the electrochemical cell of the present invention comprises an anode of a metal selected from group ia of the periodic table of the elements , including lithium , sodium , potassium , etc ., and their alloys and intermetallic compounds including , for example , li — si , li — al , li — mg , li — b and li — si — b alloys and intermetallic compounds . the preferred anode comprises lithium . the form of the anode may vary , but typically , the anode is a thin sheet or foil of the anode metal , pressed or rolled on a metallic anode current collector , i . e ., preferably comprising nickel , to form an anode component . in the electrochemical cell of the present invention , the anode component has an extended tab or lead of the same metal as the anode current collector , i . e ., preferably nickel , integrally formed therewith such as by welding and contacted by a weld to a cell case of conductive metal in a case - negative configuration . alternatively , the anode may be formed in some other geometry , such as a bobbin shape , cylinder or pellet to allow an alternate smaller volume cell design . the electrochemical cell of the present invention further comprises a cathode comprised of a combination of a first material that is electrochemically active and a second material that is electrochemically non - active , but electrically conductive . the cathode is preferably of solid materials and the electrochemical reaction at the cathode involves conversion of ions that migrate from the anode to the cathode into atomic or molecular forms . the solid cathode of the present invention preferably comprises a first electrochemically active material and a second electrochemically non - active material . more preferably , the first active cathode material comprises a fluorinated carbonaceous material and the second cathode material comprises a material of a non - electrochemically active carbonaceous chemistry . most preferably , the first electrochemical active cathode material comprises carbon monofluoride ( cf x ). preferred second non - active carbonaceous cathode materials may include acetylene black , graphitic and non - graphitic forms of carbon , coke , charcoal , ketjen black ®, and combinations thereof . in a traditional lithium oxyhalide electrochemical cell , the cathode is entirely composed of a carbon material that is electrochemically non - active , but electrically conductive . the cathode of a traditional lithium oxyhalide cell does not chemically react within the cell but provides a surface on which reaction products from a reduction reaction between lithium ions from the anode and active cathode constituents from the catholyte deposit . discharge of a traditional lithium oxyhalide cell continues until either of the anode or catholyte materials are exhausted , or the surface area of the cathode becomes occupied with reaction products . in contrast , the cathode of the present invention comprises an active material portion in addition to a non - active material . more specifically , some of the non - active carbon material is replaced with the active material , such as carbon monofluoride . the addition of the active material extends the duration of the discharge voltage and increases discharge capacity of the lithium oxyhalide cell . in addition , depending upon the amount of incorporated cf x , the active material causes a lithium oxyhalide cell to exhibit a substantially stable secondary discharge voltage plateau . this secondary voltage plateau typically occurs at a discharge voltage at or less than about 3 . 0 v , which is near the end - of - life of the cell . therefore , the occurrence of the secondary discharge voltage plateau serves as a useful end - of - life indicator . in general , the addition of the active material , specifically , cf x within the cathode structure of the lithium oxyhalide cell increases the surface area of the cathode . this increase in cathode surface area creates additional surface on which the reaction products from the reduction reaction of the catholyte deposit . thus , the additional cathode surface area created by the addition of the cf x further extends the duration of the first reduction reaction between the lithium and oxyhalide constituents which extends voltage discharge and increases discharge capacity . secondly , the cf x within the cathode structure undergoes a second reduction reaction in which lithium ions react with the cathode material during discharge to provide a secondary discharge voltage and discharge capacity . during cell discharge the first reduction reaction occurs between lithium and the oxyhalide catholyte . the first reduction reaction , which typically occurs at discharge voltages above 3 . 0 v , produces a discharge voltage and lithiated chloride that deposits on the cathode surface and within pores of the cathode structure . in addition , a second reduction reaction occurs between lithium and the active cathode material , such as cf x . this second reduction reaction , which generally occurs at discharge voltages of 3 . 