ALKALINE BATTERY HAVING A PAPER SEPARATOR

Abstract: A battery separator paper suitable for use in an alkaline battery comprises a web of polyolefinic synthetic pulp fibres and fibres effective to reinforce the polyolefinic fibres. The polyolefinic synthetic pulp fibres are not substantially heat-­ bonded to each other or to the reinforcing fibres but are bonded to each other and the reinforcing fibres by means of an alkali-resistant hydrophilic binder, e.g. polyvinyl alcohol. The reinforcing fibres may for example be polyvinyl alcohol, rayon, PVC or nylon. The battery separator paper is made by conventional papermaking techniques.

Description: BATTERY SEPARATOR PAPER AND PROCESS FOR ITS MANUFACTURE This invention relates to a battery separator paper for use in an alkaline battery, for example an alkaline manganese battery (paper for this purpose is sometimes also referred to as battery component paper). Such a separator may be made from a porous or microporous single or multiple layered electrically non-conductive non-woven fibrous material. The material used for the separator should desirably have the following properties:1. Porous nature which will allow a low internal resistance within the battery whilst maintaining the required storage and service life (these characteristics are to some extent incompatible in that whereas the presence of pores affords the conductivity necessary for low internal resistance, they also give rise to the danger of shorting as a result of dendritic growth through the pores which reduces battery life - it is therefore necessary to select a suitable compromise). 2. The chemical strength to withstand stresses arising during assembly of the battery, for example folding and insertion into a battery can. 3. Dimensional stability in an alkaline environment. 4. Wettability by the electrolyte. 5. Absorbency with respect to the electrolyte. 6. Resistance to degradation by electrolyte or other battery chemicals. For certain types of alkaline battery, in which a separator of preformed shape is employed, it is in addition desirable that the separator material should be heat sealable, so as to facilitate the preforming operation. One widely used type of conventional alkaline battery separator comprises one or more layers of non-woven fibrous material. This conventional material utilises expensive synthetic fibres and, by virtue of the forming process is expensive to produce. A wet-laid paper made from cellulose fibres, either alone or in a blend with synthetic fibres, e.g. polyolefin fibres, might at first sight be thought to afford a route to a cheaper battery paper. However, although such paper has absorbency, it has a high shrinkage in alkaline solution. Proposals have been made to form an alkaline battery separator from a paper web formed by conventional papermaking techniques from a blend of polyolefin synthetic pulp fibres and other synthetic fibres, see for example UK Patent Application No. 2057028A, which also requires the presence of an alkali-resistant inorganic filler, and UK Patent Application No. 2034365A. Heat bonding is either a preferred or essential feature of these proposals and would be expected to be a drawback in view of the difficulty of controlling the degree of heat bonding so as to achieve reproducible separator properties. Papers derived from a blend of polyolefin synthetic pulp fibres and other synthetic fibres have also been proposed for separators of acid batteries; However it should be appreciated that conventional lead-acid and secondary alkaline battery systems have certain components such as electrodes, electrolytes, separators, etc., which, though commonly named, are distinctly different entities having different functions and are required to have different physical and chemical properties. It has now been found that a good alkaline battery separator paper may be made from a blend of polyolefin synthetic pulp fibres and other fibres without heat bonding if an alkali-resistant hydrophilic binder is used to bond the fibres together. No filler need be used. According to a first aspect of the invention, there is provided battery separator paper for use in an alkaline battery, comprising a blend of polyolefinic synthetic pulp fibres and alkali-resistant fibres which are effective to reinforce the polyolefinic fibres, characterized in that the synthetic pulp fibres are not substantially heat bonded to each other or to the reinforcing fibres but are bonded to each other and the reinforcing fibres by means of an alkali-resistant hydrophilic binder which is present in an amount additional to any such binder which may have been present in said synthetic pulp fibres or