JPH07302583A - Nonwoven fabric for alkaline battery separator and its manufacture - Google Patents

Abstract

PURPOSE:To provide a nonwoven fabric for an alkaline battery separator with high absorbency and retainability of an electrolyte in spite of low basic weight and provide its manufacturing method. CONSTITUTION:Organic fibers mainly comprise split type composite fibers obtained by joining polyolefin polymer and ethylene vinyl alcohol copolymer and fibrillating polyolefin fibers with a water filtering value of 20sec or more. Preferably, the fibrillating polyolefin fiber is treated by using a high pressure homogenizing device. The split type composite fibers are split to extra fine fibers in water with a macerating machine, then dispersed together with the fibrillating polyolefin fibers to form slurry, the slurry is treated with a paper machine in a wet paper machine process to form a web, then both surfaces of the web are treated with corona discharge.

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an alkali which is interposed between the positive and negative electrodes of an alkaline battery to prevent a short circuit between them and to sufficiently hold an electrolytic solution to smoothly promote an electromotive reaction. The present invention relates to a non-woven fabric for a battery separator and a method for producing the same, and more particularly to improving the liquid retention of an electrolytic solution.

[0002]

2. Description of the Related Art Alkaline batteries are widely used in electronic devices which are remarkably miniaturized and lightweight because they are excellent in charge / discharge characteristics and overcharge / overdischarge characteristics and can be repeatedly used with a long life. The characteristics of such an alkaline battery largely depend on the characteristics of the nonwoven fabric for an alkaline battery separator.

Therefore, conventionally, a polyamide fiber non-woven fabric, which is easily wet with an electrolytic solution, has a large liquid retention amount, and has a low electric resistance in a state of containing the electrolytic solution, has been used as a non-woven fabric for an alkaline battery separator. Further, for an alkaline battery which requires durability at a relatively high temperature, a polyolefin fiber nonwoven fabric is used as a nonwoven fabric for an alkaline battery separator.

However, the non-woven fabric for an alkaline battery separator made of the above-mentioned polyamide fiber non-woven fabric has a drawback that nitrogen oxide is eluted from the polyamide fiber by repeated use and the life of the alkaline battery is shortened. Further, the non-woven fabric for alkaline battery separators made of polyamide fiber non-woven fabric produces nitrate radicals when oxidized due to nitrogen contained in the polyamide, which easily causes self-discharge and also causes corrosion of electrodes. There was a problem of inviting.

On the other hand, a nonwoven fabric for an alkaline battery separator made of a polyolefin fiber nonwoven fabric has a drawback that it is difficult to wet with an electrolytic solution because of its hydrophobicity, and its liquid retention amount is small. The non-woven fabric for an alkaline battery separator may be subjected to a surfactant treatment or the like, but the surfactant has a problem in the electrolytic solution resistance, and if it is used in a cycle, it may take a certain period of time. Since the surfactant is liberated when it passes, the liquid absorbing property and liquid retaining property of the electrolytic solution have not been sufficiently improved.

Recently, an ethylene vinyl alcohol-based copolymer component has been provided for the purpose of improving both the electrolytic solution resistance and the electrochemical oxidation resistance, and the wettability of the electrolytic solution and the liquid retaining property thereof. Organic fibers have been used.

As a typical example thereof, Japanese Patent Laid-Open No. 25775/1993
Japanese Patent Laid-Open No. 5 (1993) proposes an alkaline battery separator containing 35% or more of splittable conjugate fibers of a polyolefin polymer and an ethylene vinyl alcohol copolymer. This splittable conjugate fiber generates ultrafine fibers after splitting, which increases the specific surface area of the web, so that the alkaline battery separator using this splittable conjugate fiber can improve the electrolyte retention property. However, during production, specifically, during wet paper drying in the wet papermaking method, or during heat fusion such as a heat calender in the dry method, the ethylene vinyl alcohol copolymer fibers generated after division are melted to form a film. Or the generation of polyolefin polymer fibers after splitting, greatly impairs the electrolyte absorbability. As a result, in the alkaline battery separator consisting only of these splittable conjugate fibers, unless impregnated with a surfactant or the like, there is no affinity for the electrolytic solution, and the liquid absorbing property of the electrolytic solution and its retained amount are There is a drawback that it becomes insufficient.

