JPS6386347A - Coating method of slurry substance to core material - Google Patents

Coating method of slurry substance to core material

Info

Publication number
JPS6386347A
JPS6386347A JP61232947A JP23294786A JPS6386347A JP S6386347 A JPS6386347 A JP S6386347A JP 61232947 A JP61232947 A JP 61232947A JP 23294786 A JP23294786 A JP 23294786A JP S6386347 A JPS6386347 A JP S6386347A
Authority
JP
Japan
Prior art keywords
slurry
substance
core material
hot water
thickness
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
Application number
JP61232947A
Other languages
Japanese (ja)
Inventor
Hiroaki Murayama
村山 宏明
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Resonac Corp
Original Assignee
Shin Kobe Electric Machinery Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shin Kobe Electric Machinery Co Ltd filed Critical Shin Kobe Electric Machinery Co Ltd
Priority to JP61232947A priority Critical patent/JPS6386347A/en
Publication of JPS6386347A publication Critical patent/JPS6386347A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/04Processes of manufacture in general
    • H01M4/0402Methods of deposition of the material
    • H01M4/0404Methods of deposition of the material by coating on electrode collectors
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/04Processes of manufacture in general
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

PURPOSE:To obtain a slurry layer having uniform thickness without adjusting the interval of slit by passing a core material through a slurry substance in which the viscosity is made almost constant by adjusting temperature. CONSTITUTION:When the hot water flow rate in hot water circulation paths 10, 11 is adjusted by adjusting the opening rate of flow rate control valves 13, 12, the temperature of a slurry substance A in a slurry substance storage tank 3 is controlled and the viscosity of the substance A is made almost con stant. The thickness of the substance A spread on a core material B by passing through the substance A is made almost constant without adjusting the interval of a slit 18 which is installed to remove the excess amount of the substance A.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、芯材へのスラリー状物質の塗着方法に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method of applying a slurry substance to a core material.

[従来の技術] 従来、芯材へのスラリー状物質の塗着は、スラリー貯蔵
槽内のスラリー状物質中に芯材を通し、該芯材の面にス
ラリー状物質を塗着して該芯材を引き上げ、その引き上
げの過程で余分なスラリー状物質をスラリーと除去する
ことにより、芯材に対するスラリー状物質の塗着厚ざが
一定になるようにしていた。
[Prior Art] Conventionally, applying a slurry substance to a core material involves passing the core material through a slurry substance in a slurry storage tank, applying the slurry substance to the surface of the core material, and applying the slurry substance to the core material. By pulling up the material and removing excess slurry-like material during the pulling process, the coating thickness of the slurry-like material on the core material was kept constant.

[発明が解決しようとする問題点] しかし、スラリー状物質の粘度は温度変化等により変化
するので、経時的に粘度変化が生じた場合、芯材に塗着
されるスラリー状物質の厚さが変化し、これらによりス
リッターで除去されるスラリー状物質の量が多くなり、
スリッターの内でのスラリー状物質の圧力が高まり、ス
ラリー状物質がスリッターから上方に押し出されるよう
な状態が生じ、スリッターを通り抜けたスラリー状物質
の厚さが変化し、スリッターの間隔を調節しないとスラ
リー状物質の厚さを均一にできない問題点があった。
[Problems to be Solved by the Invention] However, the viscosity of the slurry material changes due to changes in temperature, etc., so if the viscosity changes over time, the thickness of the slurry material applied to the core material may change. and these increase the amount of slurry material removed by the slitter.
The pressure of the slurry material inside the slitter increases, creating a situation where the slurry material is forced upwardly from the slitter, and the thickness of the slurry material passing through the slitter changes, unless the spacing between the slitters is adjusted. There was a problem that the thickness of the slurry material could not be made uniform.

本発明の目的は、スリッターの間隔を調節することなし
に均一した厚さのスラリー層を得ることができる芯材へ
のスラリー状物質の塗着方法を提供することにある。
An object of the present invention is to provide a method for applying a slurry-like substance to a core material, which allows a slurry layer of uniform thickness to be obtained without adjusting the spacing between slitters.

[問題点を解決するための手段] 本発明を、第1図及び第2図に示す実施例をもとに説明
すると、スラリー貯蔵槽3内のスラリー状物質A中に芯
材Bを通し、該芯材Bの面にスラリー状物質Aを塗着し
て該芯材Bを引き上げ、その引き上げの過程で余分なス
ラリー状物質Aをスリッター18で除去することにより
、スラリー状物質Aを芯材Bの面に所要の厚さに塗着す
る芯材へのスラリー状物質の塗着方法であって、本発明
においては、スラリー貯蔵槽3内のスラリー状物質Aの
温度を調節することにより該スラリー状物質Aの粘度を
略一定に保ちつつ芯材Bへの塗着を行う。
[Means for Solving the Problems] The present invention will be explained based on the embodiment shown in FIGS. 1 and 2. A core material B is passed through a slurry material A in a slurry storage tank 3, The slurry material A is applied to the surface of the core material B, the core material B is pulled up, and the excess slurry material A is removed by the slitter 18 during the pulling process, thereby converting the slurry material A into the core material. A method of applying a slurry substance to a core material to a required thickness on the surface B, in the present invention, the temperature of the slurry substance A in the slurry storage tank 3 is adjusted. The slurry material A is applied to the core material B while keeping the viscosity of the slurry material A substantially constant.

