the present invention has sufficient structural stability to maintain at least 98 percent of the specific capacity of the cathode over 500 charge/discharge cycles. Even more preferably, the cathode of the present invention has sufficient structural stability to maintain at least 99 percent of the specific capacity of the cathode over 500 charge/discharge cycles.
The element M in the LiMPO4 is selected from the group consisting of Fe, Mn, Co, Ni and combinations thereof. Preferably, while not meant to be limiting, the M in the LiMPO4 is Fe. The nano-structured carbon comprises graphene, carbon nano-tubes, and combinations thereof. Preferably, while not meant to be limiting, the nano-structured carbon comprises graphene.
The present invention further includes a lithium ion battery having an anode, an electrolyte, and a cathode comprising nano-structured carbon in electrical communication with LiMPO4, where M is a transition metal ion. The cathode of the lithium ion battery of the present invention has sufficient structural stability to maintain at least 90 percent of the specific capacity of the cathode over 500 charge/discharge cycles. More preferably, the cathode of the lithium ion battery of the present invention has sufficient structural stability to maintain at least 95 percent of the specific capacity of the cathode over 500 charge/discharge cycles. Even more preferably, the cathode of the lithium ion battery of the present invention has sufficient structural stability to maintain at least 98 percent of the specific capacity of the cathode over 500 charge/discharge cycles. Even more preferably, the cathode of the lithium ion battery of the present invention has sufficient structural stability to maintain at least 99 percent of the specific capacity of the cathode over 500 charge/discharge cycles.
The element M in the LiMPO4 is selected from the group consisting of Fe, Mn, Co, Ni and combinations thereof. Preferably, while not meant to be limiting, the M in the LiMPO4 is Fe. The nano-structured carbon comprises graphene, carbon nano-tubes, and combinations thereof. Preferably, while not meant to be limiting, the nano-structured carbon comprises graphene.
The following detailed description of the embodiments of the invention will be more readily understood when taken in conjunction with the following drawings, wherein:
a is a graph of the electrochemical cycling at various C rates for anatase TiO2/graphene in experiments demonstrating one embodiment of the present invention.
b is a graph of the electrochemical cycling at various C rates for LiFePO4 in experiments demonstrating one embodiment of the present invention.
c is a graph of the electrochemical cycling at various C rates for LiFePO4-anatase TiO2/graphene full cell in experiments demonstrating one embodiment of the present invention.
d is a graph of the voltage profiles of charge/discharge at various C rates for anatase TiO2/graphene in experiments demonstrating one embodiment of the present invention.
e is a graph of the voltage profiles of charge/discharge at various C rates for LiFePO4 in experiments demonstrating one embodiment of the present invention.
f is a graph of the voltage profiles of charge/discharge at various C rates for LiFePO4-anatase TiO2/graphene full cell in experiments demonstrating one embodiment of the present invention.
a) is a graph showing dq/dv peaks of all electrodes tested at C/5 in experiments demonstrating one embodiment of the present invention.
b) is a Ragone plot comparison of LiFePO4, anatase TiO2/graphene and LiFePO4-anatase TiO2/graphene full cell in experiments demonstrating one embodiment of the present invention.
c) is a graph of the cycling performance of the LiFePO4-anatase TiO2/graphene full cell at 1 Cm rate in experiments demonstrating one embodiment of the present invention.
For the purposes of promoting an understanding of the principles of the invention, reference will now be made to the embodiments illustrated in the drawings and specific language will be used to describe the same. It will nevertheless be understood that no limitations of the inventive scope is thereby intended, as the scope of this invention should be evaluated with reference to the claims appended hereto. Alterations and further modifications in the illustrated devices, and such further applications of the principles of the invention as illustrated herein are contemplated as would normally occur to one skilled in the art to which the invention relates.
A series of experiments where conducted to demonstrate one embodiment of the present invention. Briefly, in these experiments, Li-ion batteries made from a LiFePO4 cathode and an anatase TiO2/graphene composite anode were investigated for potential applications in stationary energy storage. Fine-structured LiFePO4 was synthesized by a novel molten surfactant approach described herein, whereas the anatase TiO2/graphene nanocomposite was prepared via a self-assembly method. The full cell was then operated at 1.6 V, wherein it demonstrated negligible fade in the specific capacity even after more than 700 cycles at measured 1 C rate. The results are the first known in the art to show the cathode maintaining sufficient structural integrity to avoid degradation of the specific capacity.
Fine-structured LiFePO4 was synthesized using LiCOOCH3.2H2O (reagent grade, Sigma), FeC2O4.2H2O (99%, Aldrich), NH4H2PO4 (99.999%, Sigma-Aldrich), oleic acid (FCC, FG, Aldrich) and paraffin wax (ASTM D 87, mp. 53-57° C., Aldrich). NH4H2PO4 was milled with oleic acid for 1 h using high energy mechanical mill (HEMM, SPEX 8000M) in a stainless steel vial and balls. After paraffin wax was added and milled for 30 min, iron oxalate was added and milled for 10 min. Finally, Li acetate was added and milled for 10 min.
The overall molar ratio was Li:Fe:P:oleic acid=1:1:1:1 with paraffin addition twice the weight of oleic acid. The precursor paste was dried in an oven at 110° C. for 30 min followed by heat-treatment in a tube furnace at 500° C. for 8 h under UHP-3% H2/97% Ar gas flow with ramping rate of 5° C./min. After LiFePO4 was synthesized, 10% carbon black by weight was added and milled in planetary mill for 4 h (Retsch 100 CM) at 400 rpm. X-ray diffraction (XRD) pattern (Philips Xpert) was obtained using CuKa (1.54 Å) radiation.