[0008]

SUMMARY OF THE INVENTION The present inventors have proposed Japanese Patent Application No. 5-300732, which has solved the above-mentioned drawbacks of the prior art. In the present invention, the main component of the organic fiber is a splittable conjugate fiber in which a polyolefin polymer and an ethylene vinyl alcohol copolymer are joined, or a splittable conjugate fiber and a polyolefin fiber, and among the organic fibers, the splittable conjugate fiber is Was dispersed in water with a disintegrator to form ultrafine fibers, or a mixture of this and an aqueous dispersion of polyolefin fibers was used as a papermaking slurry, and the papermaking slurry was made into paper by a wet papermaking method to form a web. By forming and subjecting both sides of the web to a very high energy corona discharge treatment, the affinity between the nonwoven fabric for alkaline battery separator and the electrolytic solution is enhanced, and the extremely excellent electrolytic solution absorbing and retaining properties Can be achieved. However, Japanese Patent Application No. 5-30073
Even if the affinity for the electrolytic solution is given by No. 2, since the fiber diameter after splitting of the splittable conjugate fiber is fixed, the liquid retention cannot be improved beyond a certain level. Further improvement of liquid retention is required to achieve high-performance, high-performance, high reliability, etc. required for cordless equipment.

The object of the present invention is to obtain a Japanese patent application No. 5-300732.
The present invention provides a non-woven fabric for an alkaline battery separator, which has further excellent liquid retention property than the non-woven fabric for an alkaline battery separator obtained from the method for producing a non-woven fabric for an alkaline battery separator of No. 1, and its manufacturing method.

[0010]

As a result of intensive research aimed at achieving the above object, the inventors of the present invention have invented a nonwoven fabric for an alkaline battery separator and a method for producing the same.

That is, in the non-woven fabric for alkaline battery separator of the present invention, the main component of the organic fiber is a split type composite fiber in which a polyolefin polymer and an ethylene vinyl alcohol copolymer are joined, and a fibril having a drainage value of 20 seconds or more. It is characterized in that it is composed of a modified polyolefin fiber.

Further, the fibrillated polyolefin fiber is characterized by being treated by using a high pressure homogenizer.

The method for producing a non-woven fabric for an alkaline battery separator of the present invention is a split type composite fiber obtained by joining a polyolefin polymer and an ethylene vinyl alcohol copolymer, and a fibrillated polyolefin fiber having a drainage value of 20 seconds or more. Which is made into ultrafine fibers by dividing the splittable conjugate fiber in water by a disintegrator, and then dispersed together with the fibrillated polyolefin-based fiber to form a slurry, and the slurry is made into a paper by a papermaking method to form a web. It is characterized by being formed and then subjected to corona discharge treatment on both sides of the web.

Hereinafter, the nonwoven fabric for alkaline battery separators and the method for producing the same of the present invention will be described in detail.
First, each organic fiber used in the present invention will be described.

The splittable conjugate fiber in the present invention is a conjugate fiber obtained by joining a polyolefin polymer and an ethylene vinyl alcohol copolymer.

The ethylene-vinyl alcohol copolymer forming the splittable conjugate fiber can be obtained by saponifying a copolymer of ethylene and vinyl acetate. From the viewpoint of liquid retention, MFR (Melt Fluorate, JIS-K7210,
Measured at a temperature of 210 ° C) 20-100 ethylene
It is preferably contained in an amount of up to 45 mol%, and from the viewpoint of spinnability, the saponification degree is preferably 98% or more.

The polyolefin polymer forming the splittable conjugate fiber is preferably a polyolefin such as polyethylene or polypropylene, and particularly MFR10-100.
Of polyolefins are preferred.

In the cross section of the splittable conjugate fiber, one component of the ethylene vinyl alcohol copolymer and the polyolefin polymer is interposed between the other components and split into at least two or more parts, Is a structural unit of the fiber cross section, and a part of each adjacent structural unit is exposed on the fiber surface. The mixing ratio of both components of the polyolefin polymer and ethylene vinyl alcohol copolymer can be changed according to the purpose.When a nonwoven fabric having a large liquid retention property is desired, increase the ratio of the ethylene vinyl alcohol copolymer component and In order to improve the durability, it is preferable to increase the ratio of the polyolefin polymer component. The ratio of both components is not particularly limited, but considering the spinning workability in the spinning step and the affinity for the electrolytic solution, the mixing ratio of both components of the polyolefin polymer: ethylene vinyl alcohol copolymer is 35 : 65-65:
About 35 is preferable.