[作 用] 上記のように、スラリー状物質Aの温度を調節して粘度
に維持すると、芯材Bに塗着されるスラリー状物質Aの
厚さが略一定になり、このためスリッター18の間隔を
変えなくても、スリッター17を通り抜けたスラリー状
物質Aの厚さを略−定に維持できる。
[Function] As described above, when the temperature of the slurry material A is adjusted to maintain the viscosity, the thickness of the slurry material A applied to the core material B becomes approximately constant, and therefore the slitter 18 Even without changing the interval, the thickness of the slurry material A that has passed through the slitter 17 can be maintained approximately constant.

[実施例1 以下、本発明の実施例を図面第1図及び第2図を参照し
て詳細に説明する。
[Embodiment 1] Hereinafter, an embodiment of the present invention will be described in detail with reference to FIGS. 1 and 2 of the drawings.

先ず、本発明の塗着方法を実施する装置について説明す
る。この装置においては、ニッケル粉末を粘結剤と水で
混練したスラリー状物質Aを供給するスラリーポンプ1
を右し、該スラリーポンプ1からバイブ2を経てスラリ
ー貯蔵槽3内にスラリー状物質へが供給されるようにな
っている。バイブ2の外周にはウォータージャケット5
が設けられ、またスラリー貯蔵槽3の外周にもウォータ
ージャケット6が設けられている。それぞれのウォータ
ージャケット5,6にはそれぞれ人口5a。
First, an apparatus for carrying out the coating method of the present invention will be explained. In this device, a slurry pump 1 supplies slurry-like material A made by kneading nickel powder with a binder and water.
The slurry substance is supplied from the slurry pump 1 through the vibrator 2 into the slurry storage tank 3. A water jacket 5 is attached to the outer circumference of the vibe 2.
A water jacket 6 is also provided around the outer periphery of the slurry storage tank 3. Each of the water jackets 5 and 6 has a population of 5a.

6aと出口5b、6bとが設けられている。これらウォ
ータージャケット5,6に温水Cを供給するため、ヒー
タ(図示せず。)を内蔵した渇水槽7が設けられている
。該温水槽7からは温水Cが温水循環往路8を経て各ウ
ォータージャケット5゜6の入口5a、5aの供給され
るようになっている。各ウォータージャケット5,6の
出口5b。
6a and outlets 5b, 6b are provided. In order to supply hot water C to these water jackets 5 and 6, a water tank 7 having a built-in heater (not shown) is provided. Hot water C is supplied from the hot water tank 7 to the inlets 5a, 5a of each water jacket 5.degree.6 via a hot water circulation outgoing path 8. Outlet 5b of each water jacket 5,6.

