JPH0362180B2 - - Google Patents
Info
- Publication number
- JPH0362180B2 JPH0362180B2 JP24133783A JP24133783A JPH0362180B2 JP H0362180 B2 JPH0362180 B2 JP H0362180B2 JP 24133783 A JP24133783 A JP 24133783A JP 24133783 A JP24133783 A JP 24133783A JP H0362180 B2 JPH0362180 B2 JP H0362180B2
- Authority
- JP
- Japan
- Prior art keywords
- pei
- film
- solvent
- weight
- trichloroethane
- 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.)
- Expired
Links
Classifications
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05K—PRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
- H05K1/00—Printed circuits
- H05K1/02—Details
- H05K1/03—Use of materials for the substrate
- H05K1/0313—Organic insulating material
- H05K1/032—Organic insulating material consisting of one material
- H05K1/0346—Organic insulating material consisting of one material containing N
Landscapes
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Moulding By Coating Moulds (AREA)
Description
本発明は、ポリエーテルイミド(以下「PEI」
という)を溶剤に溶解して流延し、PEIフイルム
を製造する方法に関する。
PEIは耐熱性に優れたエンジニアリングプラス
チツクとして知られており、印刷配線基板、記憶
媒体基材、電気絶縁材等に適している。そして、
そのフイルムを製造するには溶融押出法が普通に
考えられるが、溶融押出法では厚さ精度の高いフ
イルムを得るのが困難な面がある。
そこで厚さ精度の良いフイルムを得る方法とし
て流延法が考えられるが、一般にPEI等のエンジ
ニアリングプラスチツクは、耐熱性、耐溶剤性が
優れているので、適当な溶剤の選択が難しく、高
品質のフイルムを得るためには、この溶剤の選定
が重要である。
本発明は、PEIを溶解して流延するための溶剤
について種々検討の結果、特定の混合溶剤が特に
好ましいことを見出したものであつて、その特徴
は、1,1,2−トリクロロエタン、1,1,1
−トリクロロエタン及び1,2−ジクロロエチレ
ンの混合液を溶剤として用いる点にある。
以下本発明を詳しく説明する。
本発明にいうPEIは、
なる構造を有するものが代表的なものである。こ
のPEIを溶解する溶剤としては、
(1) 1,1,2−トリクロロエタン
(ClCH2CHCl2、沸点114℃) 50〜95重量%
(2) 1,1,1−トリクロロエタン(CH3CCl3、
沸点74℃) 3〜30重量%
(3) 1,2−ジクロロエタン(ClCH2CH2Cl、沸
点84℃) 2〜20重量%
の混合溶剤を用いる。
1,1,2−トリクロロエタンは、ある程度の
PEI溶解能を有し、また沸点が高いのでPEI流延
用溶剤に適しているが、それのみでは高濃度の
PEIを完全に溶解し得ず、また沸点が高すぎて流
延後の溶剤除去速度が遅くなる。
ところが、これに1,2−ジクロロエタンを2
重量%以上混合するとPEI溶解能が大幅に向上す
る。しかし1,2−ジクロロエタンは沸点が低い
ので、これが20重量%をこえると、混合液の飛散
が速くなるため、溶剤を除去して製膜するときの
条件制御が難しくなる。また1,2−ジクロロエ
タンが多いと、流延用支持体(スチールベルト
等)からの膜の剥離が困難になる傾向があるので
その量は20重量%以内とする。
さらに1,1,1−トリクロロエタンを3重量
%以上混合すると、流延用支持体からの膜の剥離
が容易になり、また膜から溶剤を除去するときの
条件範囲が広くなつて、制御が容易になる現象が
見られる。しかし30重量%をこえると混合溶剤の
PEI溶解能が大幅に低下して白濁した膜しか得ら
れないので、30重量%以下に抑える必要がある。
上記3種の溶剤の混合溶剤は、PEI溶解能が実
用上充分ありまたこの混合溶剤は適度の飛散性を
有し、また流延用支持体からの膜の剥離も容易で
あるから、特に薄いフイルムの製造に最適であ
る。この場合、PEI溶液の濃度は、25℃におい粘
度が約8000CPS以上となるようにすれば、流延し
たときに厚さの均一なフイルムが得られて好まし
い。
本発明方法においては、上記3種類の溶剤をま
ず混合し、その混合溶剤にPEIを溶解させる。
1種または2種の溶剤とPEIとを混合し、次い
で残りの溶剤を加えると、溶液が白濁して攪拌し
ても透明状態に戻らないことが多い。
かくして得られたPEI溶液を流延する方法とし
ては、金属ベルト、ガラス板、ポリエステルフイ
ルム等の支持体に上に、PEI溶液を口金から膜状
に吐出して流延する方法が普通であるが、ロール
コーター等によりPEI溶液を支持体上に膜状に塗
布する方法によることもできる。
次に実施例により本発明方法を更に具体的に説
明する。
〔実施例〕
3種類の溶剤を第1表に示す各種割合で混合し
た混合溶剤400gにPEI100gを加え、70℃で50時
間攪拌してPEI溶液を得た。そして各溶液をアプ
リケーターでガラス板上に塗布し、次いで60℃で
30秒間加熱して溶剤のほぼ97%が除去されるよう
乾燥し、さらに形成された膜をガラス板上でアニ
ーリングして溶剤を完全に除去してから剥離して
厚さ15μmのフイルムを得た。
各フイルムについてフイルム外観、支持体から
の剥離性、及びアニーリング条件範囲を評価し、
その結果を第1表に併記した。
なおアニーリング条件範囲は、140℃×5分よ
りも高温(または長時間)であれば溶剤が完全に
除去されるものを(○)、180℃×10分またはそれ
よりも苛酷な条件が必要なものを(×)とした。
The present invention uses polyetherimide (hereinafter referred to as "PEI")
) is dissolved in a solvent and cast, thereby producing a PEI film. PEI is known as an engineering plastic with excellent heat resistance, and is suitable for printed wiring boards, storage media base materials, electrical insulation materials, etc. and,
Melt extrusion is generally considered to be a method for producing such films, but it is difficult to obtain films with high thickness accuracy using melt extrusion. Therefore, the casting method can be considered as a method to obtain a film with good thickness accuracy, but engineering plastics such as PEI generally have excellent heat resistance and solvent resistance, so it is difficult to select an appropriate solvent, and it is difficult to obtain high-quality films. Selection of this solvent is important in order to obtain a film. In the present invention, as a result of various studies on solvents for dissolving and casting PEI, it was discovered that a specific mixed solvent is particularly preferable, and its characteristics include 1,1,2-trichloroethane, 1 ,1,1
