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NASA Technical Reports Server (NTRS) 20000056911: Development of High Conductivity Lithium-Ion Electrolytes for Low Temperature Cell Applications PDF

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Preview NASA Technical Reports Server (NTRS) 20000056911: Development of High Conductivity Lithium-Ion Electrolytes for Low Temperature Cell Applications

,T Development of High Conductivity Lithium-ion Electrolytes for Low Temperature Cell Applications M.C. Smart, B.V. Ratnakumar, S. Surampudi Jet Propulsion Laboratory California Institute of Technology 4800 Oak Grove Drive Pasadena, CA 91109 Introduction and reported earlier.(5) Other groups have also NASA has continued interest in reported electrolytes based on mixtures of developing power sources which are capable of carbonates and acetates.(6) Inthe present study, r operating at low temperatures (-20°C and below) to electrolytes which have been identified to have enable future missions, such as the Mars Rover good low temperature conductivity and stability and Lander. Thus, under aprogram sponsored by were incorporated into lithium-graphite cells for the Mars Exploration Program, we have been evaluation. Using various electrochemical involved in developing Li-ion batteries with methods, including ac impedance and DC improved low temperature performance. To micropolarization techniques, the film formation accomplish this task, the focus of the research has characteristics of graphite electrodes in contact been upon the development of advanced with various electrolyte formulations was electrolyte systems with improved low temperature investigated. properties. This had led to the identification of a carbonate-based electrolyte, consisting of 1.0 M LiPF6 in EC + DEC + DMC (33:33:34), which has Experimental been shown to have excellent performance at The specific conductivity of a number of -20°C inLi-ion AA-size prototype cells.(1,2) Other electrolyte solutions was measured over the groups are also actively engaged in developing temperature range of -60°C to 25°C using a electrolytes which can result in improved low conductivity cell which consists of two platinized temperature performance of Li-ion cells, including platinum electrodes which are immobilized in a Polystor (3), Yardney, and Covalent. (4) glassapparatus andseparated by afixed distance. In addition to developing cells capable of The cellconstantofthe apparatus wasdetermined operation at -20°C, there is continued interest in bycomparing the resistivityofa 0.1M KCI solution systems which can successfully operate at even with the value reported in the literature. The lower temperatures (< -30oC) and at high temperature wascontrolled in these experiments discharge rates (> C/2). Thus, we are currently by utilizing a Tenney environmental low focusing upon developing advanced electrolytes temperature chamber (+/- 1°C). which are highly conductive at low temperatures Half-cellstudies were carded out using O- and will result in cells capable of operation at ring-sealed, glasscellswhichcontained jelly rollsof -40°C. One approach to improve the low graphite (KS44) and LiCoO2(Alfa) electrodes with temperature conductivity of ethylene carbonate- porous polypropylene separator (Celgard 2500) based electrolytes involves adding co-solvents and Lireference electrodes. Allelectrolyte were of which will decrease the viscosity and extend the battery-grade purity. Electrochemical liquid range. Candidate solvent additives include measurements were made using an EG&G formates, acetates, cyclic and aliphatic ethers, Potentiostat/Galvanostat (and Solartron 1255 lactones, as well as other carbonates. Using this Frequency Response Analyzer for impedance approach, we have prepared a number of measurements) interfaced with an IBM PC, using electrolytes which contain methyl formate (MF), Softcorr 352 (and M388 for impedance) software. methyl acetate (MA), ethyl acetate (EA), ethyl Cycling Data were collected using an Arbin battery proprionate (EP), and 1,2-dimethoxyethane test system. (DME), some of which have been characterized ResultsandDiscussion solution is a good candidate for ultra-low ConductivityMeasurements temperature applications, due to the fact that the conductivity was observed to have greater than 1 A numberof EC-basedelectrolytes mS/cm at -60°C. We also initiated investigations containing lowviscosityaliphatic and cyclic edgers into