JPS63114058A - Manufacture of plate for battery - Google Patents
Manufacture of plate for batteryInfo
- Publication number
- JPS63114058A JPS63114058A JP61257011A JP25701186A JPS63114058A JP S63114058 A JPS63114058 A JP S63114058A JP 61257011 A JP61257011 A JP 61257011A JP 25701186 A JP25701186 A JP 25701186A JP S63114058 A JPS63114058 A JP S63114058A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- coating material
- drying
- coating agent
- furnace
- 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
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- 239000011248 coating agent Substances 0.000 claims abstract description 75
- 238000001035 drying Methods 0.000 claims abstract description 49
- 238000000576 coating method Methods 0.000 claims abstract description 37
- 239000000758 substrate Substances 0.000 claims abstract description 26
- 238000000034 method Methods 0.000 claims description 8
- 239000000463 material Substances 0.000 abstract description 29
- 238000013459 approach Methods 0.000 abstract description 2
- 230000005855 radiation Effects 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000007796 conventional method Methods 0.000 description 4
- 239000000853 adhesive Substances 0.000 description 3
- 230000001070 adhesive effect Effects 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
- H01M4/0402—Methods of deposition of the material
- H01M4/0404—Methods of deposition of the material by coating on electrode collectors
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
- H01M4/0402—Methods of deposition of the material
- H01M4/0409—Methods of deposition of the material by a doctor blade method, slip-casting or roller coating
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
- H01M4/0402—Methods of deposition of the material
- H01M4/0416—Methods of deposition of the material involving impregnation with a solution, dispersion, paste or dry powder
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
- H01M4/043—Processes of manufacture in general involving compressing or compaction
- H01M4/0435—Rolling or calendering
-
- 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
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は、電池用極板の製造方法に関するものである。[Detailed description of the invention] [Industrial application field] The present invention relates to a method of manufacturing a battery electrode plate.
[従来の技術]
従来の電池用極板の製造は、鉄板にニッケルメッキを施
した基体の面にスラリー状或いはペースト状の塗着剤を
塗着した後、これを乾燥炉に入れ、炉内を一定温度にし
て該塗着剤を乾燥することにより行っていた。[Prior art] Conventional battery electrode plates are produced by applying a slurry or paste coating agent to the surface of a nickel-plated iron plate, placing it in a drying oven, and drying it inside the oven. This was done by drying the coating agent at a constant temperature.
[発明が解決しようとする問題点コ
上記のような電池用極板の製造方法では、基体の面に塗
着された塗着剤の量が変動する場合には、塗着剤の変動
量に応じ一々炉内温度を設定しなければならず、その作
業が面倒となる問題点があった。また、乾燥炉の熱源と
して遠赤外線ヒータを用いたものがあるが、この遠赤外
線ヒータを用いたものは塗着剤の乾燥効率は良いが、炉
内温度を所定値に設定することが難しいという問題点が
あった。[Problems to be Solved by the Invention] In the method for manufacturing battery electrode plates as described above, when the amount of the coating agent applied to the surface of the substrate changes, There was a problem in that the temperature inside the furnace had to be set one by one, making the work cumbersome. In addition, there are drying ovens that use far-infrared heaters as a heat source, but although they have good drying efficiency for coating materials, it is difficult to set the temperature inside the oven to a predetermined value. There was a problem.
本発明の目的は、塗着剤の量が変動してもその乾燥を正
確に且つ容易に行える電池用極板の製造方法を提供する
ことにある。An object of the present invention is to provide a method for manufacturing a battery electrode plate that allows accurate and easy drying of the coating agent even if the amount of the coating agent varies.
1問題点を解決するための手段]
本発明を、第1図に示されている実施例をもとに説明す
ると、基体2の面に塗着された該塗着剤1の層の厚さを
該基体2をスリッター6に通すことにより均一にする塗
着工程Aと、塗着工程Aで基体2に塗着された塗着剤1
を乾燥する乾燥工程Bとを有する電池用極板の製造方法
であって、本発明においては、乾燥工程Bを乾燥炉7の
出口側での塗着剤1の温度による信号を乾燥炉7の温度
制御装置12に供給して塗着剤1の温度を設定温度に一
致させるように乾燥炉7内温度を制御するようにしてい
る。Means for Solving Problem 1] The present invention will be explained based on the embodiment shown in FIG. A coating process A in which the substrate 2 is made uniform by passing it through a slitter 6, and a coating agent 1 applied to the substrate 2 in the coating process A.