- A mixed solution of trichloroethane and 1,2-dichloroethylene is used as a solvent. The present invention will be explained in detail below. The PEI referred to in the present invention is A typical example is one having the following structure. Solvents for dissolving this PEI include (1) 1,1,2-trichloroethane (ClCH 2 CHCl 2 , boiling point 114°C) 50 to 95% by weight (2) 1,1,1-trichloroethane (CH 3 CCl 3 ,
A mixed solvent of 3-30% by weight (3) 1,2-dichloroethane (ClCH 2 CH 2 Cl, boiling point 84°C) 2-20% by weight is used. 1,1,2-trichloroethane has some
It has the ability to dissolve PEI and has a high boiling point, so it is suitable as a solvent for PEI casting, but it is not sufficient to use it alone as a solvent for high concentrations.
PEI cannot be completely dissolved, and the boiling point is too high, which slows down the solvent removal rate after casting. However, when 1,2-dichloroethane was added to this
Mixing more than % by weight greatly improves PEI dissolving ability. However, since 1,2-dichloroethane has a low boiling point, if it exceeds 20% by weight, the mixed liquid will scatter quickly, making it difficult to control conditions when removing the solvent and forming a film. Moreover, if the amount of 1,2-dichloroethane is too large, it tends to become difficult to peel off the film from the casting support (such as a steel belt), so the amount should be within 20% by weight. Furthermore, when 3% by weight or more of 1,1,1-trichloroethane is mixed, the membrane can be easily peeled from the casting support, and the range of conditions for removing the solvent from the membrane can be expanded, making control easier. A phenomenon can be seen. However, if it exceeds 30% by weight, the mixed solvent
Since the PEI dissolving ability is significantly reduced and only a cloudy film is obtained, it is necessary to keep the amount below 30% by weight. A mixed solvent of the above three types of solvents has sufficient PEI dissolving ability for practical purposes, and this mixed solvent has appropriate scattering properties, and the film can be easily peeled off from the casting support, so it is especially suitable for thin films. Ideal for film production. In this case, it is preferable to set the concentration of the PEI solution such that the viscosity at 25° C. is about 8000 CPS or more, so that a film with a uniform thickness can be obtained when cast. In the method of the present invention, the above three types of solvents are first mixed, and PEI is dissolved in the mixed solvent. When one or two solvents and PEI are mixed and then the remaining solvent is added, the solution often becomes cloudy and does not return to a clear state even after stirring. The method of casting the PEI solution obtained in this way is usually to discharge the PEI solution in a film form from a die onto a support such as a metal belt, glass plate, or polyester film. Alternatively, the PEI solution may be coated onto the support in a film form using a roll coater or the like. Next, the method of the present invention will be explained in more detail with reference to Examples. [Example] 100 g of PEI was added to 400 g of a mixed solvent prepared by mixing three types of solvents in various ratios shown in Table 1, and the mixture was stirred at 70° C. for 50 hours to obtain a PEI solution. Each solution was then applied onto a glass plate using an applicator, and then heated at 60°C.