the effect of mixed salt solutions upon the low have been prepared and the conductivity temperature conductivity and compared 1.0M measured over a temperature range of -60°C to LiPFe solutions with 0.50M LiPF6 + 0.50M LiAsF6 25°C. The electrolytes assessed consisted of solutions, although little benefit was observed baseline formulations, 1.0M LiPF8 EC + DEC + when the conductivity was measured at low DMC (1:1:1), to which lowviscositysolvents were temperatures. added, including: methyl acetate, ethyl acetate, ethyl butyrate, ethyl propionate, and methyl Lithium-Graphite Half-Cells formate. Of the electrolytes investigated, the A number of lithium-graphite cells have formulations that displayed the highest been fabricated to study the effect of different conductivity at low temperatures were ones with electrolytes upon the film formation characteristics lowermolecularweight acetates and displayed the on graphite electrolytes and the irreversible and following trend: > 1.0M LiPF6EC + DEC + DMC + reversible capacities of graphite electrodes. The MA (1:1:1:1) > 1.0M LiPF6 EC + DEC + DMC + EA lithium-graphite half-cells can serve as an additional (1:1:1:1) > 1.0M LiPF8 EC + DEC + DMC + EP screening test to identify the compatibility and (1:1:1:1). The conductivity values for these stability of candidate electrolytes with solutionsisshown inFig. 1. carbonaceous electrodes. The electrolytes selected in the first group of cells include: 0.75 M LiPFsEC + DEC + DMC (1:1:1), 0.75 M LiPF6EC + 1oo DEC (30:70), 0.75 M LiPF6 EC + DMC (30:70), ,oI _MEA,A._.m.e'_l,he___K._:eettamme'e . 0.75 M LiPF6EC + DEC +DMC + MA (1:1:1:1), and 0.75 M LiPF6EC + DEC + DMC + EA (1:1:1:1), and 0.75 M LiPF6 EC+ DEC+ DMC + DME (1:1:1:1). As shown in Fig. 3., electrolytes based J upon the addition of aliphatic esters, such as methyl acetate and ethyl acetate, were observed ,,L 1.0M IIPF6 EC+DEC+DMC+EB (1:1:1:1 to have small irreversible capacities (5th cycle). •.e. 1,0M LiPF6 EC+DEC+DMC (1:1:1) This suggests that desirable protective interfacial oo60 -40 2O 40 films are formed on the electrode surface with these electrolytes. The exclusively carbonate- based electrolytes showed similar behavior, with Fig.1. Theeffectoflowviscosityadditivesuponthelow higher DMC content resulting in more protective temperature conductivity of EC-based electrolyte solutions. surface films. Incontrast, the electrolyte with DME showed the highest irreversible and lowest reversible capacity, suggesting that the solvent is In addition to investigating low viscosity more reactive with the lithiated carbon and/or the additives, we have initiated research into the effect electrolyte salt and forms less desirable surface of salt type and salt concentration upon the films. Overall, the reversible capacities obtained conductivity of electrolyte solutions at low for the lithium-graphite cells studied, as shown in temperature. It was determined that solutions Fig. 4, were somewhat lower than that observed in consisting of 0.75M LiPFeEC + DEC + DMC (1:1:1) experimental and prototype LiCoO2-graphite cells showed an improvement in conductivity at which can be attributed to the selected charge temperatures below -20°C compared with 1.0M voltage (0.025 V vs Li/Li+) and the cell design LiPF6 EC + DEC + DMC (1:1:1). In addition, the which has excess electrolyte. Some correlation electrolyte formulation 0.SM LiPF6 EC + DEC + between the extent of irreversible capacity lost in DMC + MA (1:1:1:1) displayed better conductivity the first cycle and how quickly the cell reflects at low temperatures below -40°C compared with potentials indicative of the lithium intercalation the 1.0M EC + DEC + DMC + MA (1:1:1:1) reaction (>150 mV vs. Li/Li*) was observed as solution, with little loss in the room temperature shown in Fig. 3. values (> 10 mS/cm @ 23oc). This electrolyte Electrolyte Formulation R_C,_ _'_ _,C_ !