In the present invention, the drying step B includes a drying process B in which a signal from the temperature of the coating agent 1 at the outlet side of the drying oven 7 is sent to the drying oven 7. The temperature inside the drying oven 7 is controlled so that the temperature of the coating agent 1 matches the set temperature by supplying it to a temperature control device 12.
[作 用]
上記のように塗着剤1の温度による信号で温度制御装置
12を操作し、該温度制御装置12で塗着剤1の温度を
設定温度に一致されるように制御すると、基体2の面に
塗着された塗着剤1の量が変動しても該塗着剤1の乾燥
を正確に且つ容易に行うことができる。また、乾燥炉7
の熱源とじて遠赤外線ヒータ8を用いても同様に、塗着
剤1の量が変動しても該塗着剤1の乾燥を正確に且つ容
易に行うことができる。[Function] As described above, when the temperature control device 12 is operated by a signal based on the temperature of the coating material 1 and the temperature of the coating material 1 is controlled by the temperature control device 12 to match the set temperature, the temperature of the coating material 1 is controlled to match the set temperature. Even if the amount of the coating agent 1 applied to the surface of the coating material 2 changes, the coating agent 1 can be dried accurately and easily. In addition, the drying oven 7
Similarly, even if the far-infrared heater 8 is used as the heat source, the coating material 1 can be dried accurately and easily even if the amount of the coating material 1 changes.
[実施例]
以下、本発明の実施例を第1図を参照して詳細に説明す
る。[Example] Hereinafter, an example of the present invention will be described in detail with reference to FIG.
第1図は本発明の製造方法を実施する装置を示すもので
、この製造装置はスラリー状或いはペースト状の塗着剤
1を、ニッケルメッキを施した鉄板よりなる帯状基体2
に塗着し、乾燥して電池用種板3を製造するものである
。この製造装置は塗着剤1を収容したバット4を有して
いる。バット4内には帯状基体2を方向変換させるロー
ラ5が配設されていて、該バット4の上方にはスリッタ
ー6が配置され、該スリッター6の更に上方には乾燥炉
7が配置されている。乾燥炉7内には多数の遠赤外線ヒ
ータ8が並設されており、それぞれの遠赤外線ヒータ8
は並列に接続されている。これらの遠赤外線ヒータ8は
共通の電力制御用サイリスクユニット9に直列に接続さ
れている。乾燥炉7の出口側には非接触温度計10が配
置されている。該非接触温度計10は温調計11を介し
て電力制御用サイリスタユニット9に接続されている。FIG. 1 shows an apparatus for carrying out the manufacturing method of the present invention, and this manufacturing apparatus applies a slurry or paste coating agent 1 to a strip-shaped substrate 2 made of a nickel-plated iron plate.
The seed plate 3 for a battery is manufactured by applying the paste to the substrate and drying it. This manufacturing device has a vat 4 containing a coating material 1. A roller 5 for changing the direction of the strip-shaped substrate 2 is disposed within the vat 4, a slitter 6 is disposed above the vat 4, and a drying oven 7 is disposed further above the slitter 6. . A large number of far-infrared heaters 8 are arranged in parallel in the drying oven 7, and each far-infrared heater 8
are connected in parallel. These far-infrared heaters 8 are connected in series to a common power control silice unit 9. A non-contact thermometer 10 is arranged on the exit side of the drying oven 7. The non-contact thermometer 10 is connected to a power control thyristor unit 9 via a temperature controller 11.