0 v or below , produces a substantially stable discharge voltage plateau and carbon . the following are exemplary first and second reduction reactions that may occur within a lithium oxyhalide cell of the present invention . in a preferred embodiment , both the first and second reduction reactions contribute to the overall discharge voltage and capacity of the lithium oxyhalide cell . as a result , the addition of the active cathode material generally causes a lithium oxyhalide cell to exhibit a greater amount of discharge capacity than if the cell did not comprise the active cathode material . in addition , since the active carbon material , such as carbon monofluoride , generally occupies about the same volume within the cathode as the non - active material that was replaced , the inclusion of the active carbon material provides the cathode and cell thereof additional energy without occupying additional cell volume . thus , the energy density of the lithium oxyhalide cell of the present invention is further increased . as previously mentioned , a preferred active cathode material is carbon monofluoride , ( cf x ), which has a relatively high energy density compared to other non - active cathode materials . cf x is generally known to have a specific capacity of about 875 mah / g , which contributes to the overall discharge capacity of a lithium oxyhalide cell of the present invention . furthermore , cf x replaces some of the non - active material within the cathode structure on a 1 : 1 volume basis . therefore , the addition of cf x increases the energy density of the cell as the active material does not occupy a greater cell volume as compared to the non - active carbon material . in a preferred embodiment , the first active material is a fluorinated carbon , preferably , carbon monofluoride , having the formula cf x where x ranges from about 0 . 5 to about 1 . 2 , more preferably from about 0 . 9 to about 1 . 1 . stoichiometric proportions of the first active material and the second non - active material are mixed together , such as by milling the two materials together . alternatively , stoichiometric proportions of the first active material and the second non - active material may be reacted together by a chemical addition reaction or otherwise intimate contact of the various materials thereof to form a cathode material mixture . in a preferred embodiment , the first active material and the second non - active material may be heated together above ambient temperature for about 1 to 5 hours . for example , the first and second materials may be heated together at a temperature ranging from about 50 ° c . to about 800 ° c . for about 1 to 5 hours . in a preferred embodiment , the first active material , ( cf x ), comprises from about 5 to about 95 weight percent of the total cathode material mixture , the remainder comprising the second non - active material . more preferably , the first active material , ( cf x ), may comprise from about 25 to about 90 weight percent of the total cathode material mixture , the remainder comprising the second non - active material . most preferably , the first active material , ( cf x ), may comprise from about 40 to about 80 weight percent of the total cathode material mixture , the remainder comprising the second non - active material . the preferred second non - active material is acetylene black . in addition , a binder material such as a powdered fluoro - polymer , more preferably powdered polytetrafluoroethylene ( ptfe ) or powdered polyvinylidene flouride may be added to the cathode material mixture . in a preferred embodiment , the binder material may comprise about 1 to about 15 weight percent of the total cathode material mixture . in a preferred embodiment , the cathode material mixture comprises a first active material , a second non - active material , and a binder such as a powdered fluoro - polymer . cathode components for incorporation into an electrochemical cell according to the present invention may be prepared by rolling , spreading or pressing the cathode material mixture of the first active cathode material , the second non - active cathode material , and binder onto a suitable current collector selected from the group consisting of nickel , stainless steel , titanium , tantalum , platinum , gold , aluminum , cobalt nickel alloys , nickel - containing alloys , highly alloyed ferritic stainless steel containing molybdenum and chromium , nickel -, chromium - and molybdenum - containing alloys , conductive carbon , and conductive polymers . cathodes prepared as described above may be in the form of one or more plates operatively associated with at least one or more plates of anode material , or in the form of a strip wound with a corresponding strip of anode material in a structure similar to a “ jellyroll ”. the exemplary cell of the present invention further includes a separator to provide physical separation between the anode and cathode . the separator is of an electrically insulative material to prevent an internal electrical short circuit between the electrodes , and the separator material also is chemically unreactive with the anode and cathode materials and both chemically unreactive with and insoluble in the catholyte . in addition , the separator material has a degree of porosity sufficient to allow flow therethrough of the catholyte during the electrochemical reaction of the cell . illustrative separator materials include non - woven glass , polypropylene , polyethylene , microporous material , glass fiber materials , ceramics , polytetrafluorethylene membrane commercially available under the designations zitex ( chemplast inc . ), polypropylene membrane , commercially available under the designation celgard ( celanese plastic company inc .) and dexiglas ( c . h . dexter , div ., dexter corp .). other separator materials that are useful with the present invention include woven fabric separators comprising halogenated polymeric fibers , as described in u . s . pat . no . 