JPH09320577A - Manufacture of hydrogen absorbing alloy electrode - Google Patents
Manufacture of hydrogen absorbing alloy electrodeInfo
- Publication number
- JPH09320577A JPH09320577A JP8156144A JP15614496A JPH09320577A JP H09320577 A JPH09320577 A JP H09320577A JP 8156144 A JP8156144 A JP 8156144A JP 15614496 A JP15614496 A JP 15614496A JP H09320577 A JPH09320577 A JP H09320577A
- Authority
- JP
- Japan
- Prior art keywords
- absorbing alloy
- powder
- hydrogen storage
- hydrogen absorbing
- electrode
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 229910045601 alloy Inorganic materials 0.000 title claims abstract description 51
- 239000000956 alloy Substances 0.000 title claims abstract description 51
- 239000001257 hydrogen Substances 0.000 title claims abstract description 46
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 46
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 44
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 18
- 239000000843 powder Substances 0.000 claims abstract description 40
- 239000002002 slurry Substances 0.000 claims abstract description 24
- 239000004372 Polyvinyl alcohol Substances 0.000 claims abstract description 17
- 229920002451 polyvinyl alcohol Polymers 0.000 claims abstract description 17
- 239000002562 thickening agent Substances 0.000 claims abstract description 17
- 239000000758 substrate Substances 0.000 claims abstract description 16
- 239000007864 aqueous solution Substances 0.000 claims abstract description 11
- 239000006258 conductive agent Substances 0.000 claims abstract description 9
- 238000004898 kneading Methods 0.000 claims abstract description 5
- 238000001035 drying Methods 0.000 claims abstract 2
- 238000003860 storage Methods 0.000 claims description 41
- 238000010438 heat treatment Methods 0.000 claims description 30
- 239000011248 coating agent Substances 0.000 claims description 8
- 238000000576 coating method Methods 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 238000000465 moulding Methods 0.000 claims 1
- 239000011230 binding agent Substances 0.000 abstract description 11
- 230000006866 deterioration Effects 0.000 abstract description 5
- 239000003795 chemical substances by application Substances 0.000 abstract description 2
- 238000000034 method Methods 0.000 abstract description 2
- 239000000243 solution Substances 0.000 abstract 1
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 14
- 239000010410 layer Substances 0.000 description 7
- 239000000463 material Substances 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- 229910018007 MmNi Inorganic materials 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 4
- 239000001768 carboxy methyl cellulose Substances 0.000 description 4
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 4
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 4
- 229910052759 nickel Inorganic materials 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- 239000008151 electrolyte solution Substances 0.000 description 3
- 238000003825 pressing Methods 0.000 description 3
- 238000004080 punching Methods 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 229910001122 Mischmetal Inorganic materials 0.000 description 2
- 239000002033 PVDF binder Substances 0.000 description 2
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 229920000609 methyl cellulose Polymers 0.000 description 2
- 239000001923 methylcellulose Substances 0.000 description 2
- 235000010981 methylcellulose Nutrition 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- -1 polytetrafluoroethylene Polymers 0.000 description 2
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 2
- 229910000878 H alloy Inorganic materials 0.000 description 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical group OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000007859 condensation product Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229910000474 mercury oxide Inorganic materials 0.000 description 1
- UKWHYYKOEPRTIC-UHFFFAOYSA-N mercury(ii) oxide Chemical compound [Hg]=O UKWHYYKOEPRTIC-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229920006186 water-soluble synthetic resin Polymers 0.000 description 1
- 239000012866 water-soluble synthetic resin Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Landscapes
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、ニッケル・水素二
次電池の負極として用いる水素吸蔵合金電極に関する。TECHNICAL FIELD The present invention relates to a hydrogen storage alloy electrode used as a negative electrode of a nickel-hydrogen secondary battery.