The fibrillated polyolefin fiber in the present invention is a fiber obtained by highly fibrillating polypropylene fiber, polyethylene fiber, or core-sheath type, side-by-side type, sea-island type, and split type polyolefin fiber.
The shape is such that the fiber diameter is 0.1 to 1 μm by microscopic observation.
And the fiber length measured according to TAPPI T232hm-85 is 0.2-1 mm.

As a general method for fibrillating organic fibers, the following method can be mentioned. 1) A method of causing a synthetic polymer solution to flow into a poor solvent for the polymer while applying a shearing force to precipitate fibrous fibrils (fibrid method, Japanese Patent Publication No. 35-11851). 2) A method of precipitating fibrils by shearing while polymerizing a synthetic monomer (polymerization shearing method, Japanese Patent Publication No. 47-218).
98) 3) A method of mixing two or more kinds of incompatible polymers, melt-extruding or spinning them, and fibrillating them by mechanical means after cutting (split method, JP-B-35-9651).
Issue). 4) A method in which two or more incompatible polymers are mixed, melt-extruded, or spun, cut and then immersed in a solvent to dissolve one polymer, and to fibrillate into a fibrous form (polymer-blend dissolution method). , U.S. Pat. No. 3,382,305). 5) A method in which a synthetic polymer is explosively ejected from the high-pressure side to the low-pressure side above the boiling point of its solvent and then fibrillated into a fibrous state (flash spinning method, JP-B-36-1646).
No. 0). 6) A method in which a polyester polymer is blended with an insoluble alkali-soluble component in the polyester, and after molding, the mixture is reduced with an alkali and beaten to form fibrils (alkaline weight loss beating method, JP-A-56-315). (Gazette) 7) A method in which highly crystalline and highly oriented fibers such as Kevlar fibers are cut into suitable fiber lengths, dispersed in water, and fibrillated using a homogenizer, a beater, etc. (JP-A-56-1)
No. 00801, JP-A No. 59-92011).

In order to fibrillate the organic fiber, it can be produced by the above-mentioned method. As a method for producing the fibrillated polyolefin fiber used in the present invention,
Those produced by the method 7) are particularly preferable. For example, a polyolefin fiber is pulverized to a maximum length of 5 mm or less, more preferably 3 mm or less, and the raw material is used to disperse the fiber in water to obtain a suspension. The concentration of the suspension is 25% at maximum in weight percentage, preferably 1 to 10%, and more preferably 1 to 2%. This suspension is introduced into a high-pressure homogenizer for the production of emulsions and dispersions, at least 100 kg / c
A pressure of m ² , preferably 200 to 500 kg / cm ² , more preferably 400 to 500 kg / cm ² , is applied and repeatedly passed through the homogenizer. During this period, the shear force generated by colliding against the vessel wall at high speed and rapidly decelerating is applied to the polyolefin fiber, but the effect is torn mainly in the direction parallel to the fiber axis and given as a loosening force,
The fibers gradually become fibrillated.

The drainage value of the fibrillated polyolefin fiber fibrillated by the above method is preferably 20 seconds or more. Particularly preferably, the drainage value of the fibrillated polyolefin fiber is 35 seconds to 60 seconds.

The drainage value referred to in the present invention is a value for evaluating the drainage of pulp obtained by the following test method.
That is, the fibrillated polyolefin fiber is adjusted to a 0.3% aqueous dispersion (20 ° C.), and 1 liter of this is collected. The time required for obtaining 500 ml of the filtrate when the slurry was transferred to a cylindrical container having an inner diameter of 102 mmφ (a wire mesh of 80 mesh was stretched on the bottom) was indicated as a drainage value.

When the drainage value of the fibrillated polyolefin fiber is lower than 20 seconds, the amount of the fibrillated polyolefin fiber may be increased in order to improve the liquid retention of the nonwoven fabric for alkaline battery separator. There is a problem that the breathability of the nonwoven fabric for an alkaline battery separator is impaired and the strength is weakened.

Among the methods for fibrillating polyolefin fibers, the above method 7) is the best method for obtaining a drainage value of 20 seconds or more. The drainage value is 60
Seconds. When a fibrillated polyolefin fiber having a drainage value of 35 to 60 seconds is used, other physical properties other than the liquid retention required for the nonwoven fabric for alkaline battery separator are used even if the amount of the fibrillated polyolefin fiber is small. It is possible to improve the liquid retaining property of the nonwoven fabric for alkaline battery separators without significantly impairing the above.

