JPH01184071A - Painting apparatus - Google Patents

Painting apparatus

Info

Publication number
JPH01184071A
JPH01184071A JP1028788A JP1028788A JPH01184071A JP H01184071 A JPH01184071 A JP H01184071A JP 1028788 A JP1028788 A JP 1028788A JP 1028788 A JP1028788 A JP 1028788A JP H01184071 A JPH01184071 A JP H01184071A
Authority
JP
Japan
Prior art keywords
slit
coating
coating liquid
edge surface
width
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.)
Granted
Application number
JP1028788A
Other languages
Japanese (ja)
Other versions
JP2639670B2 (en
Inventor
Seiichi Tobisawa
誠一 飛沢
Shigehisa Kawabe
茂寿 川邉
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.)
Konica Minolta Inc
Original Assignee
Konica Minolta Inc
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 Konica Minolta Inc filed Critical Konica Minolta Inc
Priority to JP63010287A priority Critical patent/JP2639670B2/en
Priority to EP89100729A priority patent/EP0325206B1/en
Priority to DE68922228T priority patent/DE68922228T2/en
Priority to US07/297,756 priority patent/US5042422A/en
Publication of JPH01184071A publication Critical patent/JPH01184071A/en
Application granted granted Critical
Publication of JP2639670B2 publication Critical patent/JP2639670B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Application Of Or Painting With Fluid Materials (AREA)
  • Coating Apparatus (AREA)

Abstract

PURPOSE:To reduce variations of film thickness in the direction of the width of an obtained sheet without lowering electromagnetic properties, by tapering an exit part of a slit at least by a certain length and making the width of the edge of the exit 100mum or less. CONSTITUTION:A coating liquid is extruded continuously from a slit 3 between a front edge surface 1 and a back edge surface 3 on the surface of a running, flexible support to paint it. At least a certain area of the exit part of the slit 3 forms a taper between the wall surfaces 3A and 3B, and the angle theta1 of the taper is made within 3 deg.-10 deg. and the width of the edge of the slit is made <=100mum. As a result, the speed of the coating liquid in a prescribed flowing amount at the exit of the slit 3 is heightened and without lowering electromagnetic properties, variation of film thickness in the direction of the width of the obtained sheet is reduced. This apparatus is applicable to production of magnetic recording materials.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、押出し型塗布装置に係り、特に磁気記録媒体
を製造する際、良好な塗布が得られる塗布装置に関する
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an extrusion type coating device, and particularly to a coating device that can obtain good coating when manufacturing magnetic recording media.

〔従来の技術〕[Conventional technology]

コーティング方式としては、ロールコート、グラビアコ
ート、エクストルージョンコート、スライドビードコー
ト、カーテンコート等種々の方式があることはよく知ら
れている。
It is well known that there are various coating methods such as roll coating, gravure coating, extrusion coating, slide bead coating, and curtain coating.

磁気記録媒体は、支持体上に磁性塗布液を塗布すること
によって得られるが、その塗布方式としては、ロールコ
ート、グラビアコート、エクストルージョンコートが一
般的である。この中でも、エクストルージョンコートは
、均一な塗布膜厚が得られるので優れている。
Magnetic recording media are obtained by coating a magnetic coating liquid on a support, and the coating methods generally include roll coating, gravure coating, and extrusion coating. Among these, extrusion coating is excellent because it provides a uniform coating thickness.

一方、磁気記録媒体自体の改良が、近年、急速に進んで
いる結果、高BET値の酸化磁性粉やバリウムフェライ
ト材料の使用の指向が図られ、塗布液が高粘度化してい
る。また、高密度化に対処するために、薄膜塗布を行い
たい、あるいは生産性を高めるため可能な限り高速で塗
布したいとの要望が高まっている。
On the other hand, improvements in magnetic recording media themselves have progressed rapidly in recent years, and as a result, there has been a trend towards using oxidized magnetic powders and barium ferrite materials with high BET values, and coating liquids have become highly viscous. In addition, there is an increasing desire to perform thin film coating in order to cope with higher density, or to perform coating at the highest possible speed in order to increase productivity.