the reinforcing fibres. According to a second aspect of the invention, there is provided a process for forming a battery separator paper for use in an alkaline battery, comprising the steps of forming a wet-laid paper web from a blend of polyolefinic synthetic pulp fibres and alkali-resistant fibres which are effective to reinforce the polyolefinic fibres, and drying the web thus formed, characterized in that in applying heat to dry or otherwise treat the web, the conditions are such that the synthetic pulp fibres do not become substantially heat bonded to each other or to the reinforcing fibres and in that an alkali-resistant hydrophilic binder is incorporated in the web in an amount additional to any such binder which may already be present in said synthetic pulp fibres or the rein for cing fibres. The invention also resides in a battery separator made using battery paper according to said first aspect of the invention and in an alkaline battery incorporating such a separator. By "polyolefinic synthetic pulp fibres" is meant polyolefinic fibres of the kind specially produced for use in papermaking and which exhibit a high degree of fibrillation (in contrast to chopped staple fibres). Suitable fibres, for example are those supplied under the names "Pulpex" by Solvay, "SWP" by Crown Zellerbach, "Hostapulp" by Hoechst and "Ferlosa" By Montedison. The polyolefin fibres are preferably polyethylene fibres but polypropylene fibres may be used. Polyethylene fibres have so far been found to afford better pore size characteristics. Since polyolefins are hydrophobic in nature, it is necessary for synthetic pulp fibres to be specially modified to make them water-dispersible. Such modification may take the form of a coating of hydrophilic material on each fibre. The hydrophilic material may be a chemical of the kind used in papermaking binders - hence the emphasis above on the presence or incorporation of additional binder. The reinforcing fibres are preferably polyvinyl alcohol fibres, although rayon, PVC, nylon or other chemically resistant fibres may be used. The reinforcing fibres are conveniently chopped staple fibres, but in principle need not be. The reinforcing fibres may be chopped staple polyolefinic fibres. As stated above, it is important to avoid heat bonding in making the present battery paper. This has been found to result in alteration of the microfibrillar structure of the web - the individual fibres shrivel as they are heated causing the pore size to increase. This then encourages dendrite growth in the battery and also increases the hydrophobicity of the separator. A further disadvantage is that in any event a heat consolidation step is difficult to control and thus reproducible separator properties are difficult to achieve. In contrast, use of a binder for bonding permits relatively easy control of web properties. In order to ensure that heat bonding does not occur, the maximum temperature which the web reaches in drying or other treatment must be carefully controlled so as to be below the softening temperature range of the fibres being used. Clearly the web temperature should be sufficiently below the softening threshold of the lowest softening fibres in the web to prevent heat bonding of the fibres. It is difficult to measure web temperature precisely and so it is convenient to refer to drying cylinder surface temperatures which should normally be maintained at least 10-20 C below the softening threshold. A temperature at least 30 0C below the softening threshold has so far been found preferable. The softening temperature range for polyethylene synthetic pulp is usually about 125-130 0C. For paper made from such pulp drying cylinder temperatures should preferably not exceed about 950C, although higher temperatures, say up to about 105 may be usable. Should it be found that heat bonding is occurring the skilled man will have no difficulty in establishing by routine experiment a temperature at which heat bonding no longer occurs, particularly in view of the guidance given above. For polypropylene, the softening range is about 160-165 C and so the web temperature should desirably not exceed about 130 C., although higher temperatures may be tolerated. Preferably the polyolefinic synthetic pulp is present in an amount of from about 30% to about 85% by weight of the total fibre content of the paper. Preferably, the added binder, i.e. the binder additional to any binder material present in the synthetic pulp fibres or the reinforcing fibres as supplied, is present in an amount of at least about 2 by weight based on the total weight of the web. The preferred binder is polyvinyl alcohol, in which case the added