When the non-woven fabric for an alkaline battery separator of the present invention is manufactured, the compounding ratio of the splittable conjugate fiber and the above-mentioned polyolefin fiber is 80 from the viewpoints of liquid absorbing property, liquid retaining property and strength of the electrolytic solution. It is preferable to manufacture it in an amount of up to 95% by weight and 20 to 5% by weight.

Regarding the fiber diameter of the splittable conjugate fiber used in the present invention, it is preferable to use one having a fiber diameter after splitting of 1 to 5 μm in view of the relationship between the basis weight and the liquid retaining property when the web is formed.

Further, the fiber length of the splittable conjugate fiber used in the present invention is preferably 3 to 15 mm in view of dispersibility and strength of the nonwoven fabric for alkaline battery separator. If the fiber length is longer than 15 mm, the dispersion process in water is difficult, and it is necessary to select an appropriate amount of dispersant and to use it in an appropriate amount. Also, once dispersed, it aggregates again to cause twisting, entanglement, and deception. The problem arises that it is easier to do. Also, the dispersion concentration must be lowered, resulting in poor productivity. On the other hand, the fiber length is 3
When the length is shorter than mm, the dispersion process is easy, but it is difficult to obtain a nonwoven fabric for an alkaline battery separator having high strength and high rigidity.

Next, a method for producing the nonwoven fabric for alkaline battery separator of the present invention will be described. The method for producing a non-woven fabric for an alkaline battery separator of the present invention comprises a splittable conjugate fiber in which a polyolefin polymer and an ethylene vinyl alcohol copolymer are joined and a fibrillated polyolefin fiber having a drainage value of 20 seconds or more, The splittable conjugate fiber is split in water by a disintegrator to form ultrafine fibers, which is then dispersed together with the fibrillated polyolefin fibers to form a slurry, and the slurry is formed into a web by a papermaking method, and then the web is formed. It consists of subjecting both sides of the web to corona discharge treatment.

As a method for producing a web of a nonwoven fabric for alkaline battery separators, there are known methods such as a wet papermaking method, a card method, a cross layer method and a random weber method. However, a fibrillated polyolefin fiber is blended with a splittable conjugate fiber. To achieve this, it is most preferable to use the wet papermaking method among those methods.

The card method, the cross layer method,
In the random webber method, fibers having a long fiber length can be used, but it is difficult to form a uniform web, the texture is poor, and a spotted pattern is observed when observed with transmitted light. Therefore, there is a problem that a high basis weight is required to prevent a short circuit. Further, the above fibrillated polyolefin fibers are very fine fibers and cannot be made into a web by the dry method.

Further, in the wet papermaking method, the splittable conjugate fiber can be split in the papermaking step, but in the card method, the cross layer method and the random webber method, a means such as a needle punch method or a hydroentanglement method is used. Need to be divided. Moreover, in the needle punch method, it cannot be used in a low basis weight, and even in the hydroentangling method, in the case of the dry method, it is difficult to divide due to the long fiber length, and when treated at high pressure, fibrillated polyolefin fibers are blended. Even if you can do it, there is a problem that you will drop everything.

On the other hand, the wet papermaking method has an advantage that the production speed is higher than that of the above-mentioned method, and fibers having different fiber diameters or a plurality of kinds of fibers can be mixed at an arbitrary ratio in the same apparatus. That is, the wet papermaking method has a wide range of choices such as fiber form, staple form, pulp form, etc., and the usable fiber diameter is 7 μm.
The following ultrafine fibers to thick fibers can be used, and
Even when the splittable conjugate fiber is split, the splittable conjugate fiber can be split almost completely in the disintegration step with a disintegrator such as a pulper, a high-speed mixer, or a beater, and in the dispersion step. This is a method for obtaining a good web.

Therefore, in the present invention, a wet papermaking method is used,
Manufactured a web. For example, the splittable conjugate fiber in which a polyolefin polymer and an ethylene vinyl alcohol copolymer are joined is split in water with a high-speed mixer to generate ultrafine fibers, which are then mixed with an aqueous dispersion of fibrillated polyolefin fibers. Then, it is made into a uniform papermaking slurry under mild agitation with an agitator and the like, and the papermaking slurry is made into paper using a paper machine having at least one wire such as a round net, a Fourdrinth wire, and an inclined wire. , Thickness 200μ
A web having a good texture is produced so as to have a thickness of m or less. When the splittable conjugate fiber is split in water by a disintegrator, an appropriate amount of surfactant and defoaming agent may be added.

