fast capacity fade and relatively low cycling efficiency are the main problems encountered when designing lithium - sulphur batteries . irreversible transfer of sulphur from the positive electrode ( cathode ) to the surface of the negative electrode ( anode ) and its accumulation there in the form of lithium sulphide or disulphide is one of the major reasons for capacity fade during cycling of lithium - sulphur cells . the low cycling efficiency of lithium - sulphur batteries is caused by the reversible transfer of sulphur in the middle of the charge and discharge process . this transfer results in what is known as the sulphide cycle , i . e . the energy transfer inside the battery ( in its internal circuit ). elemental sulphur and the end products of sulphur reduction ( lithium sulphide or disulphide ) are known to be poorly soluble in most organic solvents . in contrast , lithium polysulphides ( intermediate forms produced during the reduction of elemental sulphur or during oxidation of lithium sulphide and disulphide ) are well soluble in many organic solvents . the rate of sulphur transfer between the positive and negative electrodes of lithium - sulphur batteries is determined by the form of sulphur present in the electrolyte solution . the form of sulphur and sulphur - lithium compounds present in the electrolytes of lithium - sulphur batteries depends on the electrolyte system composition and the properties thereof . in particular , it depends on the polarity and donor properties of the solvents used and by the concentration of the supporting salts . lithium polysulphides may be present in electrolyte systems in three forms : molecular , mono - anionic , and di - anionic . hence sulphur in the electrolyte can be transferred either in molecular ( neutral ) or in ionic ( anionic ) form . the diffusion of elemental sulphur and non - dissociated lithium polysulphides dissolved in the electrolyte contributes to the molecular transfer of sulphur . the diffusion and electromigration of the mono - and di - anions of polysulphides , as well as sulphur anion - radicals , contributes to the ionic form of sulphur transfer . the existence of two mechanisms increases the overall sulphur transfer . the sulphur transfer will be higher in the case of a diffusion - migration process as compared to a pure diffusion mechanism . as a result , the rate of capacity fade and the cycling efficiency of lithium - sulphur batteries are dependent on the form of the sulphur present in the electrolyte solution and the form of sulphur transfer from the positive electrode to the interelectrode space and thence to the surface of the negative electrode . the rate of capacity fade for lithium - sulphur batteries will be much lower and their cycling efficiency will be much higher if the sulphur is present as neutral particles ( molecular form ) as opposed to charged particles ( ionic form ). the degree of electrolytic dissociation of each salt in the electrolyte solution will be determined by their respective concentrations and dissociation constants in the presence of two or more different salts in the electrolyte composition ( here , for example , lithium polysulphides and the supporting salts ). based on the nature of the relevant anions , the present applicant believes that the electrolytic dissociation constants of lithium polysulphides are much lower than those of most lithium salts that may be used as supporting salts . in this case , with an increase in the supporting salt concentration , the equilibrium in the dissociation reaction of lithium polysulphides will shift towards a greater presence of the molecular form rather than the ionic form . accordingly , the dissociation degree of lithium polysulphides will decrease with an increase in the concentration of the supporting salts . hence , a decrease should be found in the rate of sulphur transfer between the electrodes and , correspondingly , in the rate of the capacity fade of a lithium - sulphur cell during cycling thereof . moreover , the cycling efficiency should increase as a result of the rate decrease of the sulphide cycle . this is clearly shown in the examples that follow . when forming the electrolyte compositions of embodiments of the present invention , the following considerations may be taken into account : 1 ) the electrolyte composition should comprise a non - aqueous aprotic solvent , lithium or another alkali metal salt and optional modifying additives . 2 ) said salt can be an individual salt or a number of different salts . 