【0002】[0002]
【従来の技術】ニッケル・水素吸蔵電池の負極として用
いられる水素吸蔵電極は、一般に、次のように製造され
る。即ち、MmNi5 又はNiの一部をCo、Al、M
nなどと置換したMmNi系水素吸蔵合金粉末を主体と
し、これにコバルト、銅、ニッケル、カーボンなどの導
電剤粉末と、導電性基板に水素吸蔵合金粉末を塗着させ
るためにこれをペースト状とするために、粘稠剤とし
て、ポリビニルアルコール、メチルセルロース、ポリエ
チレンオキサイド、カルボキシメチルセルロースなどの
水溶性の合成樹脂粉末の少なくとも1種を水に溶解した
増粘剤水溶液とを混練してペースト状スラリーとし、こ
れに更に、導電性基板に塗着された合金粉末が剥離する
ことを防止すると共に、合金粉末相互を強固に結着する
結着剤としてポリテトラフルオロエチレン粉末、ポリプ
ロピレン粉末、ポリビニリデンフルオライド粉末などの
非水溶性の結着剤粉末の少なくとも1種を添加混練した
スラリーを調製し、これを導電性基板に塗着しそのスラ
リー層を形成し、次で乾燥、所定の厚さに加圧成形した
後、加熱炉で結着剤粉末の表面が少なくとも溶融する温
度に、ポリビニリデンフルオライドの場合は150〜2
10℃で、数時間加熱して水素吸蔵合金粉末粒子間を結
合させて合金粉末の脱落のない水素吸蔵合金電極を製造
していた。2. Description of the Related Art A hydrogen storage electrode used as a negative electrode of a nickel-hydrogen storage battery is generally manufactured as follows. That is, MmNi 5 or a part of Ni is replaced with Co, Al, M
Mainly consists of MmNi-based hydrogen storage alloy powder substituted with n or the like, and a conductive agent powder such as cobalt, copper, nickel or carbon, and a paste form for coating the hydrogen storage alloy powder on the conductive substrate. In order to do so, as a thickener, polyvinyl alcohol, methyl cellulose, polyethylene oxide, at least one kind of water-soluble synthetic resin powder such as carboxymethyl cellulose is kneaded with a thickener aqueous solution dissolved in water to form a paste slurry, In addition to this, the polytetrafluoroethylene powder, the polypropylene powder, the polyvinylidene fluoride powder as a binder that prevents the alloy powder coated on the conductive substrate from peeling and firmly bonds the alloy powders to each other. To prepare a slurry in which at least one kind of water-insoluble binder powder such as This is applied to a conductive substrate to form a slurry layer, which is then dried and pressure-molded to a predetermined thickness, and then heated to a temperature at which the surface of the binder powder melts at least in a heating furnace. 150-2 for rides
It was heated at 10 ° C. for several hours to bond the particles of the hydrogen-absorbing alloy powder to each other to manufacture a hydrogen-absorbing alloy electrode without dropping of the alloy powder.
【0003】[0003]
【発明が解決しようとする課題】上記従来の水素吸蔵合
金電極の製造法は、増粘剤とは別個に、非水溶性の結着
剤粉を添加し、均一に混練する煩雑な作業が必要とな
り、また、製造コストの増大をもたらし、更には、これ
による水素吸蔵合金塗着物の導電性基板からの塗着物の
剥落を防止するためには、数時間に亘る長時間の加熱処
理が必要となるばかりでなく、この長時間の加熱によ
り、水素合金粉末の熱劣化が生じ、水素吸蔵特性を著し
く低下させ、これを負極として用いた蓄電池の放電容量