Next, both sides of the thus obtained web are subjected to corona discharge treatment. Here, when each of the organic fibers described above is used, the web itself has a slight liquid absorbing property or liquid retaining property without corona discharge treatment, but is insufficient for use as a nonwoven fabric for alkaline battery separators. Therefore, a corona discharge treatment is performed for the purpose of imparting further electrolyte absorbing and liquid retaining properties.

This corona discharge treatment is performed by using electrodes connected to a high voltage generator, polyester film, high baron, E
An appropriate gap is provided between the metal rolls covered with P rubber or the like, a voltage of several thousand to tens of thousands of V is applied at a high frequency to generate a high-pressure corona, and the web obtained by the above method is applied at this interval at an appropriate speed. The hydrophilic group reacts with ozone, which generated corona on the web surface, or nitric oxide to generate carbonyl group, carboxyl group, hydroxyl group, and peroxide group. It is thought to have contributed to the improvement.

The corona discharge treatment condition is preferably a total energy per one side of 8.0 to 26.0 KW min / m ² , more preferably 15.0 to 20.
It is preferably 0 kW min / m ² . When the total energy per one surface is less than 8.0 kW min / m ² , the effect of improving the affinity with the electrolytic solution is poor, and the liquid absorption is insufficient for using the web as a nonwoven fabric for alkaline battery separators. Is. On the other hand, the total energy per side is 26.0 KW
If it exceeds min / m ² , the total energy per side is 26.0 kW min / m ^{2 in} terms of the effect of improving the affinity with the electrolyte.
There is almost no change from the above case, and because some organic fibers are decomposed, the web gives off a burning odor.

Next, the corona discharge treated nonwoven fabric for alkaline battery separator is generally subjected to calendar treatment. The reason for carrying out the calendering treatment is to provide three points of adjusting the thickness, smoothing the surface of the web, and expressing rigidity when the web is used as a nonwoven fabric for an alkaline battery separator.

The uncalendered web is thick, soft and fluffy for use as a non-woven fabric for alkaline battery separators.
The workability of battery assembly is significantly deteriorated. In addition, it is preferable that a wetting agent such as a nonionic surfactant is applied or impregnated before the web is calendered. Further, in order to be suitably used as a non-woven fabric for an alkaline battery separator for cordless devices, it is desirable that the non-woven fabric for an alkaline battery separator has a thickness of 140 μm or less as measured by a micrometer.

[0040]

EXAMPLES The present invention will now be described in more detail with reference to examples, but the present invention is not limited to these examples.
In the examples, all parts and% are by weight.

[Preparation of fibrillated polyolefin fiber] A polyethylene fiber having a fiber diameter of 8.7 μm and a fiber length of 3 mm, or a polypropylene fiber having a fiber diameter of 8.8 μm and a fiber length of 3 mm was dispersed at a concentration of 2% by weight to obtain a fiber. Each of the obtained dispersion liquids is homogenized by Gaulin.
15M-8TA) at room temperature, and a pressure of 450 kg / cm ² was applied to pass 25 to 40 times to obtain a suspension of fibrillated polyethylene fibers or fibrillated polypropylene fibers. The drainage value was changed by changing the number of times the dispersion was passed through the homogenizer, and sampling was performed midway to obtain the samples shown in Table 1. The average fiber diameter of the fibrillated polyolefin-based fiber is
Average fiber length was measured according to TAPPI T232hm-85.

[0042]

[Table 1]

Example 1 A crystalline polypropylene component comprising a crystalline polypropylene having an MFR of 40 and an ethylene vinyl alcohol copolymer having an ethylene content of 38 mol%, an MFR of 40 and a saponification degree of 99.6%. A fineness of 3 denier in which the volume ratio of the ethylene vinyl alcohol copolymer component is 50:50,
0.2 denier (3.9 μm) after fiber division, fiber length 5 m
80 parts of a slurry in which the splittable composite fiber of m was divided in water using a high speed mixer to generate ultrafine fibers, and 20 parts of a slurry in which the fibrillated polyethylene fibers of Sample 1 were separately dispersed were mixed and dispersed together. The papermaking slurry was wet-processed on a circular net paper machine to have a basis weight of 41.7 g / m ² and a width of 5
A 0 cm web was made.