電力制御用サイリスタユニット9と温調計11とにより
乾燥炉7の温度制御装置12が構成されている。乾燥炉
7の出口側の非接触温度計10が配置されている位置よ
り上方位置には帯状基体2を引上げる引上げローラ装置
13が配置されている。引上げローラ装置13は駆動ロ
ーラ14と、該駆動ローラ14と共に帯状基体2を挟持
する従動ローラ15と、該従動ローラ15を帯状きはた
い2に押付ける押圧手段16により構成されている。
次に上記した極板の製造装置を用いた本発明の極板の製
造方法の一例を説明する。帯状基体2をバット4に収容
された塗着剤1内に浸漬し、該塗着剤1内でローラ5を
介して上方に方向変換して移動すると、帯状基体2の両
板面に塗着剤1が塗着される。次いで、この塗着剤付き
帯状基体2をスリッター6に通すと、該塗着剤1の層の
厚さが均一にされる。このようにして帯状基体2に塗着
剤1を塗着する塗着工程Aが実施される。該塗着工程A
で帯状基体2に塗着剤1が塗着された後、この塗着剤1
付き帯状基体2を乾燥炉7内に導入して乾燥する。乾燥
炉7で塗着剤1が乾燥された塗着剤1付き帯状基体2の
塗着剤1温度を乾燥炉7の出口側で非接触温度計10で
測定する。The power control thyristor unit 9 and the temperature controller 11 constitute a temperature control device 12 for the drying oven 7. A pulling roller device 13 for pulling up the strip-shaped substrate 2 is arranged above the position where the non-contact thermometer 10 is arranged on the exit side of the drying oven 7. The pulling roller device 13 is composed of a driving roller 14, a driven roller 15 that clamps the strip substrate 2 together with the driving roller 14, and a pressing means 16 that presses the driven roller 15 against the strip substrate 2.
Next, an example of the method for manufacturing an electrode plate of the present invention using the above-mentioned electrode plate manufacturing apparatus will be explained. When the strip-shaped substrate 2 is dipped into the coating agent 1 housed in the vat 4 and moved upward through the rollers 5 within the coating agent 1, the coating is applied to both plate surfaces of the strip-shaped substrate 2. Agent 1 is applied. Next, when this strip-shaped substrate 2 with the coating agent is passed through a slitter 6, the thickness of the layer of the coating agent 1 is made uniform. In this way, the coating step A of coating the coating agent 1 on the strip-shaped substrate 2 is carried out. The coating process A
After the coating agent 1 is applied to the strip-shaped substrate 2, this coating agent 1
The strip-shaped substrate 2 with attached strips is introduced into a drying oven 7 and dried. The temperature of the coating agent 1 of the strip-shaped substrate 2 with the coating agent 1 on which the coating agent 1 has been dried in the drying oven 7 is measured using a non-contact thermometer 10 on the exit side of the drying oven 7.
非接触温度計10で測定した塗着剤1の温度を温調計1
1によって設定温度に近ずけるように電力制御用サイリ
スタユニット9をフィードバック制御(所謂PID制f
il)する。このように乾燥炉7の出口測用の塗着剤1
の湿度をフィードバック制御して各遠赤外線ヒータ8の
発生熱量を制御することによって乾燥炉7内湿度を制御
している。このようにして乾燥工程Bが実施されるが、
塗着剤1付き帯状基体2の塗着剤1の量が変化しても乾
燥炉7出日側での塗着剤1温度の設定温度に対する差異
によって乾燥炉7内温度を制御して塗着剤1の乾燥状態
を一定に保つことかできる。The temperature of the coating agent 1 measured with the non-contact thermometer 10 is measured with the temperature controller 1.
1, the power control thyristor unit 9 is feedback-controlled (so-called PID control f) so that the temperature approaches the set temperature.
il). In this way, the coating material 1 for measuring the outlet of the drying oven 7
The humidity inside the drying oven 7 is controlled by controlling the amount of heat generated by each far-infrared heater 8 through feedback control of the humidity. In this way, drying step B is carried out,
Even if the amount of coating agent 1 on the strip-shaped substrate 2 with coating agent 1 changes, the temperature inside the drying oven 7 is controlled based on the difference in the coating agent 1 temperature on the sunrise side of the drying oven 7 from the set temperature. The dry state of agent 1 can be kept constant.