_C=p Electrolytes incorporating acetate additives, such I==¢y¢ 1=1¢yc. !sin C_. !m Cy{ 075ML*PF I EC.0MC*OEC(1 1I) 227.2 106.0 240.4 12711 as MA or EA show similarbehavior to the ternary 0.75M _ptr. EC. OMC (3070) 302.0 94.3 312.6 122.9 carbonate mixture,as shown in Fig. 6. Whereas, the electrolyte possessing DME displayed the 07SM L_F eEC •DEC (30:70) 268.1 1068 27S.4 136.9' largest film resistance consistent with the high 075M LiPF6 EC *OMC _OEC .MA {1;1:1:1) 201.5 _+9 23_.5 S6.g irreversiblecapacityobserved withthiscell. The ac 07SMLiPF4 EC+OMC*0EC+EA (I 11,1) 210.4 49.9 214.2 68+5/ ; impedance measurements were repeated after the 07SM bPF4 EC+0MC -OEC .OME (111:1) 147.5 138,2 IM.3 192-_ cells had been subjected to a number of cycles 4_ and aself-discharge study, asshown in Figs.7 -8. Fig.2. Reversible and irreversible capacities of lithium- In the case of the solely carbonate-based graphite cells possessing different EC-based electrolytes, little variation was observed in the electrolyte formulations. Nyquist plots generated. However, a dramatic increase in the overall cell resistance and the charge transferresistance wasobserved withcells 410.75M LJPF6 EC.¢.OEC+It_MC (1:1:1} ! possessing electrolytes with MA or EA, as shown .0.75M LiPF6 EC+OMC (30:70) e.le in Fig. 7. These results suggest that these e0.75M LJPI=6 EC+OEC (30.70) i g! II0,7SM LiPF6 EC.,.OEC+-DMC+_ (I:1:1:1 ) i electrolytes continue to react with the lithiated • 0.75M I.JPF6 EC+OEC+-O_+E.4 (1:1:1:1} "0.75M LIPF6 EC+DEC+OMC+OME (1:1:1) i carbon electrode and/or other in situ generated ! byproducts after the initial "formation" cycles. The impact of temperature upon the film resistance was also investigated for all of the samples and displayed similarbehavior to thatshown inFig.9. (l,04 e.ooe I,I0O 4.|44 4.)e* 0.400 o+iee Cho+ge Cap=cRy (Ah) O+7 Fig. 3 First lithiumintercalation cycle of lithium-graphite 0.41 cells possessing different EC-based electrolyte ,0.75M LIPF6 EC +DEC (30:70) formulations. 0.$ •0.75M L;PF6 EC+OMC÷DEC (1:1:1) 0.4 10.TSM UPFI; EC +OMC (30:70) !.40 _1, 0.3 o.eo 0.2 oo..Tlet I 0,I e+go 0.0 oseJ 6 5 4 I 3 2 0 0.1 0.2 0.3 0.4 O.S 0.1 0.7 0.40 Z' (Ohms) ] Fig. 5. AC impedance (Nyquist) plots of lithium-graphite cells possessing carbonate-based electrolytes after formation cycles. e.ee ILOO O,Ol O.ll 0.11 l+:lo 0.21 11,34 1,2 F-mj.4. Reversible capacity (Ah/g) of lithium-graphite cells possessing different EC-based electrolyte ;1.0.75M LJPF6 EC+DMC+OEC (1:1:1) formulations (1= EC+ DEC + DMC, 2=EC+ DMC, 3=EC + _' 1.o I-0.75M LJPF6 EC+OMC +DEC,.MA (1:1:1:1) DEC,4= EC+DEC + DMC+ MA, 5= EC+ DEC + DMC + ,_ o, -j,o_mupF+scoo,c.oec._A (+:1:1:I> EA,6=EC+ DEC + DME). [,0.75M UPF6 EC +DMC +OEC +OM[ (1:1:1:1) _1 0.1 AC Impedance Measurements 0.4 - In addition to studying the o../...ii .II ,iiI,i,n.l ,Iii ii iiiIx,.,, charge/discharge characteristics of these cells, a.c. impedance was used to probe the interfacial 0.0 ___ __ properties of the anode passivating films on the • o.:, o+, o.i o+e I +._, Z" (Ohm=) graphite electrodes. As shown in Fig. 5, the Fig.6. AC impedance (Nyquist) plots of lithium-graphite carbonate based electrolytes with high DMC cells possessing carbonate-based electrolytes with content result in cells with lower charge transfer different low viscosity additives, MA, EA, and DME, resistance compared with DEC rich electrolytes. after formation cycles. Fig. 10 and 11, the cells that had electrolytes 07O which resulted in higher irreversible capacity • I 07_Mt.JPF41 EC*OEC*I_t*4C(I;tl) losses, such as DME and DEC, displayed the OeO a 075ML_'6 ECoOMC{3O:?0) • :1 07_MUPF6 EC*DEC(30:70) lowest polarization resistance. The improved 0SO _! 311 kinetics of Li intercalation observed with these • A = I_lial IIA_lsummil_l 040 cells may be due to the production of porous, non- v_ 030 : 8 • Aft,, Cyclk_ protective films which facilitate Li ion diffusion _o20 and/or charge transfer. In contrast, the cells containing electrolytes with MA or EA produced o=°'° films which resulted in high polarization resistance of the electrode. This is undesirable for low o(x} 010 020 03o 040 0S0 0_0 070 temperature applications where the effect is Z' (Ohms) magnified and high rates become difficult to Fig. 7. AC impedance (Nyquist) plots of lithium-graphite sustain. •cells possessing carbonate-based electrolytes before The limiting current densities were also and after cycling. F determined for the lithium deintercalation process from the graphite electrodes by conducting Tafel 1zoo polarization measurements to evaluate the rate capability of the electrodes in contact with the 10,00 • 07SMI.JPFe EC*OEC_DMC+MA(t:I:t:t) • 07_3MI._FO EC_DEC÷OMC+EA(tt:I:I) various electrolytes. The results obtained correlate well with the DC micro-polarization measurements in that the cells possessing high _ 6_OO polarization resistance, i.e. with electrolytes 4oo After Cycling Ilnitisl Measurement possessing MA or EA, have lower diffusion limiting currents (measured at an overpotential of 250 mV). 