6bからは温水Cが温水循環復路9を経て温水槽7に戻
されるようになっている。これによりウォータージャケ
ット5に対する温水循環路10と、ウォータージャケッ
ト6に対する温水循環路11とが形成されている。各温
水循環路10,11にはそれぞれ流は調整弁12.13
が取付けられ、各温水循環路10.11に温水Cを循環
させるため渇水循環往路8にはウォーターポンプ14が
取付けられている。スラリー貯蔵槽3内にはスラリーポ
ンプ1からバイブ2を通して供給されたスラリー状物質
Aが収容されている。スラリー状物質Aが収容されてい
るスラリー貯蔵槽3内にはシート状の芯材Bが連続的に
通されて順次スラリー状物質へに浸漬されるようになっ
ている。即ち、該芯材Bは巻芯15に巻回されており、
該巻芯15から巻き戻された芯材Bはローラ16によっ
て方向変換されてスラリー貯蔵槽3内に貯留されている
スラリー状物質△の中に浸漬されてからローラ17によ
って方向変換されて上方に連続的に立ち上げられるよう
になっている。芯材Bはニッケルカドミウム蓄電池に用
いる鉄にニッケルメッキを施した多孔性金属芯材からな
っている。スラリー貯蔵槽3から出て上方に移動する芯
材Bはその両板面にスラリー状物質へが塗着されており
、この塗着されているスラリー状物質Aの厚さを均一に
してスラリー層を成形するためのスリック−18がスラ
リー貯蔵槽3の上方に配置されている。スリッター18
より上方には芯材Bを挟むようにして非接触式の厚さ測
定器19が配置されている。
From 6b, hot water C is returned to the hot water tank 7 via a hot water circulation return path 9. As a result, a hot water circulation path 10 for the water jacket 5 and a hot water circulation path 11 for the water jacket 6 are formed. Each hot water circulation path 10, 11 has a flow regulating valve 12, 13.
A water pump 14 is attached to the outgoing drought circulation path 8 in order to circulate hot water C to each hot water circulation path 10.11. The slurry storage tank 3 contains a slurry substance A supplied from the slurry pump 1 through the vibrator 2. A sheet-shaped core material B is continuously passed through the slurry storage tank 3 in which the slurry material A is stored, and is successively immersed in the slurry material. That is, the core material B is wound around the winding core 15,
The core material B unwound from the winding core 15 is direction-changed by rollers 16 and immersed in the slurry material Δ stored in the slurry storage tank 3, and then direction-changed by rollers 17 and directed upward. It is designed to be launched continuously. Core material B is made of a porous metal core material made of nickel-plated iron used in nickel-cadmium storage batteries. The core material B that comes out of the slurry storage tank 3 and moves upward has a slurry-like substance applied to both its plate surfaces, and the thickness of the applied slurry-like substance A is made uniform to form a slurry layer. A slick 18 for forming the slurry is placed above the slurry storage tank 3. Slitter 18
A non-contact thickness measuring device 19 is arranged above the core material B so as to sandwich the core material B therebetween.

厚さ測定器19により検出される信号を入力信号として
流量調節弁12.13の開度を調節する制御機器20が
設けられている。
A control device 20 is provided that uses a signal detected by the thickness measuring device 19 as an input signal to adjust the opening degree of the flow rate control valves 12,13.

次に、上記した装置を用いた本発明の芯材へのスラリー
状物質の塗着方法について説明する。本実施例において
は、スラリー貯蔵槽3に収容されたスラリー状物質Aの
中に芯材Bを連続的に浸漬して芯材Bの両板面にスラリ
ー状vA質へを連続的に塗着して該芯材Bを引き上げ、
その引き上げの過程で余分なスラリー状物質Aをスリッ
ター18で除去して均一した厚さのスラリー層を成形す
る。
Next, a method of applying a slurry-like substance to a core material of the present invention using the above-described apparatus will be explained. In this embodiment, the core material B is continuously immersed in the slurry material A stored in the slurry storage tank 3, and the slurry material A is continuously applied to both plate surfaces of the core material B. and pull up the core material B,
During the pulling process, excess slurry material A is removed by a slitter 18 to form a slurry layer of uniform thickness.

この際、厚さ測定器19でスラリー苦の厚さを測定して
該厚さが均一にならない場合、その検出信号を入力信号
として該信号に応じて制御]機器20を作動し、各流量
調整弁12.13の開度を調整することにより各温水循
環路10.11を流れる温水Cの流量を調整し、各ウォ
ータージャケット5.6で覆われたスラリー貯7a13
とバイブ2内のスラリー状物質Aの温度を制御して該ス
ラリー状物質Aの粘度を略一定にする。このようにして
略一定の粘度にしたスラリー状物質Aを芯材Bに塗着す
ると、略一定の厚さのスラリー状物質Aが得られ(第2
図参照。)、その後、スリッター18により余分なスラ
リー状物質へを削り落す。このとき芯材Bの表面には多
聞に余分なスラリー状物質Aが塗着されていないので、
スリッター18で削り落されるスラリー状物質Aの闇が
少なく、従ってスリッター18内でのスラリー状物質A
の内圧の上昇を制御でき、スリッター18からのスラリ
ー状物質Aの押し出しを防止できる。このため、スリッ
ター18の間隔を変えずに、均一した厚さのスラリー層
を得ることるができる。
At this time, if the thickness of the slurry is measured using the thickness measuring device 19 and the thickness is not uniform, the detection signal is used as an input signal to control the device 20 according to the signal, and each flow rate is adjusted. By adjusting the opening degree of the valve 12.13, the flow rate of hot water C flowing through each hot water circulation path 10.11 is adjusted, and the slurry storage 7a13 covered with each water jacket 5.6 is
The temperature of the slurry material A in the vibrator 2 is controlled to keep the viscosity of the slurry material A substantially constant. When the slurry-like material A, which has a substantially constant viscosity in this way, is applied to the core material B, the slurry-like material A with a substantially constant thickness is obtained (second
See diagram. ), and then the slitter 18 scrapes off the excess slurry material. At this time, there is not much extra slurry substance A applied to the surface of core material B, so
The slurry material A scraped off by the slitter 18 has less darkness, so the slurry material A in the slitter 18
It is possible to control the rise in the internal pressure of the slitter 18 and prevent the slurry material A from being extruded from the slitter 18. Therefore, a slurry layer of uniform thickness can be obtained without changing the interval between the slitters 18.