binder amount is preferably around 5-15% by weight, based on the total weight of the web. Preferably the binder is incorporated in the web by size press application, although other methods may be employed, for example gravure roll application, spraying or impregnation. At least a proportion of the binder may be added to the stock before web formation. It may also be desirable to add a surfactant to enhance the wettability of the separator. The surfactant should be selected so as not to inhibit the chemical reactions which take place within the battery cells. The surfactant is preferably added with the binder to the stock before web formation or subsequently to the dry sheet. The paper preferably incorporates a small amount of a wet-strength agent. It has been found that the use of a filler, either as a loading or fibre inclusion, is not required in the present separator paper. However, such a filler may if desired be employed, provided it is not detrimental to the separator properties. Preferably the density of the present paper is increased by pressing. The preferred density is in the range from -3 0.170 g cm to 0.335 g cm The maximum pore diameter and air resistance of the paper may vary widely, as will be seen from the Examples hereafter. This is advantageous because the battery maker is provided with a wider variety of papers having different properties thus giving a wider scope for battery design. The separator may comprise one ply of the present paper, or more than one ply. In the latter case the plies are preferably of the same paper, but need not be. An advantage of a multiply separator is that each ply may have a large pore size so as to afford good conductivity and a low internal resistance, since the presence of several plies means that coincidence of large holes (which might promote shorting) is avoided. The plies may be separately formed on a Fourdrinier papermachine or a Rotiformer or may be made in one step by the use of, for example, a secondary headbox. The total grammage of the separator is preferably in the -2 range 30 to 100 gm 2 and more preferably in the range 60-100 gm which may be made up, for example of -2 -3 3 x 20 gm 2 sheets or 2 x 50 g cm 3 sheets or may be a single sheet of that grammage. By suitably choosing the grammage, density, fibre furnish and the binder, a separator paper of good handleability and desired physical properties (e.g. absorbency, porosity etc.) can be obtained. Guidance as to this choice may be obtained from the Examples given later. The present battery paper affords the advantages of cheapness, and, when converted into a separator and used in an alkaline battery affords good storage and shelf life, and good discharge rate. The invention will now be illustrated by reference to the following examples. Example 1 A number of sheets of battery paper of nominal grammage -2 90 gm 2 were prepared on a standard laboratory sheet machine from 0.5% consistency stock comprising 70% polyethylene fibres ("Pulpex A" marketed by Solvay), 30% polyvinyl alcohol fibres ("Mewlon F" marketed by Unitakei Ltd.), and a wet strength agent ("Kymene" marketed by Hercules) added in an amount of 2% based on the total fibre content. The resulting sheets were pressed in the wet state and then subjected to three different pressing treatments using laboratory pressing equipment to produce sheets of low, medium and high density. In all three cases the sheet was then dried on a rotary drier (at a surface temperature of approximately 950C). A laboratory size press was then used to add polyvinyl alcohol binder to give a 15% dry pick up (the binder used was that supplied as "Mowiol 4-98" by Hoechst Aktiengesellschaft in 10% solids content solution. The physical properties of each sheet were tested in all three cases to give the following results as shown in Table 1. TABLE 1 EMI9.1 <tb> Physical <SEP> properties <SEP> Sample <tb> <SEP> Low <SEP> Medium <SEP> High <tb> <SEP> Density <SEP> Density <SEP> Dens <SEP> it <tb> Grammage <SEP> (gm <SEP> <tb> Thickness <SEP> SIG <SEP> m <SEP> 530 <SEP> 450 <SEP> 330 <tb> Density <SEP> gcm <SEP> 3 <SEP> 0.174 <SEP> 0.207 <SEP> 0.272 <tb> Tensile <SEP> N/25 <SEP> mm <SEP> 64 <SEP> 56 <SEP> 60 <tb> <SEP> * <SEP> <tb> Air <SEP> Resistance <SEP> mm <SEP> W.G. <SEP> 122 <SEP> 143 <SEP> 246 <tb> Max <SEP> Pore <SEP> Diameter <SEP> pm <SEP> 30 <SEP> 23 <SEP> 18 <tb> Klemm <SEP> Absorbency <SEP> 30% <SEP> 24 <SEP> 20 <SEP> 19 <tb> <SEP> -l <tb> <SEP> KOH <SEP> mm. <SEP> min <tb> This is a measure of the porosity of the paper. The dimensional stability of each paper in 30% potassium hydroxide solution at 70 0C for 48 hours was also tested (this is intended to afford an