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Special Report                                                                 Special Report



          relatively cheaper to procure; and  is piped into the suspension. After    Compared with solid LiPF , the
                                                                                                     6
 Liquid electrolyte  solvents &  total cost  cost of materials    PCl  is relatively less hazardous   some time, LiPF  can be generated.   yield of liquid LiPF  can reach
                                                         6
             5
                                                                                                6
 LiPF salt  other: 9 %  and is a crystalline solid at normal   Although the reaction is also a solid-  more than 99%; and
 6
          conditions.                      gas reaction, the resulted product    The investment per tonne of liquid
 production: 19 %
 agitation  other : 5 %                    LiPF  can dissolve in the organic   LiPF6 is lower than that  of solid
 housing : 9 %                                 6
 electrolyte: 10 %  After more than 20 years of contin-  solvent, making the reaction inter-  products.
 anode: 15 %  uous improvement  and development,   face continuously  updated, so  that
 solvents  electrolyte  separator: 17 %
 material: 72 %  a process using PC1 , LiCl and anhy-  the reaction can go on.  Global market
                        5
 + LiPF 6  drous  hydrofl uoric  acid  (HF)  as  raw    The unreacted LiF and impurities   The global LIPF   market reached
                                                                                           6
 solvents  LiPF salt  cathode: 44 %  materials to prepare LiPF  was indus-  are insoluble in the solvent and can  approximately  50-kt in 2021 and is
                            6
 6
       trialized.                          be easily separated from the LiPF   expected to grow at a CAGR of 9.58%
 DMC EMC  DEC  EC  LiPF (s)                                            6
 6
 Fig. 2: Cost overview of a LIB cell       solution.                      to reach a size of 200-kt till 2035(6).  In
 CO+O 2  PCl (s)  given as: LiC  + CoO   ⇄ C  +   PF  is obtained by fl uorinating PCl     The solvent is then vaporized  and  2021, North America accounted for ap-
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            5
 6
 2
 6
 5
 LiCoO  in HF solvent,  and the thus-released   recovered using appropriate methods,  proximately 32% of total demand.
 CO 2  2  PF  gas was pumped into an anhydrous   so high-purity LiPF  can be
         5
                                                              6
 methanol  ethylene oxide  LiF (s)  continuous removal of the  Manufacture of LiPF 6  HF solution with LiF to produce LiPF .   obtained.   The automotive  industry accounts
                                     6
 electrolyte  In the 1950s,  American  scientist   The such-prepared LiPF  always con-  for more than 42% of the market share,
                           6
 Fig. 1: Liquid electrolyte production(2)  J.H. Simmons  proposed a  preparation   tains a trace amount of free HF, which   As per techno-economic  analysis,  but industrial energy storage is also a
 method for LiPF . He let phosphorous   requires complex purifi cation to ensure  in a facility with a capacity of making  prominent consumer.
 6
 pentafl uoride  (PF )  directly react with   the cyclability and safety of the LIBs.  10,000-tpa of  LiPF  the  cost  of pro-
                                                         6
 5
 lithium fl uoride (LiF) in a nickel con-  This leads to an increase in production  duction is around $20 per kg of LiPF ,   China is the leading  producer of
                                                                       6
 tainer to get LiPF : LiF + PF  = LiPF .  costs.   energy consumption is around 30 GWh  LIPF . According to Do-Fluoride New
                                                                               6
 5
 6
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                                         per  year, and  the  emission  of green-  Materials, a leading producer, there are
 The reaction  went on under high   The method has the following dis-  house gases in CO -equivalent gases is  currently 48 LIPF  producers in China.