5 , 415 , 959 to pyszczek et al ., which is assigned to the assignee of the present invention and incorporated herein by reference . examples of halogenated polymeric materials suitable for the electrochemical cell of the present invention include , but are not limited to , polyethylene tetrafluoroethylene which is commercially available under the name tefzel , a trademark of the dupont company ; polyethylenechlorotrifluoroethylene which is commercially available under the name halar , a trademark of the allied chemical company , and polyvinylidene fluoride . the form of the separator typically is a sheet which is placed between the anode and cathode and in a manner preventing physical contact therebetween . such is the case when the anode is folded in a serpentine - like structure with a plurality of cathode plates disposed intermediate the anode folds and received in a cell casing or when the electrode combination is rolled or otherwise formed into a cylindrical “ jellyroll ” configuration . the cell further comprises a non - aqueous ionically conductive catholyte operatively associated with the anode and the cathode . the catholyte serves as a medium for migration of ions between the anode and the cathode during the cell &# 39 ; s electrochemical reactions . in a preferred embodiment , the catholyte comprises a nonaqueous solvent depolarizer . suitable nonaqueous solvent depolarizers exhibit those physical properties necessary for ionic transport , namely , low viscosity , low surface tension and wettability . these nonaqueous depolarizers are preferably comprised of an inorganic salt dissolved in a nonaqueous co - depolarizer system and , more preferably , a lithium salt dissolved in a catholyte solution comprising a halogen and / or interhalogen dissolved in a nonaqueous solvent . the halogen and / or interhalogen serves as a soluble depolarizer . they can also serve as a co - solvent in the electrochemical cell . the halogen is selected from the group of iodine , bromine , chlorine or fluorine while the interhalogen is selected from the group of clf , clf 3 , icl , icl 3 , ibr , if 3 , if 5 , brcl , brf , brf 3 , brf 5 , and mixtures thereof . the mole ratio of any one of the above - referenced halogens and / or interhalogens dissolved in any one of the above - referenced nonaqueous organic or inorganic solvents is from about 1 : 6 to about 1 : 1 . the nonaqueous solvent depolarizer also may be one or a mixture of more than one of the inorganic solvents which can serve as both a solvent and a depolarizer such as thionyl chloride , sulfuryl chloride , selenium oxychloride , chromyl chloride , phosphoryl chloride , phosphorous sulfur trichloride , and others . the ionic conductivity of the nonaqueous catholyte solution is preferably facilitated by dissolving a lithium salt in the nonaqueous depolarizer . exemplary salts are lithium halides such as licl and libr and those of the limx n type , such as lipf 6 , libf 4 , liasf 6 , lisbf 6 , liclo 4 , lia 1 cl 4 , ligacl 4 , lic ( so 2 cf 3 ) 3 , lin ( so 2 cf 3 ) 2 , liscn , lio 3 scf 2 cf 3 , lic 6 f 5 so 3 , lio 2 , lio 2 ccf 3 , liso 3 f , lib ( c 6 i - 1 , 0 4 , licf 3 so 3 , and mixtures thereof . suitable salt concentrations typically range between about 0 . 25 to about 1 . 5 molar . the solution of halogen and / or interhalogens , the nonaqueous solvent depolarizer and , optionally , the ionic salt , serve as the co - depolarizer and catholyte of the oxyhalide cell . the preferred form of the electrochemical cell is a case - negative design wherein the anode / cathode couple is inserted into a conductive metal casing connected to the anode current collector , as is well known to those skilled in the art . a preferred material for the casing is stainless steel , although titanium , mild steel , nickel , nickel - plated mild steel and aluminum are also suitable . the casing header comprises a metallic lid having a sufficient number of openings to accommodate the glass - to - metal seal / terminal pin feedthrough for the cathode . the anode is preferably connected to the case or the lid . an additional opening is provided for electrolyte filling . the casing header comprises elements having compatibility with the other components of the electrochemical cell and is resistant to corrosion . the cell is thereafter filled with the electrolyte solution described hereinabove and hermetically