Abstract:
Conductor polymers prepared by anodic oxidation of compounds of general formula (I) ##STR1## in which E=O, S, Se; 
     R 1  =H or a saturated or unsaturated alkyl radical with double bonds in the vinyl or allyl position with respect to the nitrogen; 
     R 2 , R 3  =H or methyl radicals. 
     These polymers have a cross-linked structure with intermonomer bonds in which possible in nitrogen-bonded vinyl groups and the aromatic rings are involved, and delocalized positive charges in the chain neutralized by counter-ions such as Cl - , BF -   4 , ClO -   4  or PF -   6 . These polymers can be used in the construction of rechargeable batteries of completely solid state.

Description:
BACKGROUND OF THE INVENTION 
     1. Field of the Invention 
     This invention relates to organic polymers having delocalized positive charges in the chain neutralized by inorganic counter-ions, and suitable for use both as electrolytes and as electrode materials in the construction of completely dry batteries. 
     2. Prior art 
     Numerous conductor polymers and their relative preparation methods are known, these being based on electrochemical polymerization in the presence of an auxiliary electrolyte. 
     For example, a method for preparing polypyrrole is described in Japanese patent 131,104 (1986); a method for preparing polythiophene is described in Japanese patent 62,521 (1986); the preparation of polymers of aminochrysene, aminofluoranthene, aminophenanthrene, naphthylamine, 2-aminobenzimidazole and 2-aminobenzothiazole is described in Japanese patent 219,228 (1985). 
     These polymers have prospective applications of considerable importance as they can be used for battery electrodes, electrochemical sensors, electrochromic devices and other applications. 
     However, when used as electrodes, these polymers present self-discharge problems. 
     SUMMARY OF THE INVENTION 
     We have now discovered new conductor polymers prepared by anodic oxidation of compounds of general formula (I) ##STR2## in which E=O, S, Se; 
     R 1  =H or a saturated or unsaturated alkyl radical with double bonds in the vinyl or allyl position with respect to the nitrogen; 
     R 2 , R 3  =H or methyl radicals, 
     and having a cross-linked structure with intermonomer bonds in which possible nitrogen-bonded vinyl groups and the aromatic rings are involved, and delocalized positive charges in the chain neutralized by counter-ions such as Cl - , BF -   4 , ClO -   4  or PF -   6 . 
     The present invention also relates to the use of said polymers both as electrolytes and as electrode materials for the construction of completely dry batteries. 
     These polymers are not subject to significant self-discharge phenomena when used as electrolytes for the construction of completely dry batteries. 
     They are prepared by electrochemical polymerization of (I) by anodic oxidation in an organic solvent in the presence of a transport electrolyte which provides the counter-ion. 
    
    
     BRIEF DESCRIPTION OF THE DRAWINGS 
     FIG. 1 is the mass spectrum for the product. 
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
     The characteristics of the polymers according to the present invention and of their preparation method plus their possible applications as battery electrolytes will be illustrated in detail in the following description. 
     The monomer (I) is prepared by known methods, for example monomer (I) can be prepared by N-vinylation of thionaphthene-indole applying the method used for the N-vinylation of carbazole described by G. R. Clemo, W. H. Perkin in J. Chem. Soc. Trans., 1924, 125, 1804. The product obtained can be purified chromatographically and characterized by NMR and MS. 
     Monomer (I) is dissolved in an organic solvent in a quantity such as to obtain a concentration of between 5.10 -3  moles/liter and its solubility in the solvent itself. Suitable solvents are aprotic solvents such as CH 2  Cl 2 , CH 3  CN, C 6  H 5  CN and dimethylformamide. 
     The preferred solvent is CH 2  Cl 2 . 
     A transport electrolyte represented generically by MX in which M is Li, Na, K, NR 4  where R 4  is C 1  -C 4  alkyl and X is Cl, BF 4 , ClO 4  or PF 6  is added to the solution. 
     The preferred transport electrolyte is NBu 4  ClO 4 . 
     The transport electrolyte concentration in the solution is between 0.01 and 1 mole/l and preferably between 0.08 and 0.12 moles/l. 
     The method is preferably conducted in an anhydrous medium, however limited quantities of water of up to 10 -2  moles/l do not negatively influence the process. 
     The oxygen has to be completely removed from the solution, this being preferably accomplished by bubbling an inert gas, through such as argon or nitrogen, through the solution and in addition the electrochemical process must be conducted in an inert gas atmosphere. 
     The electrodes of the electrolytic cell used for the electrochemical polymerization are of metal or metal oxide, preferably Pt, Au, steel or SnO 2 . In the cell the cathode compartment is separated from the anode compartment by porous diaphragm means. 
     The cell is advantageously provided with a saturated calomel reference electrode. 
     The electrochemical polymerization is conducted at a constant potential of between +1 and +3.5 V and preferably between +1.2 and +1.3 V with respect to the saturated calomel electrode. 
     However it can also be conducted a constant current density, with the current density being between 0.6 and 3 mA/cm 2  and a potential difference being between the anode and cathode of about 100 V. 
     The polymerization is conducted at a temperature of between 10° and 40° C. 
     At the anode a black, oxidised, insoluble polymer deposit is obtained, and is washed with a solvent of the type used in the preparation, and then dried. Chemical, physico-chemical and electrical characterization tests are carried out on the product, together with applicational tests regarding its use as electrolytic material for batteries. 
     On elementary chemical analysis the polymer of the present invention obtained using N-vinylthionaphthene-indole (VTNI) as monomer and NBu 4  ClO 4  as transport electrolyte consists of repetitive units of formula [p(VTNI) y+ .yClO -   4  +zH 2  O] n  in which there is a difference in hydrogen content with respect to the theoretical formula C 16  H 11  SN, due to bonds between the aromatic rings, whereas the bonds are prevalently on the side chain in accordance with the scheme: ##STR3## 
     The mass spectrum for the product, shown in FIG. 1, indicates peaks relative to high-mass ions congruent with a polymer substance. 
     The results of the mass spectrometry measurements are given in Table 1, which shows the structure of some of the more significant ionic species. 
     These structures confirm that the polymerization takes place with the formation of bonds both between the vinyl groups and between the benzene rings. 
     Electrical conductivity tests were carried out on the polymer obtained, using the method described in G. Casalbore-Miceli, G. Beggiato, S. Dadio, P. G. Di Marco, S. S. Emmi, G. Giro, J. Appl. Electrochem. 17 (1987) 1111. 
     In the various examined samples the specific conductivity is between 0.97 and 1.1×10 -5  ohm -1  cm -1 . 
     The polymers according to the present invention were used with surprising results in the construction of solid rechargeable batteries in which the same polymers were shown to be able to operate both as electrolytes and as electrode materials. Consequently this application also constitutes a subject of the present invention. 
     The battery according to the present invention consists of the following elements all in the solid state: 
     