第2図は一定の発熱量の遠赤外線ヒータ8で塗着剤1付
き帯状基体2を乾燥させた際の塗着剤1温度の温度変化
をした線図である。この場合、乾燥が行なわれているの
はXゾーンのみであり、Yゾーンでは乾燥が終了してい
て塗着剤1温度が急激に高くなり略300 ’Cに達す
ると塗着剤1が焦げ始める。従って、塗着剤1を乾燥す
る際の該塗着剤1の設定温度を例えば250℃に設定し
ておくことにより、乾燥状態が自動的に確保され、スリ
ッター6をその間隔を変化させて塗着剤1の厚みを変え
た場合でも従来のように炉の設定温度を一々変える必要
がなく、塗着剤1が常に良好な乾燥状態となる。FIG. 2 is a diagram showing the temperature change of the coating agent 1 when the strip-shaped substrate 2 with the coating agent 1 is dried by the far-infrared heater 8 with a constant amount of heat generated. In this case, drying is occurring only in the X zone, and in the Y zone, drying has finished and the temperature of the coating material 1 increases rapidly and when it reaches approximately 300'C, the coating material 1 begins to burn. . Therefore, by setting the preset temperature of the coating material 1 to, for example, 250° C. when drying the coating material 1, a dry state is automatically ensured, and the slitter 6 is applied by changing the interval between them. Even when the thickness of the adhesive 1 is changed, there is no need to change the set temperature of the furnace one by one as in the conventional case, and the adhesive 1 is always kept in a good dry state.
第3図(a)、(b)はそれぞれ従来の方法による乾燥
工程後の塗着剤1の厚さのバラツキと本発明の方法によ
る乾燥工程後における塗着剤1の厚さのバラツキとを示
す図である。この乾燥後の塗着剤1の厚さのバラツキは
乾燥状態のバラツキをあられすもので、従来の方法によ
る乾燥工程後の塗着剤1の厚さのバラツキと本発明の方
法のよる乾燥工程B後の塗着剤1の厚さのバラツキとを
1000面の試料を用いてその厚みのバラツキを調べた
。その結果、第3図(a)に示すように従来の方法では
塗着剤1の厚さが681〜760μmと80μmの幅で
のバラツキを示し、第3図(b)に示すように本発明の
方法では塗着剤1の厚さが721〜740μ肌と20μ
而の幅でのバラツキを示しており、本発明の方法による
塗着剤1の層の厚さのバラツキが従来のものに比べて小
さいことがわかる。FIGS. 3(a) and 3(b) show the variation in the thickness of the coating material 1 after the drying process by the conventional method and the variation in the thickness of the coating material 1 after the drying process by the method of the present invention, respectively. FIG. This variation in the thickness of the coating material 1 after drying is due to variation in the drying state. The variation in the thickness of the coating material 1 after B was investigated using 1000 samples. As a result, as shown in FIG. 3(a), the thickness of the coating agent 1 in the conventional method showed variations in the width of 681 to 760 μm and 80 μm, and as shown in FIG. In the method, the thickness of adhesive 1 is 721-740μ skin and 20μ
It can be seen that the variation in the layer thickness of the coating agent 1 obtained by the method of the present invention is smaller than that of the conventional method.
[発明の効果]
以上のように、本発明では乾燥炉の出口側での塗着剤温
度による信号を乾燥炉の温度制御装置に供給して塗着剤
温度を設定温度に一致させるように乾燥炉内温度を制御
しているので、基体の面に塗着された塗着剤の量が変動
しても該塗着剤の乾燥を正確に且つ容易に行うことがで
きる。また、乾燥炉の熱源として遠赤外線ヒータを用い
ても同様に、塗着剤の量が変動して該塗着剤の乾燥を正
確に且つ容易に行うことができる。[Effects of the Invention] As described above, in the present invention, a signal based on the temperature of the coating material at the outlet side of the drying oven is supplied to the temperature control device of the drying oven, and the drying process is performed so that the temperature of the coating material matches the set temperature. Since the temperature inside the furnace is controlled, even if the amount of the coating agent applied to the surface of the substrate varies, the coating agent can be dried accurately and easily. Further, even if a far-infrared heater is used as the heat source of the drying oven, the amount of the coating agent can be varied and the coating agent can be dried accurately and easily.