The microstructure of the LiFePO4 was analyzed by a field-emission scanning electron microscope (FESEM, FEI Nova 600). The anatase TiO2/graphene composite (2.5 wt. % graphene) was obtained by self-assembly approach described in D. Wang, D. Choi, J. Li, Z. Yang, Z. Nie, R. Kou, D. Hu, C. Wang, L. V. Saraf, J. Zhang, I. A. Aksay, J. Liu, ACS Nano 3 (4) (2009) 907.
13 mg of the functionalized graphene sheets (FGSs) and 0.6 mL of sodium dodecyl sulfate (SDS) aqueous solution (0.5 mol/L) were then mixed by sonication. 25 mL of TiCl3 (0.12 mol/L) aqueous solution was added into as-prepared SDS-FGS dispersions while stirring, followed by 5 mL of 0.6 M Na2SO4 and 2.5 mL of H2O2 (1 wt. %) dropwise addition. Deionized water was further added under stirring to make total volume of 80 mL which was further stirred in a sealed polypropylene flask at 90° C. for 16 h. The final precipitates were separated by centrifugation and washed with deionized water and ethanol three times. The product was then dried in a vacuum oven at 70° C. overnight and calcined in air at 400° C. for 2 h.
For electrochemical evaluations, the cathode and anode comprised of active material, Super P and poly(vinylidene fluoride) (PVDF) binder were dispersed in N-methylpyrrolidone (NMP) solution in a weight ratio of 80:10:10 for the anatase TiO2/graphene anode and 90:3:7 for LiFePO4/C cathode, respectively. Both cathode and anode slurries were then coated on an Al foil.
The performance of LiFePO4 and anatase TiO2/graphene electrodes were then evaluated, both in half and full 2325 coin cells (National Research Council, Canada) in 1 M LiPF6 in EC/DMC (2:1) (ethyl carbonate/dimethyl carbonate) electrolyte at room temperature, using an Arbin Battery Tester (Model BT-2000, Arbin Instruments, College Station, Tex., USA). The half-cells using Li as anode were tested between 4.3 and 2 V for LiFePO4 and 3-1 V for anatase TiO2/graphene at various C rate currents based on the theoretical capacity of 170 mAh/g for both cathode and anode whereas the full cell was tested in 1 Cm (measured C rate) rate. Due to the initial irreversible loss observed for anatase TiO2/graphene anode, LiFePO4 loading was 2.4 mg/cm2 and 1.1 mg/cm2 for anatase TiO2/graphene in full cells and tested between 2.5 and 1 V where energy and power density was calculated based on the anode weight which is the limiting electrode.
The LiFePO4 synthesized using the molten surfactant approach, as shown in
The synthesized anatase TiO2/graphene, LiFePO4 and full-cell configuration were then tested at various C rates as shown in
As shown in
The rate capacity of the full cell (
Enhancing rate performance is vital not only for achieving higher power but also for minimizing polarization from internal resistance where the latter lead to exothermic irreversible heat generation Qiirr=Iμt+I2Rt (I: current, μ absolute value of electrode polarization, R: Ohmic resistance, t: time) which plays critical role in heat management required for large scale systems. Such heat control can extend the cycle life of Li-ion battery.
a) shows dq/dv peaks of all electrodes tested at C/5 rate where full-cell potential of 1.6 V matches the voltage difference between cathode and anode peaks. Ragone plot of all three cells based on active material weight are compared in
The full-cell power density of 4.5 kW/kg and energy density of 263 Wh/kg based on capacity limiting anatase TiO2/graphene anode weight lies within these two limitations with LiFePO4 cathode limiting the rate, which is opposite to conventional Li-ion batteries using graphite anode.
The cycling performance of the full-cell battery at 1 Cm rate shown in
While the invention has been illustrated and described in detail in the drawings and foregoing description, the same is to be considered as illustrative and not restrictive in character. Only certain embodiments have been shown and described, and all changes, equivalents, and modifications that come within the spirit of the invention described herein are desired to be protected. Any experiments, experimental examples, or experimental results provided herein are intended to be illustrative of the present invention and should not be considered limiting or restrictive with regard to the invention scope. Further, any theory, mechanism of operation, proof, or finding stated herein is meant to further enhance understanding of the present invention and is not intended to limit the present invention in any way to such theory, mechanism of operation, proof, or finding. Thus, the specifics of this description and the attached drawings should not be interpreted to limit the scope of this invention to the specifics thereof. Rather, the scope of this invention should be evaluated with reference to the claims appended hereto. In reading the claims it is intended that when words such as “a”, “an”, “at least one”, and “at least a portion” are used there is no intention to limit the claims to only one item unless specifically stated to the contrary in the claims. Further, when the language “at least a portion” and/or “a portion” is used, the claims may include a portion and/or the entire items unless specifically stated to the contrary. Likewise, where the term “input” or “output” is used in connection with an electric device or fluid processing unit, it should be understood to comprehend singular or plural and one or more signal channels or fluid lines as appropriate in the context. Finally, all publications, patents, and patent applications cited in this specification are herein incorporated by reference to the extent not inconsistent with the present disclosure as if each were specifically and individually indicated to be incorporated by reference and set forth in its entirety herein.
The invention was made with Government support under Contract DE-AC0676RLO 1830, awarded by the U.S. Department of Energy. The Government has certain rights in the invention.