上記実施例において、スラリー貯蔵槽3内のスラリー状
物質への温度を、ウォータージャケット6内に温水Cを
循環させることにより制御しているので、温水Cは熱容
量が大きいゆえ、温度の急激な変化が起きにくく、しか
も各部を均一に加熱でき、温度むらの発生の虞れがない
In the above embodiment, the temperature of the slurry-like substance in the slurry storage tank 3 is controlled by circulating the hot water C in the water jacket 6, so the hot water C has a large heat capacity, so rapid changes in temperature can occur. In addition, each part can be heated uniformly, and there is no risk of temperature unevenness.

[発明の効果] 以上のように、本発明によれば、スラリー状物質の温度
を調節して粘度に維持すると、芯材に塗着されるスラリ
ー状物質の厚さが略一定になり、このためスリッターの
間隔を変えなくても、スリッターを通り夫けたスラリー
状物質の厚さを略−定に維持できる。
[Effects of the Invention] As described above, according to the present invention, when the temperature of the slurry material is adjusted to maintain the viscosity, the thickness of the slurry material applied to the core material becomes approximately constant. Therefore, the thickness of the slurry material passing through the slitters can be maintained approximately constant without changing the spacing between the slitters.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の方法を実施する装置を示す説明図、第
2図はスラリー状物質の温度に対する粘度の大きさを示
す線図である。 A・・・スラリー状物質、B・・・芯材、C・・・温水
、3・・・スラリー貯蔵槽、6・・・ウォータージャケ
ット、11・・・温水循環路、13・・・流は調整弁、
18・・・スリッター、1つ・−・厚さ測定器、20・
・・制m+ti器。 第1図
FIG. 1 is an explanatory diagram showing an apparatus for carrying out the method of the present invention, and FIG. 2 is a diagram showing the magnitude of viscosity of a slurry-like substance with respect to temperature. A... Slurry substance, B... Core material, C... Hot water, 3... Slurry storage tank, 6... Water jacket, 11... Hot water circulation path, 13... Flow is Regulating valve,
18...slitter, 1 ---thickness measuring device, 20...
・Control m+ti device. Figure 1

Claims (1)

【特許請求の範囲】 スラリー貯蔵槽内のスラリー状物質中に芯材を通し、該
芯材の面に前記スラリー状物質を塗着して該芯材を引き
上げ、その引き上げの過程で余分な前記スラリー状物質
をスリッターで除去することにより、前記スラリー状物
質を前記芯材の面に所要の厚さに塗着する芯材へのスラ
リー状物質の塗着方法において、 前記スラリー貯蔵槽内の前記スラリー状物質の温度を調
節することにより該スラリー状物質の粘度を略一定に保
ちつつ前記芯材への塗着を行うことを特徴とする芯材へ
のスラリー状物質の塗着方法。
[Claims] A core material is passed through a slurry-like material in a slurry storage tank, the slurry-like material is applied to the surface of the core material, and the core material is pulled up. A method for applying a slurry-like substance to a core material in which the slurry-like substance is applied to a surface of the core material to a required thickness by removing the slurry-like substance with a slitter, comprising: 1. A method for applying a slurry-like substance to a core material, which comprises applying the slurry-like substance to the core material while keeping the viscosity of the slurry-like substance substantially constant by adjusting the temperature of the slurry-like substance.
JP61232947A 1986-09-30 1986-09-30 Coating method of slurry substance to core material Pending JPS6386347A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61232947A JPS6386347A (en) 1986-09-30 1986-09-30 Coating method of slurry substance to core material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61232947A JPS6386347A (en) 1986-09-30 1986-09-30 Coating method of slurry substance to core material

Publications (1)

Publication Number Publication Date
JPS6386347A true JPS6386347A (en) 1988-04-16

Family

ID=16947348

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61232947A Pending JPS6386347A (en) 1986-09-30 1986-09-30 Coating method of slurry substance to core material

Country Status (1)

Country Link
JP (1) JPS6386347A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01165563U (en) * 1988-05-12 1989-11-20

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5341740A (en) * 1976-09-28 1978-04-15 Matsushita Electric Ind Co Ltd Method of manufacturing battery electrode
JPS5725671A (en) * 1980-06-17 1982-02-10 Pettibone Corp Method and device for producing battery paste

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5341740A (en) * 1976-09-28 1978-04-15 Matsushita Electric Ind Co Ltd Method of manufacturing battery electrode
JPS5725671A (en) * 1980-06-17 1982-02-10 Pettibone Corp Method and device for producing battery paste

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01165563U (en) * 1988-05-12 1989-11-20

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