         (-)Me.sub.1 //[p(I).sup.y+.yX.sup.- +zH.sub.2 O].sub.n //Me.sub.2 (+) 
    
     in which Me 1  is an oxidisable metal such as Zn, Cu, Fe and preferably Zn, Me 2  is a noble metal such as Au, Pt or metallic oxide, p(I) is the polymer according to the invention, X -  is the counter-ion and z is a number between 1 and 2. 
     When Me 1  is Zn and Me 2  is Au, the battery can be charged to give an anodic potential of between 1.5 and 5 V at the electrode Me 2  with respect to the electrode Me 1 . 
     The electrode processes can be schematised in the following manner: 
     
         Me.sub.1.sup.++ +2e.sup.- →Me.sub.1 (reaction at cathode) 
    
     
         2P-2e.sup.- →2P.sup.+ (reaction at anode) 
    
     where P +  represents a delocalized positive site in the polymer chain. 
     When Me 1  is Zn and Me 2  is Au, the battery has an open circuit voltage of about 0.85 V. 
     When the element operates as a current generator (battery discharge), the following reactions occur: 
     
         Me.sub.2 (positive pole)2e.sup.- +2P.sup.+ →2P 
    
     
         Me.sub.1 (negative pole)Me.sub.1 -2e.sup.- →Me.sub.1.sup.++ 
    
     These reactions are evidenced by the following observations: 
     Me 1  is the negative pole of the battery; 
     after various cycles, whereas the Me 2  /polymer interface does not appear modified, the Me 1  /polymer interface appears pitted with the formation of an unidentified solid substance; 
     the battery voltage does not appear significantly modified when using an Au or Pt electrode for Me 2 , whereas if a Zn, Cu or Fe electrode is used for Me 1  the battery voltage varies significantly; 
     the voltage agress well with the theoretical value for the aforesaid electrode reactions. 
     In the battery according to the present invention the polymer therefore acts both as the electrode material and as the solid electrolyte. In this respect, during operation of the battery as a generator, the voltage measured immediately after opening the circuit is less than the value which is gradually established on leaving the circuit open, whereas during operation of the battery as an electrolyzer (charge stage), the voltage measured immediately after opening the circuit is higher than that which is gradually established on leaving the circuit open. 
     There is thus a slow diffusion of the charges in the electrolyte and a polarization overvoltage at the electrodes. This has also been demonstrated by the difference in the specific resistance of the polymer when measured in an alternating field and in a direct field. 
     The diffusion overvoltage is therefore the &#34;slow stage&#34; in the battery operation. In this respect, a large variation in external resistance does not significantly influence the delivered current. Significant variations are obtained for loads of the order of 100 kohm. 
     The battery according to the present invention is particularly advantageous because of the following characteristics: 
     battery totally of solid state; 
     easy construction; 
     not subject to substantial self-discharge phenomena; 
     rechargeable for a large number of cycles; 
     light in weight; 
     non-polluting constituent material; 
     possibility of recovering the electrode materials; 
     possibility of assembling several elements to obtain high voltage; 
     protection from short-circuiting by internal polarization; 
     possibility of varying the internal resistance by dispersing salts of the electrode metal in the polymer electrolyte or subjecting the battery to preliminary cycles. 
     The battery can be used for example in watches, calculators, cardiac stimulators, microelectronics and portable instruments generally. 
     The following examples are given by way of non-limiting illustration of the present invention. 
     EXAMPLE 1 
     A solution of N-vinyl-thionaphthene-indole (VTNI) and tetrabutylammonium perchlorate (TBAP) in methylene chloride was fed into an electrolytic cell of capacity 4 ml. 
     The VTNI had been purified by chromatography and characterised by NMR and MS; the TBAP (Fluka purum) had been recrystallized from methanol and the methylene chloride had been distilled from P 2  O 5  in a nitrogen atmosphere. 
     The VTNI concentration in the solution was 5×10 -2  M and the TBAP concentration was 0.1M. 
     The electrolytic cell was provided with Pt electrodes, of which the anode was in the form of a platinum plate of area 1 cm 2 . The cathodic compartment containing a platinum spiral was separated from the anodic compartment by a sintered glass diaphragm. The cell was also provided with a saturated calomel reference electrode. 
     The solution was degassed by bubbling nitrogen through in order to completely remove the oxygen, after which polymerization was commenced by electrochemical oxidation operating with a potential difference of 1.2 V. The polymerization was conducted at 22° C. in a nitrogen atmosphere. 
     The polymer deposited at the anode in the form of a black solid deposit with a yield of 76%. 
     From elementary chemical analysis the polymer was found to have the following formula: C 15 .7 H 10 .5 N 1 .01 0.682(ClO 4 )+1.3H 2  O. 
     The mass spectrum was as shown in FIG. 1. The specific conductivity was 1.1×10 -5  ohm -1  cm -1 . 
     EXAMPLE 2 
     The polymer obtained by operating in accordance with Example 1 was used to construct a rechargeable battery formed from the following elements: 
     