の低下をもたらすなどの不都合が避けられなかった。The above-mentioned conventional method for manufacturing a hydrogen storage alloy electrode requires a complicated work of adding a water-insoluble binder powder separately from the thickener and uniformly kneading. In addition, the production cost is increased, and further, in order to prevent the coating of the hydrogen storage alloy coating from peeling off from the conductive substrate, a long heat treatment for several hours is required. In addition to the above, the heating for a long time causes thermal deterioration of the hydrogen alloy powder, which significantly deteriorates the hydrogen storage characteristics, which inevitably causes a reduction in the discharge capacity of the storage battery using this as an anode. It was
【0004】[0004]
【課題を解決するための手段】本発明は、上記従来の課
題を一挙に解決し、且つ製造容易且つ低コストで製造で
き、而も合金粉末相互結着が強固に得られ且つその塗着
物剥落のない而も水素吸蔵合金の熱劣化がなく、放電容
量の増大した水素吸蔵合金電極の製造法を提供するもの
で、水素吸蔵合金粉末を主体とし、これに添加した導電
剤粉末と少なくともポリビニルアルコールを水に溶解し
た増粘剤水溶液とを混練して得られるペースト状のスラ
リーを、導電性基板に塗着してスラリー層を形成し、乾
燥、所定厚さに加圧成形した後、120〜200℃で1
〜5分加熱処理することを特徴とする。SUMMARY OF THE INVENTION The present invention solves the above-mentioned conventional problems all at once, can be manufactured easily and at low cost, and can firmly obtain alloy powder mutual binding and peel off the adhered material. The present invention provides a method for producing a hydrogen storage alloy electrode having an increased discharge capacity without thermal deterioration of the hydrogen storage alloy, which is mainly composed of hydrogen storage alloy powder, and a conductive agent powder and at least polyvinyl alcohol added thereto. After a paste-like slurry obtained by kneading a thickener aqueous solution in which is dissolved in water is applied to a conductive substrate to form a slurry layer, which is dried and pressure-molded to a predetermined thickness, 120- 1 at 200 ° C
The heat treatment is performed for 5 minutes.
【0005】[0005]
【作用】このように、本発明は、従来、水素吸蔵合金電
極の製造に必要であった非水溶性の結着剤の使用を廃す
るので、電極の製造作業が容易で且つ製造コストの低下
をもたらす。また、ポリビニルアルコールは、当初は、
増粘剤として作用し、スラリーに粘稠剤を付与して導電
性基板への塗着に役立つばかりでなく、120℃〜20
0℃の範囲の加熱でポリビニルアルコールを縮合せし
め、その縮合物は、水素吸蔵合金粉末粒子相互の強固な
結合及び導電性基板への強固な結着性をもたらす非水溶
性で且つ強固な結着剤として役立ち、合金粉末の脱落、
その塗着物の剥離のない安定堅牢で放電特性の向上した
電池をもたらす。As described above, according to the present invention, since the use of the water-insoluble binder, which has been conventionally required for manufacturing the hydrogen storage alloy electrode, is eliminated, the electrode manufacturing work is easy and the manufacturing cost is reduced. Bring In addition, polyvinyl alcohol was originally
It acts as a thickening agent, imparts a thickening agent to the slurry, and serves not only for application to a conductive substrate, but also at 120 ° C to 20 ° C.
Polyvinyl alcohol is condensed by heating in the range of 0 ° C., and the condensate is a water-insoluble and strong bond that causes strong bonding between the hydrogen storage alloy powder particles and strong bonding to the conductive substrate. Serves as an agent, dropping of alloy powder,
A stable and robust battery with no peeling of the adherend and improved discharge characteristics is provided.