3 ) said salt or number of salts are dissolved in an individual aprotic polar solvent or a mixture of solvents . 4 ) said electrolyte composition should be chosen in a way that the concentration of the lithium salt or the mixture of salts is equal ( or close ) to the concentration of a saturated solution of the salt or salts used in the solvent or mixture of solvents . in generally , batteries or other devices , or compositions such as electrolyte compositions , or chemical sources of electric energy , according to embodiments of the present invention operate at certain temperature and pressure ranges . for example , in one embodiment , the operating temperature may be approximately − 40 to + 150 degrees celsius . in another embodiment , the operating temperature may be approximately − 20 to + 110 degrees c ., or − 10 to + 50 degrees c . in one embodiment , the operating pressure may be approximately 5 mmhg to 76000 mmhg ( 0 . 0066 to 100 atm ). in another embodiment , the operating pressure may be approximately 20 mmhg to 38000 mmhg ( 0 . 026 to 50 atm ), or for example approximately 1 atm . embodiments of the present invention may operate at standard temperature and pressure , for example at approximately 25 degrees c . and 1 atm . embodiments of the present invention may operate at other temperature and pressure ranges . a lithium - sulphur cell was produced by assembling an anode made of metal lithium foil ; a porous separator celgard 2500 ( a registered trademark of celgard inc ., available from celgard k . k ., tokyo , japan , and also available from celgard inc . south lakes , n . c . usa . ); and a sulphur cathode comprising elemental sulphur as a depolariser ( 70 % by weight ), a carbon electro - conducting additive ( 10 % by weight ) ketjenblack ec - 600jd ( available from akzo nobel polymer chemicals bv , netherlands ), and a binder ( polyethyleneoxide with molecular mass 4000000 - 20 % by weight ). the sulphur cathode was deposited by an automatic film applicator elcometer sprl onto one side of an 18 micrometer thick conductive carbon coated aluminium foil ( available from intelicoat ®, south hadley , mass .) as a current collector and substrate . a specific surface capacity of the cathode was 1 mah / cm 2 . the assembled cell was filled with an electrolyte comprising a 0 . 1m solution of liclo 4 in sulpholane . all stages of the cell assembling and filling were performed in a “ jacomex type bs531 ” glove box . the cell was cycled at a charge and discharge rate of 0 . 25 c and at a temperature of 25 ° c . the change in the charge and discharge capacity of the cell during the cycling is shown in fig1 . fig1 depicts curves of the sulphur electrode capacity change in a lithium - sulphur battery during cycling , according to one embodiment of the invention . in fig1 , the electrolyte is 0 . 1 m liclo 4 solution in sulpholane , the charge rate is 0 . 25 c , and the discharge rate is 0 . 25 c . the change of the cycling efficiency and the rate of the capacity fade during cycling are shown in fig2 . in fig2 , the electrolyte is 0 . 1 m liclo 4 solution and the average capacity fade rate is 4 . 5 %. the cycling efficiency is calculated as the ratio between the discharge capacity and the charge capacity expressed as a percentage . the rate of the capacity fade is calculated as the difference of the capacity at two cycles , following each other , divided by the mean capacity at these cycles and expressed as a percentage . as can be seen in fig2 , the efficiency of cycling and the rate of capacity fade initially change after the beginning of cycling , but later on they stabilize . the mean cycling efficiency between the 10 th and 20 th cycles was 68 %, and the rate of the capacity fade was 4 . 5 %. a lithium - sulphur cell was produced as described in the example 1 , but this time the assembled cell was filled with an electrolyte comprising a 1 m solution of liclo 4 in sulpholane . the cell was cycled at a charge and discharge rate of 0 . 25 c and at a temperature of 25 ° c . the change in the charge and discharge capacity of the cell during the cycling is shown in figure , showing the capacity fade of the sulphur electrode in lithium - sulphur cell during cycling . in fig3 , the electrolyte is a 1 m solution of liclo 4 in sulpholane , the charge rate is 0 . 25 c , and the discharge rate is 0 . 