第1図は本発明の製造方法を実施する製造装置の一例を
示す説明図、第2図は本発明の製造方法で乾燥される基
体に塗着された塗着剤の温度変化を示す線図、第3図(
a)は従来の方法による塗着剤の層の厚さのバラツキを
示す図、第3図(b)は本発明の方法による塗着剤の層
の厚さのバラツキを示す図である。
1・・・塗着剤、2用基体、6・・・スリッター、7・
・・乾燥炉、A・・・塗1着工稈、B・・・乾燥工程。
第1図
列刑FIG. 1 is an explanatory diagram showing an example of a manufacturing apparatus for carrying out the manufacturing method of the present invention, and FIG. 2 is a diagram showing the temperature change of the coating agent applied to the substrate to be dried by the manufacturing method of the present invention. , Figure 3 (
FIG. 3(a) is a diagram showing the variation in the thickness of the coating agent layer according to the conventional method, and FIG. 3(b) is a diagram showing the variation in the thickness of the coating agent layer according to the method of the present invention. 1. Painting agent, 2. Substrate, 6. Slitter, 7.
・・Drying oven, A: 1st coated culm, B: Drying process. Figure 1 Punishment
Claims (1)
リッターに通すことにより均一にする塗着工程と、前記
塗着工程で前記基体に塗着された前記塗着剤を乾燥する
乾燥工程とを有する電池用極板の製造方法において、 前記乾燥工程は乾燥炉の出口側での前記塗着剤温度によ
る信号を前記乾燥炉の温度制御装置に供給して前記塗着
剤温度を設定温度に一致させるように前記乾燥炉内温度
を制御することを特徴とする電池用極板の製造方法。[Scope of Claims] A coating step in which the thickness of the layer of the coating agent applied to the surface of the substrate is made uniform by passing the substrate through a slitter, and a coating agent applied to the substrate in the coating step. and a drying step of drying the coating agent, wherein the drying step includes transmitting a signal based on the temperature of the coating agent at the outlet side of the drying oven to a temperature control device of the drying oven. A method for manufacturing a battery electrode plate, characterized in that the temperature inside the drying oven is controlled so that the temperature of the coating agent matches a set temperature.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61257011A JPS63114058A (en) | 1986-10-30 | 1986-10-30 | Manufacture of plate for battery |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61257011A JPS63114058A (en) | 1986-10-30 | 1986-10-30 | Manufacture of plate for battery |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63114058A true JPS63114058A (en) | 1988-05-18 |
Family
ID=17300484
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61257011A Pending JPS63114058A (en) | 1986-10-30 | 1986-10-30 | Manufacture of plate for battery |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63114058A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6284405B2 (en) | 1996-06-19 | 2001-09-04 | Toshiba Battery Co., Ltd. | Nonaqueous electrolyte battery, electrode plate for nonaqueous electrolyte battery, and method for manufacturing electrode plate for nonaqueous electrolyte battery |
CN106000822A (en) * | 2015-03-27 | 2016-10-12 | 株式会社思可林集团 | Drying device, coating forming system and method thereof |
-
1986
- 1986-10-30 JP JP61257011A patent/JPS63114058A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6284405B2 (en) | 1996-06-19 | 2001-09-04 | Toshiba Battery Co., Ltd. | Nonaqueous electrolyte battery, electrode plate for nonaqueous electrolyte battery, and method for manufacturing electrode plate for nonaqueous electrolyte battery |
US6314638B1 (en) | 1996-06-19 | 2001-11-13 | Toshiba Battery Co., Ltd. | Apparatus for manufacturing electrode plate for nonaqueous electrolyte battery |
CN106000822A (en) * | 2015-03-27 | 2016-10-12 | 株式会社思可林集团 | Drying device, coating forming system and method thereof |
CN106000822B (en) * | 2015-03-27 | 2020-03-10 | 株式会社思可林集团 | Coating film forming system and coating film forming method |
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