【0006】[0006]
【発明の実施の形態】次に、本発明の実施の形態を説明
する。本発明の電極を製造する主原料である水素吸蔵合
金粉末の合金の種類は、MmNi系、LaNi系など従
来公知の全ての種類のものから適当に選択できる。これ
に添加される導電剤としては、従来公知のコバルト粉
末、銅粉末、ニッケル粉末などの所望の金属粉末、カー
ボン粉末から少なくとも1種類を選択使用する。その添
加量は、水素吸蔵合金粉末に対し、重量比で0.5〜2
0%の範囲である。また、粘稠剤としては、少なくとも
ポリビニルアルコール(PVA)は必須であり、必要に
応じ、これにその他の水溶性の粘稠剤として、メチルセ
ルロース、カルボキシメチルセルロース、ポリエチレン
オキサイドなどの公知の粘稠剤の少なくとも1種を併用
することができ、これをイオン交換水や蒸溜水に少なく
ともPVAを0.5〜10wt.%の範囲添加し、溶解
して粘稠剤水溶液として調製したものを使用する。かく
して、水素吸蔵合金粉末を主体とし、これに導電剤粉末
とPVAを少なくとも含む粘稠剤水溶液とを混合し、混
練してペースト状のスラリーを作製する。次に、これを
導電性基板に塗着し、そのスラリー層を形成する。導電
性基板としては、無孔の金属箔、無孔の肉薄の金属シー
ト、或いは多孔のパンチングメタルシート、金網状シー
ト、発泡金属などの三次元の微孔金属シートなどが選択
使用される。無孔の導電性基板の場合は、その両面にス
ラリーを均一な厚さに塗布する塗着作業を行い、多孔の
導電性基板の場合は、その多数の孔にスラリーを充填す
ると共にその両面に均一な厚さのスラリー層を形成する
塗布作業を行う。次に、このようにスラリー塗着導電正
極板を、100℃以下の温度で加熱して水分を蒸発させ
てスラリー層を乾燥させた後、一対の加圧ローラを通し
て均一な厚さに加圧成形し、その乾燥充填基板を得た
後、本発明に従い、これを電気炉などの加熱炉内に導入
し、そのまゝ或いは窒素ガス、アルゴンガスなどを導入
した不活性ガス雰囲気下で、或いは内部の空気を吸引除
去した真空減圧下で、120〜200℃の温度で、僅か
1〜5分の短時間加熱した後、常温まで急冷した後、加
熱炉から導出させることにより本発明の水素吸蔵合金電
極が得られる。Next, an embodiment of the present invention will be described. The type of alloy of the hydrogen storage alloy powder, which is the main raw material for producing the electrode of the present invention, can be appropriately selected from all conventionally known types such as MmNi type and LaNi type. As the conductive agent added to this, at least one selected from conventionally known metal powders such as cobalt powder, copper powder, and nickel powder, and carbon powder is selected and used. The amount of addition is 0.5 to 2 by weight ratio with respect to the hydrogen storage alloy powder.
The range is 0%. Further, at least polyvinyl alcohol (PVA) is indispensable as a thickening agent, and if necessary, as another water-soluble thickening agent, a known thickening agent such as methyl cellulose, carboxymethyl cellulose, or polyethylene oxide can be used. At least one kind may be used in combination, and at least 0.5 to 10 wt. %, Added and dissolved to prepare a thickener aqueous solution. Thus, the hydrogen storage alloy powder is mainly used, and the conductive agent powder and the thickener aqueous solution containing at least PVA are mixed and kneaded to prepare a paste slurry. Next, this is applied to a conductive substrate to form a slurry layer thereof. As the conductive substrate, a non-perforated metal foil, a non-perforated thin metal sheet, a perforated punching metal sheet, a wire mesh sheet, or a three-dimensional micro-perforated metal sheet such as foam metal is selectively used. In the case of a non-porous conductive substrate, a coating work is performed to apply the slurry to both sides with a uniform thickness, and in the case of a porous conductive substrate, the slurry is filled in a large number of holes and both sides are filled. A coating operation is performed to form a slurry layer having a uniform thickness. Then, the slurry-coated conductive positive electrode plate is heated at a temperature of 100 ° C. or lower to evaporate water to dry the slurry layer, and then pressure-formed to a uniform thickness through a pair of pressure rollers. Then, after obtaining the dry-filled substrate, according to the present invention, it is introduced into a heating furnace such as an electric furnace, and as it is, or under an inert gas atmosphere in which nitrogen gas, argon gas, etc. are introduced, or inside Of the hydrogen-absorbing alloy of the present invention by heating at a temperature of 120 to 200 ° C. for a short time of only 1 to 5 minutes under a vacuum reduced pressure in which the air of the above is removed by suction, and then rapidly cooling to room temperature and then discharging from a heating furnace. An electrode is obtained.