25 c . the change in the cycling efficiency and the rate of the capacity fade during cycling are shown in fig4 . in fig4 the electrolyte is 1 m solution of liclo 4 in sulpholane . as can be seen in fig4 , the efficiency of cycling and the rate of capacity fade initially change after the beginning of cycling , but later on they stabilize . the mean cycling efficiency between the 10 th and 20 th cycles was 90 %, and the rate of the capacity fade was 2 . 25 %. this is a marked improvement over the cell of example 1 . a lithium - sulphur cell was produced as described in the example 1 , but this time the assembled cell was filled with an electrolyte comprising a 2m saturated solution of liclo 4 in sulpholane in accordance with an embodiment of the present invention . the cell was cycled at a charge and discharge rate of 0 . 25 c and at a temperature of 25 ° c . the change in the charge and discharge capacity of the cell during the cycling is shown in fig5 , showing the capacity fade of a sulphur electrode in a lithium - sulphur cell during cycling . in fig5 , the electrolyte is a 2 m solution of liclo 4 in sulpholane , the charge rate is 0 . 25 c , and the discharge rate is 0 . 25 c . the change in the cycling efficiency and the rate of the capacity fade during cycling are shown in fig6 . in fig6 , the electrolyte is 2 m solution of liclo4 in sulpholane . as can be seen in fig6 , the efficiency of cycling and the rate of capacity fade initially change after the beginning of cycling , but later on they stabilize . the mean cycling efficiency between the 10 th and 20 th cycles was 96 %, and the rate of the capacity fade was 1 . 75 %. this is a marked improvement over the cells of examples 1 and 2 . a lithium - sulphur cell was produced as described in the example 1 , but this time the assembled cell was filled up with an electrolyte comprising a 0 . 1m solution of liclo 4 in methylpropylsulfone . the cell was cycled at a charge and discharge rate of 0 . 25 c and at a temperature of 25 ° c . the change in the charge and discharge capacity of the cell during the cycling is shown in fig7 , showing the capacity fade of a sulphur electrode in lithium - sulphur cell during cycling . the electrolyte is a 0 . 1 m solution of liclo4 in methylpropylsulfone , the charge rate is 0 . 25 c , and the discharge rate is 0 . 25 c . the change in the cycling efficiency and the rate of capacity fade during cycling are shown in fig8 . in fig8 , the electrolyte is 0 . 1 m solution of liclo4 in methylpropylsulfone . as can be seen in fig8 , the efficiency of cycling and the rate of capacity fade initially change after the beginning of cycling , but later on they stabilize . the mean cycling efficiency between the 10 th and 20 th cycles was 55 %, and the rate of the capacity fade was 3 . 1 %. a lithium - sulphur cell was produced as is described in the example 1 , but this time the assembled cell was filled with an electrolyte comprising a 1 . 7m solution of liclo 4 in methylpropylsulfone ( the concentration close to the saturated solution ). the cell was cycled at a charge and discharge rate of 0 . 25 c and at a temperature of 25 ° c . the change in the charge and discharge capacity of the cell during the cycling is shown in fig7 . the change in the cycling efficiency and the rate of capacity fade during cycling are shown in fig8 . as can be seen in fig8 , the efficiency of cycling and the rate of capacity fade initially change after the beginning of cycling , but later on they stabilize . the mean cycling efficiency between the 10 th and 20 th cycles was 90 %, and the rate of the capacity fade was 1 . 15 %, which is a marked improvement over the cell of example 4 . examples 4 and 5 illustrate that the improvement in cycling efficiency and rate of capacity fade is independent of the chemical identity of the solvent , but instead depends on the electrolyte concentration . while some embodiments of the invention have been illustrated and described , it is clear that the invention is not limited to these specific embodiments . numerous modifications , changes , variations , substitutions , and equivalents will occur to those skilled in the art without departing from the scope of the present invention . the preferred features of the invention are applicable to all aspects of the invention and may be used in any possible combination . throughout the description and claims of this specification , the words “ comprise ” and “ contain ” and variations of the words , for example “ comprising ” and “ comprises ”, mean “ including but not limited to ”, and are not intended to ( and do not ) exclude other components , integers , moieties , additives or steps .