sealed , such as by close - welding a stainless steel plug over the fill hole , but not limited thereto . the cell of the present invention can also be constructed in a case - positive design . one preferred form of the cell assembly described herein is referred to as a wound element cell . that is , the fabricated cathode , anode and separator are wound together in a “ jellyroll ” end type configuration or “ wound element cell stack ” such that the anode is on the outside of the roll to make electrical contact with the cell case in a case - negative configuration . using suitable top and bottom insulators , the wound cell stack is inserted into a metallic case of a suitable size dimension . the glass - to - metal seal preferably comprises a corrosion resistant glass having from between about 0 % to about 50 % by weight silica such as cabal 12 , ta 23 or fusite msg - 12 , fusite a - 485 , fusite 425 or fusite 435 . the positive terminal pin feedthrough preferably comprises stainless steel such as 52 alloy or 446 stainless steel , although titanium , molybdenum and aluminum can also be used . the cell header comprises elements having compatibility with the other components of the electrochemical cell and is resistant to corrosion . the cathode lead is welded to the positive terminal pin in the glass - to - metal seal and the header is welded to the case containing the electrode stack . the cell is thereafter filled with the electrolyte described hereinabove and hermetically sealed such as by close - welding a stainless steel ball over the fill hole , but not limited thereto . this above assembly describes a case - negative cell which is the preferred construction of the exemplary cell of the present invention . as is well known to those skilled in the art , the exemplary electrochemical system of the present invention can also be constructed in a case - positive configuration . the electrochemical cell of the present invention operates in the following manner . when the ionically conductive catholyte solution becomes operatively associated with the anode and the cathode of the cell , an electrical potential difference is developed between terminals operatively connected to the anode and the cathode . during discharge , the electrochemical reaction at the anode includes oxidation to form metal ions . the electrochemical reaction at the cathode involves conversion of these ions which migrate from the anode to the cathode into atomic or molecular forms . in addition , the halogen and / or interhalogen of the catholyte is believed to undergo a reaction or reactions with the lithium ions thereof resulting in the formation of a compound or complex which exhibits the observed open circuit voltage of the cell . as previously mentioned , the incorporation of the active cathode material , preferably cf x , within the cathode structure increases the surface area of the cathode . as a result , the first reduction reaction that occurs between the lithium ions from the anode and the halogen and / or interhalogen from the catholyte is extended thereby producing additional discharge voltage and capacity . in order to demonstrate the advantages attributed to the present invention , two hermetically sealed lithium oxyhalide coin cells were constructed and tested . each cell was constructed having about the same weight of anode and catholyte . the cathodes of the respective first and second test cells were constructed having about the same volume but of a different composition . the cathode of the first cell , test cell 1 , was constructed similar to that of a traditional lithium oxyhalide cathode comprising about 90 weight percent non - active acetylene black and about 10 weight percent ptfe binder . the cathode of the second cell , test cell 2 , was constructed according to an embodiment of the present invention comprising about 80 weight percent active carbon monofluoride , 10 weight percent non - active acetylene black and about 10 weight percent ptfe binder . the anode of both test cells 1 and 2 was composed of lithium and the catholyte of the cells was composed of thionyl chloride with 1 . 8 m lithium tetrachloroaluminate salt . both test cells 1 and 2 were discharged in which the discharge voltage was measured as a function of capacity delivered in mah . fig1 illustrates the discharge testing results in which each of the first and second test cells of example i were fully discharged . curve 10 represents the discharge profile of test cell 1 which comprised the cathode composed of about 90 weight percent acetylene black and about 10 weight percent ptfe . curve 12 represents the discharge profile of test cell 2 which comprised a cathode composed of about 80 weight percent cf x , 10 weight percent acetylene black and about 10 weight percent ptfe . as illustrated by the graph of fig1 , both test cells had an initial discharge voltage of about 3 . 6 v . test cell 1 exhibited a discharge capacity of about 320 mah after which the cell &# 39 ; s discharge voltage abruptly dropped as the cell reached end - of - life . in comparison , test cell 2 , which comprised a cathode composed of a mixture of about 80 weight percent cf xr exhibited an increased discharge capacity 14 of about 520 mah , which was about 200 mah more than the discharge capacity of test cell 1 . in addition to the increased discharge capacity at about 3 . 