【0007】120℃以上で加熱する理由は、水素吸蔵
合金塗層中のポリビニルアルコールを結合させ、非水溶
性で且つ結着性の強固な縮合物とすることにある。20
0℃を越えると、合金粉末粒子に熱劣化を生ぜしめるの
で好ましくない。また、その時間を1〜5分と限定する
理由は、上記の加熱温度でポリビニルアルコールの縮合
物を生ぜしめるには、少なくとも1分必要であり、一
方、5分を越える場合は、合金粉末が熱劣化し水素吸蔵
特性などが低下するからである。通常は、導電性基板
は、長尺帯状シートを使用するので、上記の加熱処理
後、所定の極板寸法に切断することにより、選択的に多
数の極板が得られるようにする。The reason for heating at 120 ° C. or higher is to bond the polyvinyl alcohol in the hydrogen storage alloy coating layer to form a water-insoluble and binding strong condensate. 20
If the temperature exceeds 0 ° C, the alloy powder particles will be deteriorated by heat, which is not preferable. Further, the reason for limiting the time to 1 to 5 minutes is that at least 1 minute is required to produce the condensation product of polyvinyl alcohol at the above heating temperature, while if it exceeds 5 minutes, the alloy powder is This is because heat deterioration deteriorates the hydrogen storage characteristics and the like. Usually, since a long strip-shaped sheet is used as the conductive substrate, a large number of electrode plates can be selectively obtained by cutting into a predetermined electrode plate size after the above heat treatment.
【0008】[0008]
【実施例】次に、本発明の具体的な実施例1〜6を、比
較例1〜3及び従来例と共に説明する。 実施例1 組成MmNi3.3 Co0.9 Al0.3 Mn0.4 (Mmはミ
ッシュメタル)の水素吸蔵合金を粉砕して平均粒径60
μmの粉末とし、この粉末100重量部に対し、導電剤
としてニッケル粉末10重量部、粘稠剤としてポリビニ
ルアルコールの5%水溶液20重量部を混練してスラリ
ーを調製した。このスラリーを、パンチングニッケルシ
ート(開口径1.5mm、開口率38%、厚み0.07
mm)の開口に充填すると共にその両面にスラリー層を
形成するように塗着した後、80℃で加熱し、水分を除
去して乾燥し、更に加圧力2ton/cm2 で一対のロ
ールで圧延して全体としての厚み0.4mmの負極板に
した後、加熱炉により温度120〜200℃で1〜5分
空気中で加熱処理を行って下記表1に示す実施例1の水
素吸蔵合金電極を製造した。 実施例2〜6 組成MmNi3.3 Co0.9 Al0.3 Mn0.4 (Mmはミ
ッシュメタル)の水素吸蔵合金を粉砕して平均粒径60
μmの粉末とし、この粉末100重量部に対し、導電剤
としてニッケル粉末10重量部、粘稠剤としてポリビニ
ルアルコールの10%水溶液9重量部とカルボキシメチ
ルセルロースの0.5%水溶液10重量部を混練してス
ラリーを調製した。このスラリーを、パンチングニッケ
ルシート(開口径1.5mm、開口率38%、厚み0.
07mm)の開口に充填すると共にその両面にスラリー
層を形成するように塗着した後、80℃で加熱し、水分
を除去して乾燥し、更に加圧力2ton/cm2 で一対
のロールで圧延して全体としての厚み0.4mmの負極
板にした後、加熱炉により温度120〜200℃で1〜
5分空気中で加熱処理を行って下記表1に示す実施例2
〜6の水素吸蔵合金電極を製造した。EXAMPLES Next, specific examples 1 to 6 of the present invention will be described together with comparative examples 1 to 3 and a conventional example. Example 1 A hydrogen storage alloy having a composition of MmNi 3.3 Co 0.9 Al 0.3 Mn 0.4 (Mm is misch metal) was crushed to obtain an average particle size of 60.