                                                        2
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 temperature  and pressure and did not   advantages:   around 80 tonnes per day(5).
 use any solvents. Its main drawback is     It uses a large amount of highly cor-  Currently, Do-Fluoride and Guang-
 that it has a low yield and is diffi cult to   rosive  anhydrous HF,  so requires   Compared with solid LiPF , the  zhou Tinci  Materials Technology  Co.,
                                                                   6
 achieve mass production. The reaction   the equipment to be highly resistant  advantages of liquid LiPF  devices are  Ltd. dominate the markets; other rele-
                                                              6
 is a gas-solid reaction.  The generated   to corrosion;  mainly refl ected in two aspects:   vant enterprises are  Tianji  Co., Ltd.,
 LiPF  can completely  cover LiF, pre-    Requires cryogenic conditions;    In terms of product quality – after  Yongtai  Technology,  Yan’an  Bikang,
 6
 venting the reaction from going on.    The reaction has multiple steps and   liquefaction,  the  uniformity of  the  Shenghua New Materials,  Shenzhen
          is a long process.               product is better, which is more  Xinxing, and Morita New Energy
 Production of LiPF  for LIB elec-         conducive to the stability of  cus-  Materials (3-ktpa capacity).
 6
 trolytes is constrained by the required   While HF is necessary for the pro-  tomer product quality and improves
 purity (>99.9%) and the type of impuri-  duction of LiPF  by any method, it has   the consistency of cell performance;  According to Qidian Lithium, China’s
                   6
 Fig. 3: Charging and discharging of a LIB(4)   ties present in the fi nal product. Trace   also been used as a solvent. But due to
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 compositions either during calendar  year is generally observed in popular   amounts of impurities such as moisture,   its hazardous nature, alternate solvents   Table 1: Breakdown of LiPF  manufacturing costs
 aging or cycling in LIBs, along with  top-brand mobile phones.  metal, and free HF are detrimental for   have been also used including sulphur   Process 1   Process 2   Process 3
 formation of deleterious components   the life, quality, and safety of the LIB.   dioxide (SO ) and organic solvents like   (HF)  (SO2)  (ACN)
                2
 (e.g.,  hydrogen  fl uoride  (HF))  par-  The  degradation  of electrolyte   Thus, the raw materials,  processing   acetonitrile, diethyl ether and ethyl car-  Manufacturing cost   $/kg LiPF 6  29  26  20
 ticularly at elevated  temperatures.  materials is one of major aging process   equipment,  and production metho-  bonate.  Sale Price   $/kg LiPF  31  28  22
 Consequently, the service lifetime of  responsible for capacity  and power   dology are selected with great caution   Purchased equipment  $  6  25,931,100 20,808,900 26,925,300
 the state-of-the-art LIBs is usually  fading of LIBs, particularly at elevated   to avoid any possible contamination.   A broad outline of the new process
 less than 15 years, which is required  temperatures(3).   Some of the key considerations in the   is as follows:  Materials purchased   $/year  90,800,000 71,322,300 72,449,700
 by EVs to compete with conventional   selection of starting materials are:    LiF is fi rst suspended in an organic   Material recycling   $/year  98,606,500 99,453,900 47,618,000
 fossil fuel vehicles in terms of cost. In    The positive (cathode) electrode     LiF and PF  are expensive starting   solvent consisting of EC (ethylene   Operating labor   $/year  1,974,100  1,969,000  1,969,000
 5
 fact, the limited lifetimes of LIBs are   half-reaction: CoO  + Li  + e-  ⇄   materials;  carbonate),  DEC (diethyl carbo-  Electricity   $/year  2,045,500  1,419,000  2,349,600
 2
 +
 very intuitively sensed by everyone   LiCoO 2    PF  is a highly toxic gas, making it   nate) and DME (ethylene glycol
 5
 from rapid capacity fading of LIBs    The negative  (anode) electrode   diffi cult and hazardous to store;  dimethyl  ether)  to form a uniform   Water   $/year  469  221  134
 used in portable electronics, wherein   half-reaction: LiC  ⇄ C  + Li  + e-    Lithium chloride (LiCl) and phos-  suspension.  Natural gas   $/year  21,200  11,700  9,500
 6
 +
 6
 at  least  20%  capacity fading  in  one    The overall reaction thus  can  be   phorus  pentachloride (PCl ) are     At the appropriate temperature, PF    For 10,000-tpa of LiPF  Source: Reference 5
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 166  Chemical Weekly  January 30, 2024  Chemical Weekly  January 30, 2024                             167
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