6 v discharge volts , the second test cell also exhibited a second substantially stable discharge voltage plateau 16 at about 2 . 3 v . this discharge voltage plateau 16 thus generated an additional discharge capacity of about 20 mah . furthermore , the second substantially stable discharge voltage at about 2 . 3 v may serve as an indicator that the cell is approaching end - of - life . in addition , two hermetically sealed lithium oxyhalide aa size cells were constructed and tested . a third cell , test cell 3 , was constructed similar to that of a prior art lithium oxyhalide cell comprising a cathode composed of about 90 weight percent acetylene black and about 10 weight percent ptfe binder . a fourth cell , test cell 4 , was constructed according to an embodiment of the present invention comprising a cathode composed of about 45 weight percent cf x , about 45 weight percent acetylene black and about 10 weight percent ptfe binder . the anodes of the respective test cells were composed of lithium and were constructed having about the same weight and size . the catholyte of both cells was composed of thionyl chloride with 1 . 8 m lithium tetrachloroaluminate salt . both test cells 3 and 4 were discharged in which the discharge voltage was measured as a function of discharge capacity in mah . fig2 illustrates the discharge testing results in which the third and fourth aa sized test cells from example ii were fully discharged . curve 18 represents the discharge profile of test cell 3 which comprised a cathode composed of about 90 weight percent acetylene black and about 10 weight percent ptfe . curve 20 represents the discharge profile of test cell 4 which comprised a cathode composed of about 45 weight percent cf x , 45 weight percent acetylene black and about 10 weight percent ptfe . as illustrated by the graph of fig2 , test cell 3 , which was constructed having a cathode comprised of non - active carbon material , exhibited an overall discharge capacity of about 160 mah . in comparison , test cell 4 , which was constructed having a cathode comprised of about 45 weight percent active cf x , exhibited a discharge capacity of about 210 mah . the lithium test cell comprising the cf x active material , thus exhibited an increase in discharge capacity of about 31 percent in comparison to test cell 3 that did not comprise cf x . the discharge test results illustrated in fig1 and 2 clearly indicate that the addition of cf x within the cathode of a lithium oxyhalide electrochemical cell significantly increases discharge capacity . test cell 2 of example i which comprised about 80 weight percent cf x , exhibited a significant increase in discharge capacity of about 200 mah or about 52 . 5 % more than respective test cell 1 that did not comprise cf x . in addition , test cell 4 of example ii , which comprised about 45 weight percent cf x , also exhibited a significant increase in discharge capacity in comparison to test cell 3 which did not comprise cf x . as illustrated from fig2 , test cell 4 exhibited about 65 mah or about 40 % more capacity than the respective test cell 3 that did not comprise cf x . the discharge test results appear to indicate that an increasing amount of cf x . within a cathode structure of a lithium oxyhalide cell increases its overall capacity , as evidenced by the discharge results of test cells 2 and 4 . as illustrated , test cell 2 that comprised the greater weight percent of cfx , exhibited the greater discharge capacity in comparison to test cell 4 . thus , in general , the discharge test results appear to indicate that a greater weight percent of cf x within the cathode structure causes an increase in cell discharge capacity . this correlation is generally believed to be the result of increased cathode surface area stemming from the incorporation of a greater amount of cf x within the carbon structure . however , while the test results indicate that , in general , there is a direct correlation between increased weight percent of cf x within the cathode and increased discharge capacity , it is not desirable to construct a lithium oxyhalide cathode entirely of cf x . this is because cf x is generally a poor conductor of electricity and a lithium oxyhalide cathode must comprise a material that exhibits a degree of electrical conductivity of which cf x is not sufficient . it is noted that u . s . pat . no . 6 , 780 , 542 to spillman et al ., assigned to the assignee of the present invention and incorporated herein by reference , discloses a lithium oxyhalide cell which comprises a lithium carbonate passivation layer on the lithium anode to minimize voltage delay . in addition , spillman discloses that the cathode current collector of the oxyhalide cell may be composed of an electrically conductive material , including carbon monofluoride , cf x . however , constructing a lithium oxyhalide cell comprising a cathode composed entirely of cf x is not advisable as the electrical conductivity of the cf x material , which is about 10 - 14 s / cm ( touhara et al . ( 1987 ) 2 . anorg . all . chem . 