indication of how the paper would withstand an alkaline environment over a long period of time when incorporated in a battery). In each case the papers were found to be stable. Example 2 This Example illustrates the use of a different furnish from that used in Example 1. The battery paper was made in the same way as the low density paper in Example 1 except that the furnish used consisted of 85% polyethylene fibres with 15% polyvinyl alcohol fibres. The physical properties of the resulting sheet are shown in Table 2. TABLE 2 EMI10.1 <tb> <SEP> Physical <SEP> properties <SEP> Sample <tb> Grammage <SEP> (gm <SEP> 2) <SEP> <SEP> 90 <tb> Thickness <SEP> SIG <SEP> pm <SEP> 495 <tb> <SEP> -3 <tb> Density <SEP> gcm <SEP> - <SEP> 0.182 <tb> Tensile <SEP> N/25 <SEP> mm <SEP> 44 <tb> Air <SEP> resistance <SEP> mm <SEP> W.G. <SEP> 163 <tb> Max. <SEP> Pore <SEP> Diameter <SEP> pm <SEP> 19.5 <tb> Klemm <SEP> Absorbency <SEP> 18 <tb> <SEP> 30% <SEP> KOH <SEP> mm <SEP> min <SEP> <tb> The paper was also tested for stability in potassium hydroxide as described in Example 1 above and was found to be stable. Example 3 This example illustrates the use of papers of different grammage and varying density. The procedure was generally as described in Example 1 and the results are shown in Table 3. TABLE 3 EMI11.1 <tb> Physical <SEP> properties <SEP> Sample <tb> Grammage <SEP> gm-ê <SEP> 62.5 <SEP> 62 <SEP> 78 <SEP> 77 <tb> Thickness <SEP> SIG <SEP> pm <SEP> 300 <SEP> 230 <SEP> 340 <SEP> 255 <tb> <SEP> -3 <tb> Density <SEP> gem <SEP> - <SEP> 0.208 <SEP> 0.269 <SEP> 0.229 <SEP> 0.302 <tb> Tensile <SEP> N/25 <SEP> mm <SEP> 45 <SEP> 44 <SEP> 54 <SEP> .47.5 <SEP> <tb> Air <SEP> Resistance <SEP> mm <SEP> W.G. <SEP> 185 <SEP> 264 <SEP> 205 <SEP> 277 <tb> Max. <SEP> Pore <SEP> Diameter <SEP> pm <SEP> <SEP> 30.7 <SEP> 23.8 <SEP> 28.4 <SEP> 23.3 <tb> Klemm <SEP> absorbency <SEP> 30% <SEP> 20 <SEP> 25 <SEP> 20 <SEP> 28 <tb> <SEP> KOH <SEP> mm <SEP> min <SEP> 1 <SEP> <tb> Each sheet was also tested -! stability in potassium hydroxide as described in Example 1 above and in each case it was found to be stable. Example 4 This example illustrates the use of different reinforcing fibres and different furnishes. The procedure was generally as described in Example 1 except that rayon was used in place of polyvinyl alcohol fibres and in combination with polyvinyl alcohol fibres. The following furnishes were tested Sample (1) 70% Pulpex A 30% 6mm 1.5 den. Rayon Sample (2-) 30% Pilpex A 45% Short-fibre Rayon 25% 6mm. 1.5 den. Rayon Sample (3) 30% Pulpex A 45% Short-fibre Rayon 25% Polyvinyl'alcohol fibre Sample (4) 50% Pulpex A 30% Polyvinyl alcohol fibre 20% Short-fibre Rayon The results are shown in Table 4. TABLE 4 EMI12.1 <tb> Physical <SEP> properties <SEP> Sample <tb> <SEP> (1) <SEP> (2)- <SEP> <SEP> (3) <SEP> (4) <SEP> <tb> <SEP> <tb> <SEP> Grammage <SEP> gm <tb> Thickness <SEP> <SEP> (SIG) <SEP> jim <SEP> <SEP> 305 <SEP> 305 <SEP> 295 <SEP> 230 <tb> <SEP> density <SEP> <SEP> gem <SEP> 3 <SEP> <SEP> 0.246 <SEP> 0.24 <SEP> 0.258 <SEP> 0.217 <tb> Tensile <SEP> <SEP> N/25mm <SEP> 28 <SEP> 30 <SEP> 54 <SEP> 20 <tb> <SEP> Air <SEP> Resistance <SEP> 426 <SEP> 67 <SEP> 69 <SEP> 96.7 <tb> <SEP> Max <SEP> . <SEP> Pore <SEP> Diameter <SEP> m <SEP> 18.3 <SEP> 40.4 <SEP> 40.7 <SEP> 35.3 <tb> <SEP> Klemm <SEP> Absorbency <SEP> 18 <SEP> 22 <SEP> 25 <SEP> 29 <tb> <SEP> 30% <SEP> KOH <SEP> mm <SEP> min <tb> Each sheet was also tested for stability in potassium hydroxide as described in Example 1 above and in each case it was found to be stable. Example 5 This example illustrates the effect of wet pressing on density and pore size. A furnish of 30% Pulpex A and 70% 6 mm 1.5 den rayon was made into two samples and one subjected to light pressing and the other to more heavy pressing. The results are shown in Table 5. TABLE 5 EMI13.1 <tb> <SEP> Sample <tb> Physical <SEP> Properties <SEP> Light <SEP> Heavy <tb> <SEP> pressing <SEP> pressing <tb> <SEP> -2 <SEP> 75 <SEP> 77 <tb> Grammage <SEP> gm <tb> Thickness <SEP> (SIG) <SEP> um <SEP> 330 <SEP> 230 <tb> Density <SEP> gem <SEP> 3 <SEP> <SEP> 0.227 <SEP> 0.334 <tb> Tensile <SEP> N/25 <SEP> mm <SEP> 41 <SEP> 49 <tb> Air <SEP> resistance <SEP> mm <SEP> WG <SEP> 38 <SEP> 112 <tb> Max. <SEP> Pore <SEP> Diam. <SEP> um <SEP> 49.5 <SEP> 32.0 <tb> Klemm <SEP> Absorbency <SEP> 24 <SEP> 23 <tb> <SEP> 30% <SEP> KOH <SEP> mm <SEP> min <SEP> <tb> Each sheet was also tested for stability in potassium hydroxide as described in Example 1 above and in each case it was found to be stable. When papers produced as described in the above examples were incorporated into test alkaline manganese batteries, they were found to function satisfactorily.