A powder having a size of μm was prepared, and 100 parts by weight of this powder was kneaded with 10 parts by weight of nickel powder as a conductive agent and 20 parts by weight of a 5% aqueous solution of polyvinyl alcohol as a thickening agent to prepare a slurry. This slurry was punched into a nickel sheet (opening diameter 1.5 mm, opening ratio 38%, thickness 0.07).
(mm) opening and apply it on both sides to form a slurry layer, then heat at 80 ° C. to remove water and dry, and further roll with a pair of rolls at a pressing force of 2 ton / cm 2. Then, a negative electrode plate having a total thickness of 0.4 mm is formed, and then heat treatment is performed in air at a temperature of 120 to 200 ° C. for 1 to 5 minutes in a heating furnace to give a hydrogen storage alloy electrode of Example 1 shown in Table 1 below. Was manufactured. Examples 2 to 6 A hydrogen storage alloy having a composition of MmNi 3.3 Co 0.9 Al 0.3 Mn 0.4 (Mm is misch metal) was crushed to obtain an average particle size of 60.
As a conductive agent, 10 parts by weight of nickel powder, 9 parts by weight of a 10% aqueous solution of polyvinyl alcohol and 10 parts by weight of a 0.5% aqueous solution of carboxymethyl cellulose were kneaded with 100 parts by weight of this powder. To prepare a slurry. A punching nickel sheet (opening diameter 1.5 mm, opening ratio 38%, thickness 0.
(07 mm) opening and apply it on both sides to form a slurry layer, then heat at 80 ° C. to remove water and dry, and further roll with a pair of rolls at a pressing force of 2 ton / cm 2. Then, after making a negative electrode plate having a total thickness of 0.4 mm, it is heated at a temperature of 120 to 200 ° C. for 1 to 1
Example 2 shown in Table 1 below after heat treatment in air for 5 minutes
~ 6 hydrogen storage alloy electrodes were produced.
【0008】比較例1〜6 また、比較のため、上記の同じ負極板について、温度1
20〜200℃及び1〜5分のいずれか一方又は両方の
条件をはずれた条件で夫々加熱処理を行い、表1に示す
比較例1〜6の水素吸蔵合金電極を製造した。Comparative Examples 1 to 6 For comparison, the same negative electrode plate as described above was used at a temperature of 1
Heat treatment was carried out under conditions deviating from one or both of 20 to 200 ° C. and 1 to 5 minutes to manufacture hydrogen storage alloy electrodes of Comparative Examples 1 to 6 shown in Table 1.
【0010】従来例 一方、従来例として、下記の製造法により水素吸蔵合金
電極を製造した。実施例1〜5の製造に使用したと同じ
上記の水素吸蔵合金粉末を用い、この粉末100重量部
に対して、導電剤としてニッケル粉末10重量部、粘稠
剤としてカルボキシメチルセルロースの0.5%水溶液
10重量部と結着剤としてポリビニリデンフルオライド
粉末2重量部とを混練してスラリーを調製した。このス
ラリーを、パンチングニッケルシートの開口に充填する
と共にその両面に塗着した後、80℃で加熱し、更に加
圧力2ton/cm2 でロール圧延して全体の厚み0.
4mmの負極板にした後、加熱炉により温度170℃、
60分窒素中で加熱処理を行って水素吸蔵合金電極を製
造した。Conventional Example On the other hand, as a conventional example, a hydrogen storage alloy electrode was manufactured by the following manufacturing method. Using the same hydrogen storage alloy powder as that used in the production of Examples 1 to 5, with respect to 100 parts by weight of this powder, 10 parts by weight of nickel powder as a conductive agent and 0.5% of carboxymethylcellulose as a thickening agent. A slurry was prepared by kneading 10 parts by weight of the aqueous solution and 2 parts by weight of polyvinylidene fluoride powder as a binder. This slurry was filled in the openings of a punching nickel sheet and applied on both sides thereof, then heated at 80 ° C., and further rolled at a pressing force of 2 ton / cm 2 to obtain an overall thickness of 0.
After making a negative electrode plate of 4 mm, the temperature is 170 ° C. in a heating furnace.
