JPH02251854A - Biaxially stretched polyester film for photoresist - Google Patents

Biaxially stretched polyester film for photoresist

Info

Publication number
JPH02251854A
JPH02251854A JP7358789A JP7358789A JPH02251854A JP H02251854 A JPH02251854 A JP H02251854A JP 7358789 A JP7358789 A JP 7358789A JP 7358789 A JP7358789 A JP 7358789A JP H02251854 A JPH02251854 A JP H02251854A
Authority
JP
Japan
Prior art keywords
film
methylene chloride
shrinkage rate
polyester
shrinkage
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
JP7358789A
Other languages
Japanese (ja)
Inventor
Satoyuki Kotani
小谷 智行
Yujiro Fukuda
裕二郎 福田
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.)
Diafoil Co Ltd
Original Assignee
Diafoil 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 Diafoil Co Ltd filed Critical Diafoil Co Ltd
Priority to JP7358789A priority Critical patent/JPH02251854A/en
Publication of JPH02251854A publication Critical patent/JPH02251854A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To provide the polyester film having the characteristic that the film hardly curls with methylene chloride by specifying the shrinkage rate of the film after the film is subjected to a treatment under specific conditions. CONSTITUTION:The shrinkage rate obtd. after the polyester film is immersed for 60 seconds in the methylene chloride kept at 20 deg.C and is dried for 24 hours under the temp. and humidity conditions of 23 deg.C and 50RH is determined to satisfy equation alphaMD+alphaTD<=1.4. {alphaMD: the shrinkage range (%) in the longitudinal direction, alphaTD: the shrinkage rate (%) in the transverse direction.} The sum of this shrinkage rate is preferably >=-0.1% and <=1.2% and is further preferably >=-0.1% and <=1.0%. The value of the shrinkage rate alphaTD in the transverse direction is <=0.7%, more preferably >=-0.1% and <=0.6%, more particularly preferably >=-0.1% and <=0.5%. The photoresist film of a solvent development type has the characteristic that the film hardly curls at the time of removing the polyester layer from the photosensitive layer by treating the film with the methylene chloride.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はフォトレジスト用二軸延伸ポリエステルフィル
ムに関するものであり、詳しくは、溶剤現像型フォトレ
ジストフィルムにおいてポリエステル層を現像前に感光
層から塩化メチレンで処理して除去する際、カールし難
い特性を有する二輪延伸ポリエステルフィルムに関する
ものである。
Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a biaxially oriented polyester film for photoresists, and more specifically, in a solvent-developed photoresist film, the polyester layer is removed from the photosensitive layer by chlorination before development. The present invention relates to a two-wheel stretched polyester film that is resistant to curling when removed by treatment with methylene.

〔従来の技術および発明が解決しようとする課題〕ポリ
エステル二軸延伸フィルムは、耐熱性、機械的性質、耐
薬品性等に優れているため、フォトレジスト用ベースフ
ィルムとして需要が急増している。
[Prior Art and Problems to be Solved by the Invention] Biaxially stretched polyester films have excellent heat resistance, mechanical properties, chemical resistance, etc., and are therefore rapidly in demand as base films for photoresists.

ところで、溶剤現像型フォトレジストフィルムでは、現
像前にポリエステル層を感光層から塩化メチレンで処理
して除去する工程があるが、この工程においてフィルム
は感光層側にカールしてくる。このカールの度合が著し
いときには、現像に支障をきたす場合があり、非常に重
大な問題点となっている。このため、フィルムを塩化メ
チレンで処理してもカールし難い特性を有するポリエス
テルフィルムの開発が強く要望されている。
Incidentally, in a solvent-developed photoresist film, there is a step of removing the polyester layer from the photosensitive layer by treating it with methylene chloride before development, but in this step, the film curls toward the photosensitive layer. When this degree of curl is significant, development may be hindered, which is a very serious problem. Therefore, there is a strong demand for the development of a polyester film that is resistant to curling even when the film is treated with methylene chloride.

〔課題を解決するための手段〕[Means to solve the problem]

本発明者らは、上記課題に鑑み鋭意検討した結果、ある
特定の物性を有するフィルムが塩化メチレンに対しカー
ルし難い特性を有することを見い出し本発明に到達した
As a result of intensive studies in view of the above-mentioned problems, the present inventors have discovered that a film having certain specific physical properties has the property of being resistant to curling when exposed to methylene chloride, and has thus arrived at the present invention.