544 : 7 ), is not adequate for a lithium oxyhalide cell to operate . in contrast , the lithium oxyhalide cell of the present invention is a hybrid cell that comprises a cathode composed of an active material portion , cfx , and an inactive material portion , i . e ., acetylene black that is electrically conductive . thus , unlike a cathode of a traditional lithium oxyhalide cell , the cathode of the present invention does not act solely as a current collector , but rather , in addition , comprises a portion of a cathode material that chemically reacts within the lithium oxyhalide cell to provide an additional discharge voltage . the addition of the active material , cf x , in specific proportions , thus , enables a desired modification of the extended discharge voltage and capacity exhibited by a lithium oxyhalide cell . a specific amount of the active cf x material chemically reacts with lithium ions in the catholyte solution to provide additional discharge voltage and increased discharge capacity . the addition of the non - active carbonaceous material provides electrical conductivity within the cell that enables cell operation . thus , as illustrated by the test results , the discharge and capacity characteristics of a lithium oxyhalide cell can by modified by specific amounts of cf x incorporated within the cathode of the cell . these preferred amounts of cfx and inactive material , respectively , are not disclosed by spillman and thus , would not be obvious to one of ordinary skill in the art . with regards to the lithium oxyhalide cell of the present invention , the increased amount of carbon surface area provided by the cf x allows for more of the first reduction reaction product to deposit on the surface of the cathode . thus , the increased carbon surface area provides additional sites on which the reaction products of the first reduction reaction deposit , thereby extending the discharge voltage , and increasing discharge capacity as indicated by test cells 2 and 4 of examples i and ii ( 12 , 20 fig1 and 2 ). in addition , as shown in fig1 , test cell 2 that comprised the greater amount of cf x , also exhibited the second discharge voltage plateau 16 at about 2 . 3 v . this second discharge voltage plateau 16 is generally believed to be the result of discharge voltage produced from the second reduction reaction of the cf x after the lithium - oxyhalide first reduction reaction of the oxyhalide was complete . the first reduction reaction between lithium and the catholyte is generally of a greater energy state than the second reduction reaction between lithium and active cf x material . thus , as the lithium oxyhalide cell of the present invention discharges , a first discharge plateau at a higher discharge voltage , generally greater than about 3 . 0 v (˜ 3 . 6 v in fig1 and ˜ 3 . 4 v in fig2 ) is generated . after the first reduction reaction of the catholyte material nears completion , the second reduction reaction between lithium and cf x takes over , typically exhibiting a lower voltage plateau at or below 3 . 0 v (˜ 2 . 3 v in fig1 ). the second discharge voltage plateau 16 thus serves as an indicator that the cell is approaching end - of - life . the test results appear to indicate that there is a threshold amount of active cathode material , such as cf x , incorporated within the cathode structure to exhibit this second discharge voltage plateau 16 . for example , test cell 4 , which comprised a lesser amount of cf x , did not exhibit a second discharge voltage plateau as was exhibited in test cell 2 . thus , from the test results as illustrated in fig1 and 2 , it is preferred that a lithium oxyhalide cathode comprises at least about 40 weight percent active cathode material , i . e ., cf x , of the total cathode material formulation to exhibit a substantially stable end - of - life indicator as exhibited in the test results shown in fig1 . however , this threshold amount of cf x added to the total cathode material formulation may be as low as 10 weight percent depending upon certain parameters such as cell size , the volume of catholyte and / or the volume of the anode within the cell . therefore , depending on the proportion of cf x added to the cathode material mixture , it is possible to observe two voltage plateaus during cell discharge as illustrated by the discharge test results of fig1 . thus , lithium oxyhalide electrochemical cells constructed with a cathode comprising the mixture of an electrochemically active and non - active material of the present invention have increased discharge capacity . in addition , a cathode comprising the mixture of an electrochemically active and non - active material of the present invention also enables a lithium oxyhalide electrochemical cell to exhibit a substantially stable discharge voltage plateau that may serve as a discernible end - of - life indicator . the above detailed description and examples are intended for purposes of illustrating the invention and are not to be construed as limited .