Claims: Claims 1. A battery separator paper for use in an alkaline battery, comprising a blend of polyolefinic synthetic pulp fibres and alkali-resistant fibres which are effective to reinforce the polyolefinic fibres, characterised in that the synthetic pulp fibres are not substantially heat-bonded to each other or to the reinforcing fibres but are bonded to each other and the reinforcing fibres by means of an alkali resistant hydrophilic binder which is present in an amount additional to any such binder which may have been present in said synthetic pulp fibres or the reinforcing fibres. 2. A battery separator paper as claimed in claim 1 characterised in that the polyolefinic synthetic pulp is present in an amount of from about 30% to about 85% by weight of the total fibre content of the paper. 3. A battery separator paper as claimed in claim 1 or 2 characterised in that the alkali-resistant fibres which are effective to reinforce the polyolefinic fibres are of polyvinyl alcohol, rayon, PVC or nylon. 4. A battery separator paper as claimed in any preceding claim characterised in that the alkali-resistant hydrophilic binder is polyvinyl alcohol. 5. A battery separator paper as claimed in any preceding claim characterised in that the alkali-resistant hydrophilic binder is present in an additional amount of at least 2%. 6. A battery separator paper as claimed in any preceding claim characterised in that the total grammage of the separator is in the range from 60 gm to 100 gm 7. A battery separator paper as claimed in any preceding claim characterised in that the density of the separa tor is in the range from 0.170 gem 3 to 0.335 gem 3. 8. A process for forming a battery separator paper for use in an alkaline battery, comprising the steps of forming a wet-laid paper web from a blend of poly olefinic synthetic pulp fibres and alkali-resistant fibres which are effective to reinforce the poly olefinic fibres, and drying the web thus formed, characterised in that in applying heat to dry or otherwise treat the web, the conditions are such that the synthetic pulp fibres do not. become substantially heat-bonded to each other or to the reinforcing fibres and in that an alkali-resistant hydrophilic binder is incorporated in the web in an amount additional to any such binder which may already be present in said synthetic pulp fibres or the reinfor cing fibres. 9. A process as claimed in claim 8 characterised in that the binder is applied to the web by means of size press treatment. 10. A process as claimed in claim 8 or 9 characterised in that the polyolefinic synthetic pulp is present in an amount of from about 30 to about 85% by weight of the total fibre content of the paper. 11. A process as claimed in any of claims 8 to 10 charac terised in that the alkali-resistant fibres which are effective to reinforce the polyolefinic fibres are of polyvinyl alcohol, rayon, PVC or nylon. 12.A process as claimed in any of claims 8 to 11 charac terised in that the alkali-resistant hydrophilic binder added is polyvinyl alcohol. 13.A process as claimed in any of claims 8 to 12 charac terised in that the alkali-resistant hydrophilic binder is added in an amount of at least 25. 14.A battery separator for use in an alkaline battery formed from a battery separator paper as claimed in any of claims 1 to 7. 15.An alkaline battery having a separator as claimed in claim 14.

Inventors: DREW, QUENTIN MILES, NICHOLAS, ROGER PHILIP
Applicants: THE WIGGINS TEAPE GROUP LIMITED
Application year: 1982
Main classification: H01M2
IPC codes: H01M2