即ち、本発明の要旨は、20℃の塩化メチレン中に60
秒間浸漬し、次いで23℃、50%RHの温湿度条件下
に24時間乾燥した後の収縮率が下記式[1]を満足す
ることを特徴とするフォトレジスト用二軸延伸ポリエス
テルフィルムに存する。
That is, the gist of the present invention is that 60%
A biaxially stretched polyester film for photoresist is characterized in that the shrinkage rate after being immersed for seconds and then dried under temperature and humidity conditions of 23° C. and 50% RH for 24 hours satisfies the following formula [1].

αNil+α7D≦1.4  ・・・  ■以下、本発
明を更に詳細に説明する。
αNil+α7D≦1.4 (2) The present invention will be explained in more detail below.

本発明にいうポリエステルとはテレフタル酸イソフタル
酸、及びナフタレン−2,6−ジカルボン酸のような芳
香族ジカルボン酸、又はそのエステルとエチレングリコ
ール、ジエチレングリコール、テトラメチレングリコー
ル、及びネオペンチルグリコール等のジオールとを重縮
合させて得ることの出来る結晶性芳香族ポリエステルで
ある。
Polyester as used in the present invention refers to aromatic dicarboxylic acids such as terephthalic acid isophthalic acid and naphthalene-2,6-dicarboxylic acid, or esters thereof and diols such as ethylene glycol, diethylene glycol, tetramethylene glycol, and neopentyl glycol. It is a crystalline aromatic polyester that can be obtained by polycondensation of

かかるポリエステルは芳香族ジカルボン酸とグリコール
を直接重縮合させて得られる他、芳香族ジカルボン酸ジ
アルキルエステルとグリコールをエステル交換反応させ
た後、重縮合させる、あるいは芳香族ジカルボン酸のジ
グリコールエステルを重縮合させる等の方法によっても
得られる。
Such polyesters can be obtained by directly polycondensing aromatic dicarboxylic acids and glycols, or by polycondensing aromatic dicarboxylic acid dialkyl esters and glycols after transesterification, or by polycondensing diglycol esters of aromatic dicarboxylic acids. It can also be obtained by a method such as condensation.

ポリマーの代表的なものとして、ポリエチレンテレフタ
レート、ポリエチレン−2,6−ナフタレート、ポリテ
トラメチレンテレフタレート及びポリテトラメチレン−
2,6−ナフタレート等であり、例えばポリエチレンテ
レフタレート、あるいはポリエチレン−2,6−ナフタ
レートはテレフタル酸あるいはナフタレン−2,6−ジ
カルボン酸とエチレングリコールとが結合したポリエス
テルのみならず、繰り返し単位の80モル%以上がエチ
レンテレフタレートあるいはエチレン−2゜6−ナフタ
レート単位より成る繰り返し単位の20モル%以下が他
の成分である共重合ポリエステル、またはこれらのポリ
エステルに他のポリマーを添加、混合した混合ポリエス
テルである。
Typical polymers include polyethylene terephthalate, polyethylene-2,6-naphthalate, polytetramethylene terephthalate, and polytetramethylene-
2,6-naphthalate, etc. For example, polyethylene terephthalate or polyethylene-2,6-naphthalate is not only a polyester in which terephthalic acid or naphthalene-2,6-dicarboxylic acid and ethylene glycol are bonded, but also 80 moles of repeating units. A copolymerized polyester in which 20 mol% or less of repeating units consisting of ethylene terephthalate or ethylene-2゜6-naphthalate units is other components, or a mixed polyester obtained by adding and mixing other polymers to these polyesters. .

また、本発明においては、塩化メチレンに対し一層カー
ルし難い特性を付与するために、原料ポリエステルに分
子量が200〜10000、好ましくは200〜500
0の範囲内の有機物を配合して用いるのが好ましい。
In addition, in the present invention, in order to impart properties that make it more difficult for methylene chloride to curl, the raw material polyester has a molecular weight of 200 to 10,000, preferably 200 to 500.
It is preferable to mix and use an organic substance within the range of 0.

上記有機物としては、脂肪族炭化水素、脂肪族エステル
、アルキレンビス脂肪族アミド、アルキレンビス芳香族
アミド等が好ましく用いられる。
As the organic substance, aliphatic hydrocarbons, aliphatic esters, alkylene bis aliphatic amides, alkylene bis aromatic amides, etc. are preferably used.