         (-)Zn//poly-VTNI.sup.+ (ClO.sub.4).sup.- //Au(+) 
    
     all in the solid state and with the following constructional characteristics: 
     electrode diameter (Au and Zn) . . . 0.5 cm 
     electrode area . . . 0.196 cm 2   
     thickness of polymer layer (oxidised poly-VTNI powder compressed to 2 ton.) . . . 661 microns 
     weight of polymer (density about 1) . . . 13 mg 
     maximum current 20 μA; average current 2-3 μA (load=1000 O) 
     The battery was charged by providing a potential of 5 V at the Au anode with respect to the Zn, to obtain an open-circuit battery voltage of slightly less than 1 V. This voltage corresponds to the free energy of the following reactions taking place during the discharge stage: 
     
         Au(positive pole)2e.sup.- +2P.sup.+ →2P(E.=-0.1)(saturated calomel electrode) 
    
     
         Zn(negative pole)Zn-2e.sup.- →Zn.sup.++ (E.=-1 V in aqueous solution)(saturated calomel electrode) 
    
     The ratio of delivered charge to supplied charge is close to 1. 
     The battery internal resistance varies with the number of cycles or on dispersing a Zn salt in the polymer electrode (2 MO-1600 O). 
     The theoretical capacity depends on the extent of polymer oxidation and can range from 55 to 80 Ah/kg of polymer. 
     EXAMPLE 3 
     A battery was constructed consisting of two elements as described in Example 2 but with the positive pole formed of platinum instead of gold. The electrodes were 1 cm 2 . 
     The voltage was practically additive (1.9 V), the maximum current delivered was 400 μA and the average current 30-40 μA. 
     
                                           TABLE 1__________________________________________________________________________RESULTS OF MASS SPECTROMETRY MEASUREMENTS ON POLY VTNI&#39;S   empiricalm/z   formula    structure formula__________________________________________________________________________665   C.sub.42 H.sub.23 N.sub.3 S.sub.3     ##STR4##498   C.sub.32 H.sub.22 N.sub.2 S.sub.2     ##STR5##478   C.sub.31 H.sub.28 NS.sub.2     ##STR6##   or    or   C.sub.33 H.sub.36 NS     ##STR7##444   C.sub.20 H.sub.10 N.sub.2 S.sub.2     ##STR8##412   C.sub.20 H.sub.22 NS.sub.2     ##STR9##   or    or   C.sub.28 H.sub.30 NS     ##STR10##357   C.sub.22 H.sub.15 NS.sub.2     ##STR11##   or    or   C.sub.24 H.sub.23 NS     ##STR12##325   C.sub.22 H.sub.15 NS     ##STR13##257   C.sub.18 H.sub.13 N.sub.2     ##STR14##   or    or   C.sub.19 H.sub.29    CH.sub.2(CHCH.sub.2 ) .sub.9223   C.sub.14 H.sub.9 NS     ##STR15##142   C.sub.10 H.sub.8 N     ##STR16##121   C.sub.7 H.sub.5 S     ##STR17##   or    or   C.sub.9 H.sub.13    (CHCH.sub.2 ) .sub.4CH120   C.sub.8 H.sub.10 N     ##STR18## 93   C.sub.6 H.sub.7 N     ##STR19## 78   C.sub.6 11.sub.6     ##STR20##__________________________________________________________________________