The film was dried by heating for 30 seconds to remove approximately 97% of the solvent, and the formed film was annealed on a glass plate to completely remove the solvent and then peeled off to obtain a 15 μm thick film. . For each film, evaluate the film appearance, peelability from the support, and annealing condition range,
The results are also listed in Table 1. The range of annealing conditions is one in which the solvent is completely removed at a higher temperature (or longer time) than 140°C for 5 minutes (○), and one in which the solvent is completely removed at 180°C for 10 minutes or more severe conditions. The items were marked with an (x).
【表】【table】
【表】
第1表の結果から明らかなように、溶剤の混合
比率が本発明の範囲内にあるNo.3、5〜6及び8
は、各種特性がいずれも優れている。
比較例 1
溶剤として塩化メチレン30重量%、1,1,2
−トリクロロエタン70重量%からなる混合溶剤を
用いた以外は実施例と同様にしてフイルムを得た
が、雰囲気が多湿の場合にはフイルム外観は不透
明となり、良好なものが得られなかつた。
これは塩化メチレンの飛散が速く蒸発潜熱を奪
うため、雰囲気中の水分が膜表面に結露して、膜
表面が微細な水滴を巻込んだ状態になるためと考
えられる。
比較例 2
1,1,2−トリクロロエタン200gと1,2
−ジクロロエタン80gを混合した溶液にPEI100
gを加え、70℃で50時間攪拌して透明な溶液を得
た。そしてこれに70℃に加熱した1,1,1−ト
リクロロエタン120gを添加したところ白濁した
ので、70℃で1時間攪拌したが透明な溶液は得ら
れなかつた。
比較例 3
1,1,2−トリクロロエタン200gと1,1,
1−トリクロロエタン120gの混合溶剤にPEIを
溶解させ、次いで1,2−ジクロロエタン80gを
添加して、比較例2と同様の操作をしたが、白濁
した溶液しか得られなかつた。[Table] As is clear from the results in Table 1, Nos. 3, 5 to 6, and 8 in which the mixing ratio of the solvent is within the range of the present invention.
is excellent in all properties. Comparative Example 1 30% by weight of methylene chloride as a solvent, 1,1,2
A film was obtained in the same manner as in Example except that a mixed solvent consisting of 70% by weight of trichloroethane was used, but when the atmosphere was humid, the appearance of the film became opaque and a good film could not be obtained. This is thought to be because the methylene chloride scatters quickly and takes away the latent heat of vaporization, so that moisture in the atmosphere condenses on the film surface, and the film surface becomes engulfed with fine water droplets. Comparative example 2 200g of 1,1,2-trichloroethane and 1,2
- Add PEI100 to a solution of 80g of dichloroethane.
g was added and stirred at 70°C for 50 hours to obtain a clear solution. When 120 g of 1,1,1-trichloroethane heated to 70°C was added to this, the mixture became cloudy, so although the mixture was stirred at 70°C for 1 hour, no clear solution was obtained. Comparative Example 3 200g of 1,1,2-trichloroethane and 1,1,
PEI was dissolved in a mixed solvent of 120 g of 1-trichloroethane, then 80 g of 1,2-dichloroethane was added, and the same operation as in Comparative Example 2 was carried out, but only a cloudy solution was obtained.
Claims (1)
造するにあたり、溶剤として1,1,2−トリク
ロロエタン50〜95重量%、1,1,1−トリクロ
ロエタン3〜30重量%及び1,2−ジクロロエタ
ン2〜20重量%を混合し、その混合溶剤にポリエ
ーテルイミドを溶解して流延することを特徴とす
る方法。1. When producing a polyetherimide film by a casting method, 1,1,2-trichloroethane 50-95% by weight, 1,1,1-trichloroethane 3-30% by weight, and 1,2-dichloroethane 2-95% by weight are used as solvents. A method characterized by mixing 20% by weight of polyetherimide, dissolving the polyetherimide in the mixed solvent, and casting the solution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24133783A JPS60132714A (en) | 1983-12-21 | 1983-12-21 | Preparation of polyetherimide film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24133783A JPS60132714A (en) | 1983-12-21 | 1983-12-21 | Preparation of polyetherimide film |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60132714A JPS60132714A (en) | 1985-07-15 |
| JPH0362180B2 true JPH0362180B2 (en) | 1991-09-25 |
Family
ID=17072797
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24133783A Granted JPS60132714A (en) | 1983-12-21 | 1983-12-21 | Preparation of polyetherimide film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60132714A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5283350B2 (en) * | 2007-04-25 | 2013-09-04 | Sabicイノベーティブプラスチックスジャパン合同会社 | Polyetherimide film for capacitors |
| DE102008009069A1 (en) * | 2008-02-13 | 2009-08-20 | Gkss-Forschungszentrum Geesthacht Gmbh | Coating of a Magnesuimbauteils |
-
1983
- 1983-12-21 JP JP24133783A patent/JPS60132714A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60132714A (en) | 1985-07-15 |
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