その添加量としては、ポリエステルに対し、lOppm
以上1)0000pp以下である。好ましくは20pp
m以上2000ppm以下である。更に好ましくは30
ppm以上1)000pp以下である。1o ppm以
下では、効果が極めて小さく、逆に1)0000pp以
上では、フィルム表面に滑剤がブリードアウトする恐れ
があるので不適当である。
The amount added is lOppm based on polyester.
The above is 1) 0000 pp or less. Preferably 20pp
m or more and 2000 ppm or less. More preferably 30
ppm or more 1) 000pp or less. If the amount is less than 10 ppm, the effect will be extremely small, and if it is more than 10,000 ppm, the lubricant may bleed out onto the film surface, which is inappropriate.

また、ポリエステルの重合度は、これが低すぎると機械
的特性が低下するので、固有粘度が0.40以上、好ま
しくはO,SO〜0.90、更に好ましくは0.55〜
0.85の範囲内の重合度のものを使用するのがよい。
In addition, if the polymerization degree of the polyester is too low, the mechanical properties will deteriorate, so the intrinsic viscosity should be 0.40 or more, preferably O,SO~0.90, more preferably 0.55~0.
It is preferable to use a polymer having a degree of polymerization within the range of 0.85.

本発明においては、フィルムに滑り性を付与するため、
微粒子を含有せしめることが出来る。滑り性を付与する
微粒子としては、例えばカオリン、クレー、炭酸カルシ
ウム、酸化ケイ素等の公知の不活性外部粒子が挙げられ
る。微粒子の添加量は、特に限定されないが、通常0.
0 O5〜2重量%含有させることが好ましい。また、
粒子の平均粒径としては0.005〜5.0μmの範囲
にあるものが好ましい。
In the present invention, in order to impart slipperiness to the film,
Fine particles can be contained. Examples of fine particles that impart slipperiness include known inert external particles such as kaolin, clay, calcium carbonate, and silicon oxide. The amount of fine particles added is not particularly limited, but is usually 0.
It is preferable to contain 0 O5 to 2% by weight. Also,
The average particle diameter of the particles is preferably in the range of 0.005 to 5.0 μm.

また、これらの粒子に加え、必要に応じて染料、顔料、
着色剤、安定剤、帯電防止剤、導電性物質、酸化防止剤
、消泡剤等の化合物を配合してもよい。
In addition to these particles, dyes, pigments,
Compounds such as colorants, stabilizers, antistatic agents, conductive substances, antioxidants, and antifoaming agents may be added.

本発明者らは、塩化メチレンで処理後のフィルムがカー
ルする要因を種々の面から検討した結果、このようなカ
ールを起り難くさせるためには、20°Cの塩化メチレ
ン中に60秒間浸漬し、次いで、23℃、50%RHの
温湿度条件下に24時間乾燥した後における、フィルム
の縦方向の収縮率(α14Ill)及び横方向の収縮率
(αTD)の和(αMD+αTD)を1.4%以下に制
御することが極めて有効であることを見い出した。収縮
率の和は、好ましくは、−0,1%以上かつ1.2%以
下、更に好ましくは−0,1%以上かつ1.0%以下で
ある。収縮率の和が164%より大きい場合、塩化メチ
レンで処理後のフィルムのカールの度合いが大きく不適
当である。収縮率の和が−0,1%未満のフィルム、即
ち、膨張するようなフィルムでは、塩化メチレンで処理
した際のフィルムの平面性を維持するのが困難となる。
The inventors of the present invention investigated the factors that cause the film to curl after being treated with methylene chloride from various aspects, and found that in order to prevent such curling from occurring, the film should be immersed in methylene chloride at 20°C for 60 seconds. Then, after drying for 24 hours under the temperature and humidity conditions of 23° C. and 50% RH, the sum of the longitudinal shrinkage rate (α14Ill) and the transverse shrinkage rate (αTD) of the film (αMD+αTD) is 1.4. It has been found that it is extremely effective to control it to % or less. The sum of the shrinkage percentages is preferably -0.1% or more and 1.2% or less, more preferably -0.1% or more and 1.0% or less. If the sum of the shrinkage rates is greater than 164%, the degree of curl of the film after treatment with methylene chloride is large and unsuitable. If the sum of the shrinkage rates is less than -0.1%, that is, if the film swells, it will be difficult to maintain the flatness of the film when treated with methylene chloride.