ところで、主として磁気記録媒体の製造を目的としたエ
クストルージョンコート法における従来技術として、特
開昭57−84771号、同5B−104666号、同
60−238179号公報記載のものが知られている。
By the way, as a conventional technique in the extrusion coating method mainly aimed at manufacturing magnetic recording media, there are known techniques described in Japanese Patent Application Laid-open Nos. 57-84771, 5B-104666, and 60-238179.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

上記のエクストルージョンコート法は、確かに均一な塗
布膜厚を得ることができるけれども、良好な塗布条件が
狭い範囲でしか得ることができず、前述のような、高粘
度、薄膜塗布および高速塗布条件下では、所望の塗布を
行い得ない。
Although the extrusion coating method described above can certainly obtain a uniform coating film thickness, it is only possible to obtain good coating conditions in a narrow range, and it is difficult to achieve high viscosity, thin film coating, and high speed coating as described above. Under these conditions, the desired application cannot be achieved.

本発明者らは、この点に鑑み、種々の実験および検討を
加えたところ、エクストルーダーの形状もさることなが
ら、これとの関連で、塗布液の流動性が大きな支配要因
となっていることを突き止めた。
In view of this, the present inventors conducted various experiments and studies, and found that in addition to the shape of the extruder, the fluidity of the coating liquid is a major controlling factor in this regard. I found out.

特に、電磁変換特性に塗布液の流動性が大きく影響し、
とりわけ塗布液流出スリットの出口での塗布液の流速が
ある条件以上であることが必要とされることを知見した
。この条件は、特にBET値50rrf/g以上の磁気
粉やメタル粉を伴う塗布液の場合に必須となる。
In particular, the fluidity of the coating liquid greatly affects the electromagnetic conversion characteristics.
In particular, it has been found that the flow rate of the coating liquid at the outlet of the coating liquid outflow slit is required to be higher than a certain condition. This condition is especially essential in the case of a coating liquid containing magnetic powder or metal powder with a BET value of 50 rrf/g or more.

しからば、設定膜厚、したがって設定塗布液流量条件下
で、流速を高めるためには、フロントエツジ面とバック
ェツジ面との間のスリット間隔を狭めればよいことは当
然に考えられる。
Therefore, it is natural to think that in order to increase the flow rate under the conditions of the set film thickness and therefore the set coating liquid flow rate, the slit interval between the front edge surface and the back edge surface may be narrowed.

しかし、前記各公報記載のように、従来の塗布装置のス
リットは平行であるため、スリット間隔を狭めると、ス
リット部分での圧力損失が大きくなり、しかもスリット
部分を通る過程での圧力変動が大きい。
However, as described in each of the above publications, the slits of conventional coating devices are parallel, so narrowing the slit interval increases pressure loss at the slit portion, and moreover, pressure fluctuations during the process of passing through the slit portion are large. .

かかる大きな圧力損失を示す条件下で、特願昭58−1
62420号に示された塗布液飾剪断処理装置を併用す
ると、たとえば スリット間隔が50μm以下では、同装置に作用する圧
力は4kg/cj以上となり、同装置および送液系の各
部分での機械的シール部にトラブルを生じがちであり、
またスリットの形成に当り、その間隔が50μm以下で
は、スリット面の機械加工精度が直接的に影響し、流出
する塗布液の圧力変動を生じてしまう。
Under conditions exhibiting such a large pressure loss,
When used in conjunction with the coating liquid decoration shearing device shown in No. 62420, for example, when the slit interval is 50 μm or less, the pressure acting on the device will be 4 kg/cj or more, and the mechanical stress in each part of the device and liquid delivery system will be Trouble tends to occur in the seal part,
Furthermore, when forming slits, if the spacing between the slits is 50 μm or less, the machining accuracy of the slit surface will directly affect the slit surface, resulting in pressure fluctuations in the flowing coating liquid.

後者の機械加工精度に伴う圧力変動、ならびにスリット
間隔が一定であることによる圧力変動(圧送圧力を均一
にすることは圧送ポンプ脈動等により難しい)があると
、塗布液が不規則にスリット出口から流出し、その結果
、シートの流れ方向および幅方向に関して膜厚のバラツ
キの原因となる。
If there are pressure fluctuations due to the latter machining precision, or pressure fluctuations due to the constant slit spacing (it is difficult to make the pumping pressure uniform due to pressure pump pulsation, etc.), the coating liquid may flow irregularly from the slit outlet. As a result, this causes variations in film thickness in the machine direction and width direction of the sheet.

そこで、本発明の主たる目的は、磁性塗布液の場合、得
られる磁気記録媒体の電磁交換特性として十分満足でき
るものが得られ、また膜厚のバラツキが少く、さらに圧
力損失が少い塗布装置を提供することにある。
Therefore, the main object of the present invention is to provide a coating device that, in the case of a magnetic coating liquid, can provide sufficiently satisfactory electromagnetic exchange characteristics of the resulting magnetic recording medium, has little variation in film thickness, and has little pressure loss. It is about providing.