A hydrogen storage alloy electrode was manufactured by performing heat treatment in nitrogen for 60 minutes.
【0011】これらの実施例1〜6、比較例1〜6及び
従来例の水素吸蔵電極につき、下記の方法で単極試験を
行い、充分活性化した後の水素吸蔵合金1グラム当たり
の放電容量を測定した。その単極試験は、次のように行
った。即ち、30wt.%の水酸化カリウム水溶液を電
解液とした、対極には金属ニッケル、参照極には酸化水
銀電極、作用極には上記のように作製した水素吸蔵合金
電極を用い、電解液を満たした容器にこれらを入れ、3
0mA/gで充電した後放置し、15時間充電後、水素
吸蔵合金電位が−750mV(vs.Hg/HgO)と
なるまで放電した。続いて、70mA/gで充放電を容
量が安定するまで数サイクル行った後、放電容量を測定
した。また、これらの電極につき、電解液に浸漬し、そ
の際の様子から塗着物の剥落の有無を調べた。その結果
を下記表1に示す。The hydrogen storage electrodes of Examples 1 to 6, Comparative Examples 1 to 6 and the conventional example were subjected to a unipolar test by the following method, and the discharge capacity per gram of the hydrogen storage alloy after being sufficiently activated. Was measured. The monopolar test was performed as follows. That is, 30 wt. % Potassium hydroxide aqueous solution as an electrolytic solution, using metallic nickel as a counter electrode, a mercury oxide electrode as a reference electrode, and a hydrogen storage alloy electrode prepared as described above as a working electrode, in a container filled with the electrolytic solution. Put these in 3
The battery was charged at 0 mA / g, left for 15 hours, and then discharged until the hydrogen storage alloy potential became −750 mV (vs. Hg / HgO). Then, after charging / discharging at 70 mA / g for several cycles until the capacity became stable, the discharge capacity was measured. Further, these electrodes were immersed in an electrolytic solution, and the appearance at that time was examined for the presence or absence of peeling of the coating. The results are shown in Table 1 below.
【0012】[0012]
【表1】 [Table 1]
【0013】上記表1から明らかなように、従来例は、
塗着物の剥落は生じないが、放電容量は、実施例1〜6
に比し低下している。このことは、水素吸蔵合金の吸蔵
特性が熱劣化することを証明する。比較例1〜6は、実
施例1〜6と対比し明らかなように、加熱処理しない場
合、加熱温度が120℃未満であるとポリビニルアルコ
ールの縮合が起こらず、従って、ポリビニルアルコール
のまゝのもつ弱い結着力しかないので、塗着物の剥落を
生じ、負極として実用性がない。一方、加熱温度が20
0℃を越える場合、或いは200℃以下で120℃以上
の範囲であっても、加熱時間が5分を越える場合は、塗
着物の剥落は生じないが、放電容量が、120〜200
℃で1〜5分の加熱処理条件である本発明の実施例1〜
5に比し著しく低いものとなる。As is apparent from Table 1 above, the conventional example is
No peeling of the coated material occurs, but the discharge capacities are those of Examples 1 to 6
It is lower than. This proves that the storage characteristics of the hydrogen storage alloy are thermally deteriorated. In Comparative Examples 1 to 6, as is clear from comparison with Examples 1 to 6, when the heat treatment is not carried out, the condensation of polyvinyl alcohol does not occur when the heating temperature is lower than 120 ° C., and accordingly Since it has only a weak binding force, it causes peeling of the adhered material and is not practical as a negative electrode. On the other hand, the heating temperature is 20
If the heating time exceeds 5 minutes, even if the heating temperature exceeds 0 ° C. or the heating temperature exceeds 200 ° C. and 120 ° C. or more, the coating material does not peel off, but the discharge capacity is 120 to 200.
Example 1 of the present invention, which is a heat treatment condition at 1 ° C for 1 to 5 minutes
It is significantly lower than that of No. 5.