本発明においては、上記の収縮率における縦方向の収縮
率と横方向の収縮率の差(α。−αア、)は、−0,2
%以上0.2%以下、好ましくは−0,1%以上0.1
%以下にするのがよい。収縮率の差が一〇、2%未満或
いは0.2%を越えるフィルムでは、フィルムを塩化メ
チレンで処理した場合の収縮量の異方性が大きくカール
が発生しやすくなる。
In the present invention, the difference (α.-αa,) between the shrinkage percentage in the longitudinal direction and the shrinkage percentage in the lateral direction in the above shrinkage percentage is -0,2
% or more and 0.2% or less, preferably -0.1% or more and 0.1
It is best to keep it below %. If the difference in shrinkage rate is less than 10.2% or more than 0.2%, the anisotropy of the amount of shrinkage when the film is treated with methylene chloride is large and curling is likely to occur.

本発明においては、横方向の上記収縮率αア、の値は0
.7%以下、好ましくは−0,1%以上0.6%以下、
特に好ましくは−0,1%以上0.5%以下にするのが
よい。αア、の値が0.7%を越えるフィルムでは、ロ
ールから巻き出し塩化メチレンで連続的に処理してロー
ルに巻き取る場合、横方向のカールの度合が大きくなり
好ましくない。また、0.1%未満のフィルムでは塩化
メチレン処理時に平面性が保てず好ましくない。
In the present invention, the value of the contraction rate αa in the lateral direction is 0.
.. 7% or less, preferably -0.1% or more and 0.6% or less,
Particularly preferably, the content is -0.1% or more and 0.5% or less. When a film having an α value exceeding 0.7% is unwound from a roll, treated continuously with methylene chloride, and then wound onto a roll, the degree of curl in the lateral direction becomes large, which is undesirable. In addition, if the amount of the film is less than 0.1%, flatness cannot be maintained during treatment with methylene chloride, which is not preferable.

本発明者らの考察によれば、フィルムの片面を塩化メチ
レンで処理した際にフィルムがカールするのは、主とし
て、塩化メチレンによるフィルムの局所的な収縮による
ものと考えられ、収縮率を適正な値に限定することによ
り、フィルムの前記カールを最低限に抑えられるものと
考えられる。
According to the inventors' considerations, the reason why the film curls when one side of the film is treated with methylene chloride is thought to be mainly due to local shrinkage of the film due to methylene chloride, and the shrinkage rate must be adjusted appropriately. It is believed that by limiting the amount to a certain value, the curling of the film can be suppressed to a minimum.

本発明においては、150t5分間熱処理した際のフィ
ルムの巾方向の加熱収縮率は、−0,1%以上かつ0.
5%以下であることが好ましく、−〇。
In the present invention, the heat shrinkage rate in the width direction of the film when heat treated at 150t for 5 minutes is -0.1% or more and 0.1% or more.
It is preferably 5% or less, -〇.

1%以上かつ0.3%以下であることが更に好ましい。It is more preferably 1% or more and 0.3% or less.

上記条件下でのフィルムの巾方向の加熱収縮率が−0,
1%未満、すなわち、膨張するようなフィルムである場
合、或いは0.5%より大きい場合には、塩化メチレン
でフィルムを処理した後の収縮率が大きくなり、その結
果として、塩化メチレンで処理後のフィルムのカールの
度合いが大きくなり不適当である。
The heat shrinkage rate in the width direction of the film under the above conditions is -0,
If it is less than 1%, i.e., the film will swell, or if it is more than 0.5%, the shrinkage after treatment with methylene chloride will be large; The degree of curl of the film increases, which is inappropriate.

また、本発明においては、フィルムの面配向度(ΔP)
は、0.150〜0.180の範囲にあることが好まし
く、0.160〜0.180の範囲にあることが更に好
ましい。面配向度(八P)が0.150未満或いは0.
180を越えるフィルムでは、塩化メチレンで処理後の
フィルムのカールの度合いが太き(なり不適当である。
In addition, in the present invention, the plane orientation degree (ΔP) of the film
is preferably in the range of 0.150 to 0.180, more preferably in the range of 0.160 to 0.180. The plane orientation degree (8P) is less than 0.150 or 0.
For films exceeding 180, the degree of curl of the film after treatment with methylene chloride is large (and unsuitable).