0`00 200 dl00 0`00 100 10.00 1100 Z' (Ohms) Fig.8. AC impedance (Nyquist) plots oflithium-graphite cells possessing carbonate-based electrolytes with different lowviscosity additives, MA and EA, before and after cycling. 22.$0I 075 M I.JPF6 EC +DEC _.DMC ÷MA(It1:l:f) ic.u¢ T..*._e T.,. |e.1_¢ Tw..llJ T_*.|A _ 1s.oo Elect_ryte "i'yl_ 1 11.._ Fig. 10 Linear polarization resistance calculated from IX; micropolarJzation plots of graphite electrodes with different electrolytes atroom temperature. 5'C &4&li&d6=_a=&ll 6&_ ,_1,._.. ,,-- o_ ooIoXT"""-'_- =e o.oo 2_N s.oo 7.so to.oo 12.50 _.¢00 tT.IW ZEo_ 21.54 _._ 11• l¢. c1[¢.OM¢•F._ Z"(Ohms) Fig. 9. AC impedance (Nyquist) plots of a lithium- graphite cell possessing EC+DEC+DMC+MA electrolyte at various temperatures. ii , DC Micropolarization Measurements DC micropoladzation techniques were also 'IM! employed to study the charge transfer behavior of the passivating films on the graphite electrodes at ElectmMe Type various temperatures. The polarization resistance Fig 11 Polarization resistance ofgraphite electrodes in of the electrodes was calculated from the slopes of contact with EC-based electrolytes ofdifferent types as the linear plots generated under potentiodynamic a function oftemperature conditions at scan rates of 0.02 mV/s. As shown in I Low Temperature Discharge Capacity these highly conducting electrolytes display low After performing the electrochemical irreversible capacity losses during the formation measurements described above, the discharge cycles, such as with MA and EA, AC impedance capacities were determined for the various cells and DC micro polarization methods have shown under similarconditions. As shown inFig. 12,'the that these cells have high polarization and charge delivered capacities at -20°C (25 mA current to 1.5 transfer resistance. Thus, the benefits of the V cut-off vs. Li/Li+)correlate well with the results highly conducting medium is offset by the poor Li÷ obtained with the DC micropolarization intercalation-deintercalation kinetics of the techniques. Due to the high polarization graphite electrodes produced by the nature of the resistance observed at graphite electrodes in interfacial films. contact with MA or EA-containing electrolytes the delivered capacities were lower than that of the References ternary carbonate mixture or the DME-containing electrolyte. Although differences are anticipated 1)M.C. Smart, C.-K. Huang, B.V. Ratnakumar, and when these electrolytes are evaluated in S. Surampudi, Proceedings of the Intersocity r experimental or prototype LiCoO2-carbon cells due Energy Conversion Engineering Conference to cell design, pack tightness, and electrolyte (IECEC), Honalulu, Hawaii, July, 1997. volume, the observed trends should be consistent. 2) M.C. Smart, B.V. Ratnakumar, C.-K. Huang, and S. Surampudi, SAE Aerospace Power Systems IJDO Conference Proceedings P-322, 1998, p. 7-14. 160 4b 3b 2b Ib '''Oy 3) Juzkow, M.W., Proceedings 14th International 20 Primary and Secondary Battery Technology and t.O0 Applications Seminar, 1997. O.B0 060 4) Ein-Eli, Y., et al, J. Electrochem.Soc., 1996, _ 3" ,_ 142, L273. 040 - ........... :.... _h ,j za_ ,,,, 4, 0.20 ,_. _..* ..___, ..... ooo m 5) Smart, M.C.; Huang, C.-K.; Ratnakumar, B.V.; o.oo 0.050 0,100 0.150 0.200 0.250 0.30q and Surampudi, S., 1996, Proceedings, 37th c._,:_ IAh) Power Sources Conference, pp. 239-242. Fig. 12 Discharge curves of graphite electrodes in different electrolytes (I=EC+DEC+DMC, 2=EC+DEC +DMC+DME, 3=EC+DEC+DMC+EA, and 4=EC+DEC+ 6) Ohta, A.H., Koshina, H.; Okuno,, and H. Mural, J.Power Sources, 1995, 54, 6. DMC+MA)at different temperatures (A=25°C,B=-20°C). Acknowledgment Conclusions The workdescribed here wascarded out at A number of EC-based electrolytes with the Jet Propulsion Laboratory, California Institute improved low temperature conductivity have been of Technology, for the Mars Exploration Program and a DARPA TRP program under contract with identified. These electrolytes are based on ternary mixtures of organic carbonates to which solvents the National Aeronautics and Space Administration (NASA). possessing low viscosity and low melting points are added, such as, MA, EA, and DME. The compatibility of these electrolytes with graphite anode materials was assessed in lithium-graphite half-cells using various electrochemical techniques. Although some cells incorporating

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