【0014】上記の実施例1〜6の電極の製造におい
て、ポリビニルアルコールは、粘稠剤としてペーストの
調製に役立つと共に、上記の加熱処理条件において結着
剤として役立つことゝなり、従来のような結着剤を別個
に添加する必要がなく、而も塗着物の剥落が防止される
と共に、従来の結着剤を使用し且つ高温で長時間加熱し
て得られる電極に比し、水素吸蔵合金の熱劣化を生ぜ
ず、良好な水素吸蔵特性を維持するので、放電容量の向
上した水素吸蔵合金電極をもたらす。In the production of the electrodes of Examples 1 to 6 above, polyvinyl alcohol serves as a thickening agent in the preparation of the paste, and also serves as a binder under the above heat treatment conditions. Since it is not necessary to add a binder separately, peeling of the adhered material is prevented, and compared with an electrode obtained by using a conventional binder and heating at high temperature for a long time, a hydrogen storage alloy Since it does not cause thermal deterioration and maintains good hydrogen storage characteristics, it provides a hydrogen storage alloy electrode with improved discharge capacity.
【0015】[0015]
【発明の効果】このように本願発明によるときは、ポリ
ビニルアルコールを水素吸蔵合金をペースト状スラリー
とするための粘稠剤として使用することに加え、120
〜200℃の加熱温度で1〜5分加熱する加熱処理によ
り水素吸蔵合金粉末粒子相互を強固に結着すると共に、
その塗着物が導電性基板に対し塗着した水素吸蔵合金の
剥落を防止し、安定堅牢で且つ電気特性の向上した水素
吸蔵合金電極をもたらし、従来のような非水溶性の結着
剤粉末を併用しないので、製造が容易で且つ製造コスト
の低下した電極が得られる。As described above, according to the present invention, in addition to using polyvinyl alcohol as a thickener for forming a hydrogen storage alloy into a paste-like slurry, 120
The hydrogen storage alloy powder particles are firmly bound to each other by a heat treatment of heating at a heating temperature of ~ 200 ° C for 1 to 5 minutes, and
The adhered material prevents the hydrogen storage alloy applied to the conductive substrate from peeling off, resulting in a hydrogen storage alloy electrode that is stable and robust and has improved electrical characteristics. Since they are not used together, an electrode that is easy to manufacture and has a low manufacturing cost can be obtained.
Claims (1)
加した導電剤粉末と少なくともポリビニルアルコールを
水に溶解した増粘剤水溶液とを混練して得られるペース
ト状のスラリーを、導電性基板に塗着してスラリー層を
形成し、乾燥、所定厚さに加圧成形した後、120〜2
00℃で1〜5分加熱処理することを特徴とする水素吸
蔵合金電極の製造法。1. A paste-like slurry obtained by kneading a hydrogen-absorbing alloy powder as a main component, and a conductive agent powder added to the powder and a thickener aqueous solution in which at least polyvinyl alcohol is dissolved in water are kneaded on a conductive substrate. After coating and forming a slurry layer, drying and press-molding to a predetermined thickness, 120-2
A method for producing a hydrogen storage alloy electrode, which comprises heat treatment at 00 ° C. for 1 to 5 minutes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8156144A JPH09320577A (en) | 1996-05-28 | 1996-05-28 | Manufacture of hydrogen absorbing alloy electrode |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8156144A JPH09320577A (en) | 1996-05-28 | 1996-05-28 | Manufacture of hydrogen absorbing alloy electrode |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH09320577A true JPH09320577A (en) | 1997-12-12 |
Family
ID=15621298
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8156144A Pending JPH09320577A (en) | 1996-05-28 | 1996-05-28 | Manufacture of hydrogen absorbing alloy electrode |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH09320577A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0969540A3 (en) * | 1998-06-05 | 2002-04-24 | Nisshinbo Industries, Inc. | Fuel cell separator and process for producing same |
-
1996
- 1996-05-28 JP JP8156144A patent/JPH09320577A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0969540A3 (en) * | 1998-06-05 | 2002-04-24 | Nisshinbo Industries, Inc. | Fuel cell separator and process for producing same |
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