更に、本発明においては、フィルムの平均屈折率(n)
は、1.6050〜1.6085(7)範囲にあること
が好ましく、1.6060〜1.6085の範囲にある
ことが更に好ましい。平均屈折率(丁)が1.6050
未満では塩化メチレンで処理後のフィルムのカールの度
合いが大きくなり不適当である。
Furthermore, in the present invention, the average refractive index (n) of the film
is preferably in the range of 1.6050 to 1.6085(7), more preferably in the range of 1.6060 to 1.6085. Average refractive index (di) is 1.6050
If it is less than that, the degree of curling of the film after treatment with methylene chloride becomes large, which is unsuitable.

次に、本発明のフィルムの製膜方法を具体的に述べる。Next, the method for forming the film of the present invention will be specifically described.

本発明のフィルムは、前記のポリエステルを通常280
〜320℃の範囲の温度で押出機よりシート状に押し出
し約70℃以下の温度に冷却して実質的に無定形のシー
トとし、次いで得られたシート状物を縦及び樽方向に1
5倍以上に延伸して二軸配向ポリエステルフィルムとし
、更に得られたフィルムを220〜260℃の範囲の温
度で熱処理することにより得ることができる。
The film of the present invention usually contains the above-mentioned polyester with a 280%
A sheet is extruded from an extruder at a temperature in the range of ~320°C, cooled to a temperature of about 70°C or less to form a substantially amorphous sheet, and then the resulting sheet is rolled lengthwise and in the barrel direction.
It can be obtained by stretching 5 times or more to obtain a biaxially oriented polyester film, and then heat-treating the obtained film at a temperature in the range of 220 to 260°C.

特に、面配向度をあげるために、再縦延伸及び/又は再
横延伸、熱固定時巾出し、縦多段延伸等を適用すること
は好ましい形態である。
Particularly, in order to increase the degree of plane orientation, it is preferable to apply longitudinal re-stretching and/or transverse re-stretching, widening during heat setting, longitudinal multi-stage stretching, etc.

また、特に、熱固定時及び熱固定後冷却過程において、
0.1〜25%好ましくは2〜20%の巾弛緩を適用す
ることも本発明のフィルムを得るための好ましい形態の
1つである。本発明のフィルムは、上記範囲内で条件を
適宜選択することにより得ることができ、その厚みは通
常50〜200μm、好ましくは10〜1)00uであ
る。
In addition, especially during heat setting and during the cooling process after heat setting,
Applying a width relaxation of 0.1 to 25%, preferably 2 to 20% is also one of the preferred forms for obtaining the film of the invention. The film of the present invention can be obtained by appropriately selecting conditions within the above range, and its thickness is usually 50 to 200 μm, preferably 10 to 1)00 μm.

〔実施例〕〔Example〕

以下に実施例にて本発明を具体的に説明するが、本発明
はこれら実施例に限定されるものではない。
The present invention will be specifically explained below with reference to Examples, but the present invention is not limited to these Examples.

なお、フィルムの評価方法を以下に示す。In addition, the evaluation method of the film is shown below.

(1)塩化メチレンに浸漬した際のフィルムのカールし
やすさの評価 巾300mm、長さ500mのロール状の評価フィルム
を巻取り張力0.5 kg/mm” 、巻取り速度29
m/HiHにて巻取り、その際フィルムの片面に、塩化
メチレンを1.0 m l /minの速度で塗布した
のち圧空を吹きつけて乾燥した。塩化メチレンを塗布し
た側の巾方向にカールしたフィルムのカールの度合を目
視で評価し、以下のランクに分類した。
(1) Evaluation of ease of curling of film when immersed in methylene chloride A roll-shaped evaluation film with a width of 300 mm and a length of 500 m was wound up at a tension of 0.5 kg/mm and a winding speed of 29.
Methylene chloride was applied to one side of the film at a rate of 1.0 ml/min, and then dried by blowing compressed air. The degree of curl of the film curled in the width direction on the side to which methylene chloride was applied was visually evaluated and classified into the following ranks.

ランク:◎ (極めて良好) ランク:○ (良好) ランク:△ (やや不良) ランク:×(不良) (2)塩化メチレンに浸漬し、乾燥した際のフィルムの
収縮率の測定方法 20°Cの塩化メチレンに、巾10mm、長さ150m
m(標点間100mm)の評価フィルムの両面を60秒
間浸漬した。その後、フィルムを23℃、50%RHの
温湿度条件下にて24時間乾燥し、評価フィルムの標点
間の長さを測定することにより収縮率を次式にて計算し
た。
Rank: ◎ (Extremely Good) Rank: ○ (Good) Rank: △ (Slightly Poor) Rank: × (Poor) (2) Method for measuring the shrinkage rate of a film when immersed in methylene chloride and dried at 20°C In methylene chloride, width 10 mm, length 150 m
Both sides of the evaluation film of m (gauge distance 100 mm) were immersed for 60 seconds. Thereafter, the film was dried for 24 hours under a temperature and humidity condition of 23° C. and 50% RH, and the shrinkage rate was calculated by the following formula by measuring the length between the gauge marks of the evaluation film.