〔問題点を解決するための手段〕[Means for solving problems]

上記目的は、フロントエツジ面およびバックェツジ面に
沿って連続的に走行する可撓性支持体表面に、前記フロ
ントエツジ面とバックェツジ面とのスリットから塗布液
を連続的に押し出して前記支持体表面に塗布液を塗布す
る装置において、前記スリットの少くとも出口部分のあ
る長さにわたり、その出口端に向って先細のテーパをな
しており、テーパ面が交わる角度が3°〜20°であり
、出口端間隔巾が100μm以下であることで達成され
る。
The above purpose is to continuously extrude a coating liquid onto the surface of a flexible support that runs continuously along the front edge surface and the back edge surface through slits between the front edge surface and the back edge surface. In an apparatus for applying a coating liquid, the slit is tapered over a certain length of at least the exit portion toward the exit end, and the angle at which the tapered surfaces intersect is 3° to 20°; This is achieved by setting the width between the ends to 100 μm or less.

〔作 用〕[For production]

本発明では、第1図のように、スリットの少くとも出口
部分のある範囲にわたり、スリット3の壁面3A、3B
がテーパをなしており、それらが交わる角度θ1が3°
〜10”であるため、ある設定された塗布液流量の下で
、スリット面が平行である場合に比較して、スリット出
口端での流速が高まる。したがって、得ようとする磁気
記録媒体の電磁変換特性を低下させないためには、スリ
ット出口端での流速がある値以上であることが必要であ
るとの事実の下で、十分な出口端流速を得ることができ
るから、所望の電磁変換特性を満足できる。
In the present invention, as shown in FIG.
are tapered, and the angle θ1 where they intersect is 3°
10", the flow velocity at the slit exit end is higher under a certain set coating liquid flow rate than when the slit surfaces are parallel. Therefore, the electromagnetic Given the fact that the flow velocity at the slit exit end is required to be above a certain value in order to avoid deterioration of the conversion characteristics, it is possible to obtain a sufficient flow velocity at the exit end, so that the desired electromagnetic conversion characteristics can be achieved. can be satisfied.

また、スリットの壁面がテーパであると、圧力損失が低
くなり、前述の塗布前剪断装置の使用を行っても、圧力
損失が小さいため、その使用に当ってのトラブルが悪く
なる。さらに、スリット面が平行であると、スリット面
全面の加工精度が高くないと、塗布したとき、シート幅
方向の膜厚バラツキが大きくなるのに対して、本発明に
従うと、主にスリットの出口端の加工精度のみにシート
幅方向の膜厚バラツキが左右され、かつスリット出口端
のみであれば所望の加工精度を保つことは容易であるか
ら、結果としてシート幅方向の膜厚バラツキを少くでき
る。
Further, if the wall surface of the slit is tapered, the pressure loss will be low, and even if the above-mentioned pre-coating shearing device is used, the pressure loss will be small, and troubles during its use will worsen. Furthermore, if the slit surfaces are parallel, if the processing accuracy of the entire slit surface is not high, there will be large variations in film thickness in the sheet width direction when coating. The film thickness variation in the sheet width direction depends only on the processing accuracy of the edges, and it is easy to maintain the desired processing accuracy only at the slit exit end, so as a result, the film thickness variation in the sheet width direction can be reduced. .

〔発明の具体的構成〕[Specific structure of the invention]

以下本発明をさらに詳説する。 The present invention will be explained in more detail below.

第1図は本発明に係るエクストルーダーの要部を示した
もので、上流側表面にフロントエツジ面1、下流側表面
にバックェツジ面2を有し、それらの間に塗布液ポケッ
ト部(図示せず、同図下方)に連通ずるスリット3を有
している。
FIG. 1 shows the main parts of the extruder according to the present invention, which has a front edge surface 1 on the upstream surface and a back edge surface 2 on the downstream surface, and a coating liquid pocket section (not shown) between them. It has a slit 3 that communicates with the lower part of the figure.