Next, on both surfaces of the thus obtained web, electrodes 20 mm × 600 mm, dielectric hyperon 3.
Using 2 mm, the total energy per one side was 17.5 KW min / m ² , and the corona discharge treatment was performed. Finally, calendering was performed at room temperature, and the thickness was measured to be 122 μm with a micrometer having a diameter of 6.3 mm to obtain a nonwoven fabric for alkaline battery separator.

Example 2 Regarding the blending ratio of the organic fiber, the same method as in Example 1 was used except that the splittable conjugate fiber used in Example 1 was changed to 90 parts and the fibrillated polyethylene fiber of sample 2 was changed to 10 parts. A non-woven fabric for alkaline battery separator was obtained.

Example 3 Regarding the compounding ratio of the organic fiber, the same method as in Example 1 was used except that the splittable conjugate fiber used in Example 1 was 93 parts and the fibrillated polyethylene fiber of Sample 3 was 7 parts. A non-woven fabric for alkaline battery separator was obtained.

Example 4 The alkaline battery separator was prepared in the same manner as in Example 1 except that the compounding ratio of the organic fiber used in Example 1 was 80 parts of splittable conjugate fiber and 20 parts of fibrillated polyethylene fiber. A non-woven fabric was obtained.

Example 5 Regarding the blending ratio of the organic fiber, the same method as in Example 1 was used except that the splittable conjugate fiber used in Example 1 was 90 parts and the fibrillated polypropylene fiber of sample 4 was 10 parts. A non-woven fabric for alkaline battery separator was obtained.

Example 6 Regarding the compounding ratio of the organic fiber, the same method as in Example 1 was used except that the splittable conjugate fiber used in Example 1 was changed to 96 parts and the fibrillated polyethylene fiber of sample 3 was changed to 4 parts. A non-woven fabric for alkaline battery separator was obtained.

Example 7 Regarding the compounding ratio of the organic fiber, the same method as in Example 1 was used except that the splittable conjugate fiber used in Example 1 was 78 parts and the fibrillated polypropylene fiber of sample 2 was 22 parts. A non-woven fabric for alkaline battery separator was obtained.

Comparative Example 1 A nonwoven fabric for an alkaline battery separator was obtained in the same manner as in Example 1, except that the splittable conjugate fiber used in Example 1 was changed to 100 parts with respect to the compounding ratio of the organic fiber.

Comparative Example 2 Regarding the compounding ratio of the organic fiber, the same method as in Example 1 was used except that the splittable conjugate fiber used in Example 1 was 80 parts and the fibrillated polyethylene fiber of Sample 5 was 20 parts. A non-woven fabric for alkaline battery separator was obtained.

Comparative Example 3 A non-woven fabric for an alkaline battery separator was obtained in the same manner as in Example 2 except that corona discharge treatment was not performed in Example 2.

Comparative Example 4 In Example 2, the corona discharge treatment was not performed, and before the calendar treatment, 0.15 g / m ² of a nonionic surfactant was impregnated with a size press and dried with a hot air dryer. A non-woven fabric for an alkaline battery separator was obtained in the same manner as in Example 2 except that the treatment with a surfactant was performed.

Comparative Example 5 A current nylon dry type nonwoven fabric (melt spinning type) manufactured by Tonen Kagaku KK was used as a nonwoven fabric for an alkaline battery separator.

The nonwoven fabrics for alkaline battery separators produced in Examples 1 to 7 and Comparative Examples 1 to 5 were evaluated by the following evaluation methods, and the performance evaluation results are shown in Table 2. Evaluation method: [Thickness] To evaluate the thickness, a micrometer is used to measure the thickness (μ
m) was measured and the average value was shown.

[Vertical Tensile Strength] When wound around an electrode plate,
Since it is wound while being pulled in the flow direction, the longitudinal (flow direction) tensile strength (kg / 2 cm width) was measured to evaluate the strength of the alkaline battery separator nonwoven fabric. The tensile strength is JIS-8113, and the nonwoven fabric for an alkaline battery separator is cut into a width of 2 cm and a length of 20 cm, and a load at break with a full scale of 5 kg is measured using a tensilon measuring machine (HTM-100 manufactured by Orientec Co., Ltd.). The measurement was performed 10 times and the average value was shown. The practical level of longitudinal tensile strength of the nonwoven fabric for alkaline battery separator is 2.
The width is 30 kg / 2 cm or more.