収縮率(%)= (3)熱収縮率 無張力状態で、150℃、5分間熱処理しその前後のサ
ンプルの長さを測定することにより次式にて計算した。
Shrinkage rate (%) = (3) Heat shrinkage rate Calculated using the following formula by heat-treating the sample at 150° C. for 5 minutes under no tension and measuring the length of the sample before and after that.

加熱収縮率(%)= (4)面配向度及び平均屈折率 フィルムの屈折率の測定は、アタゴ■製アツへの屈折計
を使用し、光源にはナトリウムランプを用いて行なった
Heating shrinkage rate (%) = (4) Degree of plane orientation and average refractive index The refractive index of the film was measured using a refractometer manufactured by Atago Corporation and a sodium lamp as a light source.

フィルム面内の最大の屈折率nア、それに直角方向の屈
折率n5、及び厚さ方向の屈折率n工を求め、面配向度
及び平均屈折率を算出した。
The maximum refractive index n in the film plane, the refractive index n5 in the direction perpendicular to it, and the refractive index n in the thickness direction were determined, and the degree of plane orientation and the average refractive index were calculated.

(5)極限粘度(η〕 ポリマー1gをフェノール/テトラクロルエタン−50
150(重量比)の混合溶媒100m1に溶解し落下式
粘度計を用い30°Cで測定した。
(5) Intrinsic viscosity (η) 1 g of polymer was mixed with phenol/tetrachloroethane-50
It was dissolved in 100 ml of a mixed solvent of 150 (weight ratio) and measured at 30°C using a drop viscometer.

次に、実施例及び比較例で用いたフィルムの製造方法を
示す。
Next, a method for manufacturing the films used in Examples and Comparative Examples will be described.

実施例1 1.3crmの5tOzが90ppm、−次粒径30μ
mのSiO□が1)00pp、ヘキサメチレンビスベヘ
ンアミド(有機滑剤)が200ppmとなるように調整
したポリエチレンテレフタレート樹脂を常法により乾燥
し290℃で溶融押出し冷却固化し無定形シートを得た
Example 1 5tOz of 1.3crm is 90ppm, -order particle size 30μ
A polyethylene terephthalate resin adjusted to have a SiO□ of 1)00 ppm and a hexamethylene bisbehenamide (organic lubricant) of 200 ppm was dried by a conventional method, melt-extruded at 290° C., cooled and solidified to obtain an amorphous sheet.

先ず、上記無定形シートを83℃で2゜9倍縦延伸した
のち、更に78°Cで1.5倍縦延伸し、次にテンター
で1)0℃で4.0倍横延伸し、次いで247℃で巾方
向に5%の弛緩を与えながら熱固定して厚さ25μmの
フィルムを得た。得られたフィルムの物性及び特性を表
1に示す。
First, the above amorphous sheet was longitudinally stretched 2°9 times at 83°C, further longitudinally stretched 1.5x at 78°C, then transversely stretched 4.0x at 0°C using a tenter, and then The film was heat-set at 247° C. while being relaxed by 5% in the width direction to obtain a film with a thickness of 25 μm. Table 1 shows the physical properties and characteristics of the obtained film.

実施例2 1、3 p mのSin、が60ppm、−次粒径30
μmのS i Ozが120ppmとなるように調整し
たポリエチレンテレフタレート樹脂を常法により乾燥し
、290℃で溶融押出し冷却固化し無定形シートを得た
Example 2 1,3 pm of Sin, 60 ppm, -order particle size 30
A polyethylene terephthalate resin adjusted to have a S i Oz in μm of 120 ppm was dried by a conventional method, melt-extruded at 290° C., cooled and solidified to obtain an amorphous sheet.