本発明では、スリット3の壁面3A、3Bがテーパ面を
なし、それらの交わる角度θ1が36〜20°とされる
。3°未満では従来の問題を避けることができず、20
°を超えると、安定した流速を得がたい。また、スリッ
ト3の出口端間隔巾L、すなわちエツジ面1.2のいず
れか一方または両者とスリット3との境界縁(図示例で
はバックェツジ面2との境界縁C)を通り、スリット3
の中心NlAl4と直交する方向に測った間隔りが、1
00μm以下、望ましくは50μ…以下とされる。
In the present invention, the wall surfaces 3A and 3B of the slit 3 form tapered surfaces, and the angle θ1 at which they intersect is 36 to 20 degrees. If it is less than 3°, the conventional problem cannot be avoided, and the
If it exceeds °, it is difficult to obtain a stable flow rate. In addition, it passes through the exit end interval width L of the slit 3, that is, the boundary edge between either or both of the edge surfaces 1.2 and the slit 3 (in the illustrated example, the boundary edge C with the back edge surface 2), and passes through the slit 3.
The distance measured in the direction perpendicular to the center NlAl4 is 1
00 μm or less, preferably 50 μm or less.

また、下流端Bを通り間隔りを取った線と平行に引いた
線と、境界縁Cとの長さHは、H<Lであることが望ま
れる。
Further, it is desirable that the length H between the boundary edge C and a line drawn parallel to the line that passes through the downstream end B and is spaced apart satisfies H<L.

なお、第1図の仮想線で示すように、スリット3の基部
側は平行であるなど、必らずしも全面がテーパ面である
ことは要しない。
Note that, as shown by the imaginary lines in FIG. 1, the base side of the slit 3 is parallel, and the entire surface does not necessarily have to be a tapered surface.

一方、フロントエツジ面lの下流端Bにおける接線J、
より、バンクエツジ2の一部が突出(第1図ではほぼ上
方に突出)するのが望ましい。
On the other hand, the tangent J at the downstream end B of the front edge surface l,
Therefore, it is preferable that a part of the bank edge 2 protrudes (protrudes substantially upward in FIG. 1).

この条件は、前記l、と、下流端Bを通りバックェツジ
面を結ぶ線13とのなす角度をα2、前記IIと、バッ
クェツジ面2の下流端Aにおける接線12となす角度を
α1としたとき、次記(2)式の条件としてもあられす
ことができる。
This condition is as follows: When the angle between the above l and the line 13 passing through the downstream end B and connecting the backing surface is α2, and the angle between the above II and the tangent 12 at the downstream end A of the backing surface 2 is α1, It can also occur as a condition of the following equation (2).

α2〈α+<180°  ・・・・・・(2)一方、バ
ックェツジ面2の曲率半径rは、3〜10龍が好ましい
α2<α+<180° (2) On the other hand, the radius of curvature r of the backing surface 2 is preferably 3 to 10 degrees.

また、接線12と壁面とのなす角度θ2は、80°〜1
10°が好ましい。
Also, the angle θ2 between the tangent line 12 and the wall surface is 80° to 1
10° is preferred.

支持体は、矢印で示すように、フロントエツジ1に沿っ
てせり上りから下流端Bを通って、スリット3および液
溜り部分4を越えて、バックェツジ面2の塗布液層厚分
上方をめぐりながら右方へ抜けて行く。
As shown by the arrow, the support rises along the front edge 1, passes through the downstream end B, crosses the slit 3 and the liquid reservoir part 4, and goes around above the thickness of the coating liquid layer on the back edge surface 2. Go out to the right.

本発明に係る支持体としては、ポリエステルフィルム等
のプラスチックフィルム、紙、両者の積層シート、金属
シート等を挙げることができ、可撓性材料であればその
材質は問われない。
Examples of the support according to the present invention include a plastic film such as a polyester film, paper, a laminated sheet of both, a metal sheet, etc., and the material is not limited as long as it is a flexible material.

塗布液としては、磁性塗布液、特に1000cps(B
型粘度計にて60回転、1分後の測定値)以上の磁性塗
布液を対象とする場合に本発明の効果が顕著にあられれ
るけれども、写真感光性塗布液等を対象するものであっ
てもよい。
As a coating liquid, a magnetic coating liquid, especially 1000 cps (B
Although the effect of the present invention is noticeable when the present invention is applied to a magnetic coating liquid with a magnetic coating liquid of 60 rotations after 1 minute using a type viscometer, it is not applicable to a photographic photosensitive coating liquid or the like. Good too.

また、塗布速度としては、150m/分以上の高速の場
合において、顕著な効果があられれる。
Further, when the coating speed is 150 m/min or higher, a remarkable effect can be obtained.

〔実施例〕〔Example〕

次に実施例にて本発明め効果を明らかにする。 Next, the effects of the present invention will be clarified in Examples.

支持体として、15μmのポリエステルテレフタレート
フィルムを用い、メタル粉(BET値60り?/g)を
有する3000cpsの高粘度磁性塗布液を、ウェット
膜厚で30μmに塗布し磁気記録媒体シートを得た。
A 15 μm polyester terephthalate film was used as a support, and a 3000 cps high viscosity magnetic coating liquid containing metal powder (BET value 60?/g) was applied to a wet film thickness of 30 μm to obtain a magnetic recording medium sheet.