[Liquid-absorbing property] The evaluation of the initial liquid-absorbing property of the electrolytic solution includes the absorbing speed of the electrolytic solution (the suction height m per minute m).
m) was measured. The absorption rate of the electrolyte solution was 4 when the three 1.5 cm x 18 cm test pieces were sampled from the flow direction of each sample.
After pre-drying at 0 ± 5 ° C to reduce the moisture content to below the official moisture content, leave the sample in the test room under standard greenhouse conditions, and then weigh the sample at intervals of 1 hour or longer, and measure the mass before and after that. The difference was within 0.1% of the subsequent mass (this state is called water equilibrium state), and then the test piece was caustic potash (KOH) with a specific gravity of 1.3 (20 ° C) at 20 ± 2 ° C. Place a horizontal bar of a predetermined height on the water tank containing the solution, align the lower end of each sample with this horizontal bar and fix it with a pin to hang each sample, and lower the horizontal bar to lower the bottom of each test piece. Is not soaked in the liquid for 5 mm, and after 1 minute, K due to capillary phenomenon
The height at which the OH solution rose was measured. The practical level of the liquid absorption speed of the nonwoven fabric for alkaline battery separator is 2 mm / min or more.

[Terminal liquid retention] Due to the swelling of the electrodes caused by charging and discharging, a large pressure is applied to the non-woven fabric for an alkaline battery separator, so that the electrolytic solution in the non-woven fabric for an alkaline battery separator gradually moves to the positive electrode side or the negative electrode side. To go. In this case, the amount of water retained (g / m ² ) after pressurization was measured as an evaluation of the liquid retaining property of the electrolytic solution of the nonwoven fabric for an alkaline battery separator. The amount of water retained after pressurization is 10 cm x 1 from each sample.
Three test pieces with a size of 0 cm were sampled, and the weight W (g) when in a water equilibrium state was measured, and then 20 ± 1 ° C.
Spread the test piece in the distilled water of No. 1 and leave it for 1 minute, then remove it from the distilled water, immediately sandwich it with filter paper (Advantech No. 26), pass it through a roll press with a linear pressure of 50 Kg / cm, and weigh the test piece W ₁ (g) was measured and calculated by the following formula 1. The practical level of liquid retention at the end of the nonwoven fabric for alkaline battery separator is 17 g / m ² or more. When the final liquid retention in the alkaline battery separator nonwoven fabric is lower than 17 g / m ² , the electrolyte swells from the alkaline battery separator nonwoven fabric due to the swelling of the electrode due to charge and discharge, and the electrolyte gradually migrates to the electrode side and is gradually depleted. Because the internal resistance of the battery increases and the internal pressure increases,
The discharge characteristics of the battery deteriorate.

[0060]

[Equation 1] Amount of water retained after pressurization (g / m ² ) = [(W ₁ −W)
/(0.1×0.1)]

[Alkali resistance] To evaluate the alkali resistance of the non-woven fabric for an alkaline battery separator, the weight loss rate (%) after the alkali treatment was measured. The weight loss rate after alkali treatment is the weight W (m when the water equilibrium state is obtained by collecting three test pieces of 10 cm × 10 cm from each sample.
After measuring g), K of 30% concentration corresponding to the electrolytic solution
Immerse in OH solution and store in an atmosphere of 80 ± 2 ° C. for 7 days. After that, the sample taken out was washed with water and dried until it reached the neutralization point, and the weight W ₂ (m
g) was measured and the weight loss rate (%) after the alkali treatment was calculated by the following equation 2. The practical level of the weight loss rate after alkaline treatment in the nonwoven fabric for alkaline battery separator is
It is 1.5% or less.

[0062]

[Formula 2] Weight loss rate after alkali treatment (%) = [(W-
W ₂ ) / W] × 100

[0063]

[Table 2]

The non-woven fabric for an alkaline battery separator composed of the splittable conjugate fiber generating ultrafine fibers and the highly fibrillated polyolefin-based fiber as shown in each example is the splittable conjugate fiber shown in Comparative Example 1. It is very excellent in the liquid retaining property of the electrolytic solution as compared with the one composed only. Further, compared with the current nylon dry-type nonwoven fabric shown in Comparative Example 6, although the basis weight is about 20 g / m ² less, the electrolyte-absorbing property and liquid retention of the alkaline battery separator nonwoven fabric are reduced. It has excellent properties, especially excellent liquid absorption. Furthermore, since the paper is made by the wet papermaking method, the formation is uniform,
Also has excellent alkali resistance.