先ず、上記無定形シートを83℃で2.9倍縦延伸した
のち、更に78゛Cで1.5倍縦延伸し、次にテンター
で1)0℃で4.0倍横延伸したのち、緊張固定下で2
47℃にて熱固定し、次いで220°Cで中方向に8%
の弛緩を与えて厚さ25μmのフィルムを得た。得られ
たフィルムの物性及び特性を表1に示す。
First, the above amorphous sheet was longitudinally stretched 2.9 times at 83°C, then further longitudinally stretched 1.5 times at 78°C, and then 4.0 times transversely stretched at 1) 0°C using a tenter. 2 under tension fixation
Heat set at 47℃, then 8% in the middle direction at 220℃
A film with a thickness of 25 μm was obtained. Table 1 shows the physical properties and characteristics of the obtained film.

比較例1 実施例2の無定形シートを用い、実施例2と同じ条件で
縦延伸及び横延伸をしたのち、緊張固定下で247℃に
て熱固定して厚さ25μmのフィルムを得た。得られた
フィルムの物性及び特性を表1に示す。
Comparative Example 1 The amorphous sheet of Example 2 was longitudinally stretched and transversely stretched under the same conditions as Example 2, and then heat-set at 247° C. under tension fixation to obtain a film with a thickness of 25 μm. Table 1 shows the physical properties and characteristics of the obtained film.

比較例2 実施例2の無定形シートを用い、実施例2と同じ条件で
縦延伸及び横延伸をしたのち、220℃で巾方向に8%
の弛緩を与えながら熱固定して厚さ25μmのフィルム
を得た。得られたフィルムの物性及び特性を表1に示す
Comparative Example 2 The amorphous sheet of Example 2 was longitudinally stretched and transversely stretched under the same conditions as Example 2, and then stretched by 8% in the width direction at 220°C.
A film having a thickness of 25 μm was obtained by heat setting while giving relaxation. Table 1 shows the physical properties and characteristics of the obtained film.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、溶剤現像型フォトレジストフィルムに
おいて、塩化メチレンで処理してポリエステル層を感光
層から除去する際、カールし難い特性を有するフォトレ
ジスト用ベースフィルムを製造することができ、その工
業的価値は高い。
According to the present invention, it is possible to produce a base film for a photoresist that is resistant to curling when a polyester layer is removed from a photosensitive layer by treatment with methylene chloride in a solvent-developed photoresist film, The value is high.

Claims (1)

【特許請求の範囲】[Claims] (1)20℃の塩化メチレン中に60秒間浸漬し、次い
で、23℃、50%RHの温湿度条件下に24時間乾燥
した後の収縮率が下記式[1]を満足することを特徴と
するフォトレジスト用二軸延伸ポリエステルフィルム。 α_M_D+α_T_D≦1.4・・・[1] 〔α_M_D;縦方向の収縮率(%) α_T_D;横方向の収縮率(%)〕
(1) The shrinkage rate after immersing in methylene chloride at 20°C for 60 seconds and then drying for 24 hours under the temperature and humidity conditions of 23°C and 50% RH satisfies the following formula [1]. Biaxially oriented polyester film for photoresist. α_M_D+α_T_D≦1.4...[1] [α_M_D; Vertical contraction rate (%) α_T_D; Transverse contraction rate (%)]
JP7358789A 1989-03-24 1989-03-24 Biaxially stretched polyester film for photoresist Pending JPH02251854A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7358789A JPH02251854A (en) 1989-03-24 1989-03-24 Biaxially stretched polyester film for photoresist

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7358789A JPH02251854A (en) 1989-03-24 1989-03-24 Biaxially stretched polyester film for photoresist

Publications (1)

Publication Number Publication Date
JPH02251854A true JPH02251854A (en) 1990-10-09

Family

ID=13522593

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7358789A Pending JPH02251854A (en) 1989-03-24 1989-03-24 Biaxially stretched polyester film for photoresist

Country Status (1)

Country Link
JP (1) JPH02251854A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06110211A (en) * 1992-09-25 1994-04-22 Nippon Paper Ind Co Ltd Photosensitive sheet
JP2005208635A (en) * 1999-06-24 2005-08-04 Hitachi Chem Co Ltd Resist pattern, substrate with overlying resist pattern, process for producing wiring pattern, and wiring pattern

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06110211A (en) * 1992-09-25 1994-04-22 Nippon Paper Ind Co Ltd Photosensitive sheet
JP2005208635A (en) * 1999-06-24 2005-08-04 Hitachi Chem Co Ltd Resist pattern, substrate with overlying resist pattern, process for producing wiring pattern, and wiring pattern

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