この場合、上記本発明に係る塗布装置と、特開昭60−
238179号公報記載の塗布装置との2基を用意し、
それぞれスリットギャップ(実施例のものはスリットギ
ャップは上記りである)を50μmおよび100.uf
fiとし、得られたシートの電磁変換特性RF out
 、幅方向の膜厚バラツキ、および塗時の圧力損失を調
べたところ、第1表の結果を得た。
In this case, the coating device according to the present invention and the
Prepare two coating devices with the coating device described in No. 238179,
The slit gap (the slit gap in the example is as above) is 50 μm and 100 μm, respectively. uf
fi, and the electromagnetic conversion characteristics of the obtained sheet RF out
, the film thickness variation in the width direction, and the pressure loss during coating were investigated, and the results shown in Table 1 were obtained.

第1表 上記のように、本発明装置によると、電磁変換特性を低
下させることなく、幅方向の膜厚バラツキが少く、低い
圧力損失となる。
Table 1 As shown above, according to the device of the present invention, the film thickness variation in the width direction is small and pressure loss is low without deteriorating the electromagnetic conversion characteristics.

〔発明の効果〕〔Effect of the invention〕

以上の通り、本発明によれば、電磁変換特性を悪化させ
ることなく、得られるシートの幅方向の膜厚バラツキを
少く、圧力損失を小さくできる。
As described above, according to the present invention, the variation in film thickness in the width direction of the obtained sheet can be reduced and the pressure loss can be reduced without deteriorating the electromagnetic conversion characteristics.

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

第1図は本発明に係る塗布装置の要部断面図である。 1・・・フロントエツジ面、2・・・バックェツジ面、
3・・・スリット、3A、3B・・・スリットの壁面。
FIG. 1 is a sectional view of essential parts of a coating device according to the present invention. 1...Front edge surface, 2...Back edge surface,
3...Slit, 3A, 3B...Slit wall.

Claims (1)

【特許請求の範囲】[Claims] (1)フロントエッジ面およびバックエッジ面に沿って
連続的に走行する可撓性支持体表面に、前記フロントエ
ッジ面とバックエッジ面とのスリットから塗布液を連続
的に押し出して前記支持体表面に塗布液を塗布する装置
において、 前記スリットの少くとも出口部分のある長さにわたり、
その出口端に向って先細のテーパをなしており、テーパ
面が交わる角度が3°〜20°であり、出口端間隔巾が
100μm以下であることを特徴とする塗布装置。
(1) A coating liquid is continuously extruded from the slits between the front edge surface and the back edge surface onto the flexible support surface that runs continuously along the front edge surface and the back edge surface. In an apparatus for applying a coating liquid to the slit, at least a certain length of the exit portion of the slit,
A coating device that is tapered toward its exit end, the angle at which the tapered surfaces intersect is 3° to 20°, and the width between the exit ends is 100 μm or less.
JP63010287A 1988-01-20 1988-01-20 Coating device and coating method Expired - Fee Related JP2639670B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP63010287A JP2639670B2 (en) 1988-01-20 1988-01-20 Coating device and coating method
EP89100729A EP0325206B1 (en) 1988-01-20 1989-01-17 Coating apparatus
DE68922228T DE68922228T2 (en) 1988-01-20 1989-01-17 Coating device.
US07/297,756 US5042422A (en) 1988-01-20 1989-01-17 Coating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63010287A JP2639670B2 (en) 1988-01-20 1988-01-20 Coating device and coating method

Publications (2)

Publication Number Publication Date
JPH01184071A true JPH01184071A (en) 1989-07-21
JP2639670B2 JP2639670B2 (en) 1997-08-13

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013193021A (en) * 2012-03-19 2013-09-30 Fujifilm Corp Coating apparatus and coating method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6320069A (en) * 1986-07-15 1988-01-27 Fuji Photo Film Co Ltd Coater
JPS6320070A (en) * 1986-07-15 1988-01-27 Fuji Photo Film Co Ltd Coater

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6320069A (en) * 1986-07-15 1988-01-27 Fuji Photo Film Co Ltd Coater
JPS6320070A (en) * 1986-07-15 1988-01-27 Fuji Photo Film Co Ltd Coater

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013193021A (en) * 2012-03-19 2013-09-30 Fujifilm Corp Coating apparatus and coating method

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