The non-woven fabrics for alkaline battery separators of Examples 1 to 3 were prepared by changing the drainage value of the fibrillated polyolefin fiber fiber from 20 seconds to 55 seconds. Even if it is lowered, the liquid retaining property of the electrolytic solution can be greatly improved.

The non-woven fabric for an alkaline battery separator of Example 6 has a fibrillated polyolefin fiber blending ratio of less than 5%. Is hardly improved.

In the non-woven fabric for an alkaline battery separator of Example 7, the fibrillated polyolefin fiber has a longitudinal tensile strength smaller than the practical level, although the blending ratio of the fibrillated polyolefin fiber is more than 20%. It can be seen that the blending ratio of fibers cannot exceed 20%.

The non-woven fabric for an alkaline battery separator of Comparative Example 2 had a drainage value of fibrillated polyolefin fiber of 2
Although it is less than 0 seconds, even if the compounding ratio of the fibrillated polyolefin fiber is 20%, the liquid retaining property of the electrolytic solution is not improved so much.

The non-woven fabric for an alkaline battery separator of Comparative Example 3 was the same as the production method of Example 2 except that it was not subjected to corona discharge treatment. Since the coalesced fibers form a molten film, the liquid absorption and liquid retention of the electrolytic solution of the ethylene vinyl alcohol copolymer component are impaired, and as a result, the liquid retention cannot be evaluated by the above evaluation method, It is understood that the electrolyte absorbing property and the liquid retaining property are very poor, and that it cannot be used as a nonwoven fabric for an alkaline battery separator only by wet papermaking.

In comparison with the manufacturing method of Example 2, the non-woven fabric for an alkaline battery separator of Comparative Example 4 was impregnated with a nonionic surfactant instead of corona discharge treatment.
In the case of giving affinity to the electrolytic solution, when impregnated with a surfactant, although the electrolyte absorbing property in the initial stage is good, there is a problem that the surfactant is released after a certain period of time. It can be seen that compared with Example 2 and that of Example 2, the electrolytic solution is inferior in liquid retaining property and cannot be used as a nonwoven fabric for alkaline battery separators.

[0071]

EFFECT OF THE INVENTION The nonwoven fabric for alkaline battery separator manufactured by the manufacturing method of the present invention has a split type conjugate fiber in which the main component of the organic fiber is a polyolefin polymer and an ethylene vinyl alcohol copolymer, and the drainage value is 20 seconds. Since it is composed of the fibrillated polyolefin-based fibers as described above, it has a high alkali resistance, a low basis weight, and excellent electrolyte absorbing and liquid retaining properties.

As a result, according to the present invention, it is possible to provide a non-woven fabric for an alkaline battery separator which has a low basis weight and is particularly excellent in the liquid absorbing property and liquid retaining property of the electrolytic solution, and a method for producing the same. The non-woven fabric for an alkaline battery separator manufactured by the manufacturing method of 1 can be suitably used for cordless devices that require high characteristics such as high capacity, long life, and high reliability.

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Claims (3)

[Claims] 1. An alkaline battery in which the main component of the organic fiber is a split-type composite fiber in which a polyolefin polymer and an ethylene vinyl alcohol copolymer are joined and a fibrillated polyolefin fiber having a drainage value of 20 seconds or more. Non-woven fabric for separator. 2. A fibrillated polyolefin-based fiber,
It has been processed using a high-pressure homogenizer.
The nonwoven fabric for the alkaline battery separator described. 3. A split type conjugate fiber in which a polyolefin polymer and an ethylene vinyl alcohol copolymer are joined together and a fibrillated polyolefin fiber having a drainage value of 20 seconds or more. After dividing into ultrafine fibers in water, it is dispersed together with the fibrillated polyolefin fibers to form a slurry, and the slurry is paper-formed by a wet papermaking method to form a web, and then corona discharge treatment is applied to both sides of the web. A method for producing a non-woven fabric for an alkaline battery separator, which comprises applying the same.