JP5064705B2 - Method for manufacturing foam substrate - Google Patents
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- JP5064705B2 JP5064705B2 JP2006086997A JP2006086997A JP5064705B2 JP 5064705 B2 JP5064705 B2 JP 5064705B2 JP 2006086997 A JP2006086997 A JP 2006086997A JP 2006086997 A JP2006086997 A JP 2006086997A JP 5064705 B2 JP5064705 B2 JP 5064705B2
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Description
本発明は、微細な気泡を有し、かつ耐熱性に優れる特定の熱可塑性ポリアミド樹脂製の発泡成形体部を有する発泡体基板の製造方法に関する。 The present invention relates to a method for producing a foam substrate having a foam molded body portion made of a specific thermoplastic polyamide resin having fine bubbles and excellent heat resistance.
従来の一般的なフィルム、シート等の発泡体の製造方法として、化学的発泡と物理的発泡の2種類がある。
化学的発泡は、樹脂に添加した発泡剤である化合物の熱分解により生じたガスにより気泡を形成させ、発泡体を得る方法である。しかしこの発泡方法は、発泡後に発泡剤の残渣が発泡体中に残りやすく、電子部品等の用途においては低汚染性の要求が強いため、この方法では問題が生ずる。また物理的発泡は、発泡剤である炭化水素、フルオロカーボン等の低沸点液体を樹脂に分散させた後に、加熱により発泡剤を揮発させる方法である。この方法の場合も同様に発泡剤として用いる物質の有害性による環境問題、可燃性等の問題がある。またこのような発泡方式の場合には、数十μm以上の気泡径を有する発泡体を得るのには適した方法であるが、0.01〜10μm程度の微細な気泡径を有する発泡体を得ることは困難である。
There are two types of conventional methods for producing foams such as films and sheets, chemical foaming and physical foaming.
Chemical foaming is a method of obtaining a foam by forming bubbles with a gas generated by thermal decomposition of a compound which is a foaming agent added to a resin. However, in this foaming method, a foaming agent residue tends to remain in the foam after foaming, and there is a strong demand for low contamination in applications such as electronic parts. Physical foaming is a method in which a foaming agent is volatilized by heating after a low-boiling liquid such as hydrocarbon or fluorocarbon, which is a foaming agent, is dispersed in a resin. This method also has problems such as environmental problems and flammability due to the harmfulness of substances used as foaming agents. Further, in the case of such a foaming method, it is a suitable method for obtaining a foam having a bubble diameter of several tens of μm or more, but a foam having a fine bubble diameter of about 0.01 to 10 μm is used. It is difficult to get.
一方、気泡径が小さくセル密度の高い発泡体を得る手法として、炭酸ガス等の気体を高圧にて樹脂成形体中に浸透させた後に、圧力を開放し、樹脂のガラス転移点温度付近まで加熱することにより発泡させる方法(以下、「マイクロセルラープロセス」ということがある。)が提案されている(特許文献1参照)。また、特許文献2には、マイクロセルラープロセスを用い、耐熱性に優れ、微細なセル構造を有する耐熱性ポリマー発泡体とその製造方法が記載されている。しかし特許文献2に開示されている熱可塑性樹脂のガラス転移温度が120℃以上であるので、発泡して得られる発泡体基板を電子回路用基板として適用する場合、はんだ耐熱性及びリフロー耐熱性が必ずしも十分とはいえない。一般に使用されるSn-Pbはんだの融点は183℃程度であることが知られており、Pbフリーのはんだに至っては、融点が220℃程度のものもある。
また耐熱性に優れた電子回路用基板として、熱硬化性ポリイミドを使用した回路基板が知られている。熱硬化性ポリイミドの可塑化温度は約420℃であるため、はんだ耐熱性、リフロー温度特性に優れた材料といえる。しかしながら材料の比誘電率が3.2〜3.8程度と比較的高く、一般的な電気通信用機器に使用する場合には支障が無いが、数GHzを超えるような高速通信帯域になると、伝送ロス等の問題が生じて好ましくない。また熱硬化性ポリイミドは明瞭なガラス転移点を持たないため、マイクロセルラープロセスにより、気泡径が小さくかつセル密度の高い発泡体を得ることは困難である。
On the other hand, as a method of obtaining a foam having a small cell diameter and a high cell density, a gas such as carbon dioxide gas is permeated into the resin molded body at a high pressure, then the pressure is released, and the resin is heated to near the glass transition temperature of the resin. Thus, a method of foaming (hereinafter, sometimes referred to as “microcellular process”) has been proposed (see Patent Document 1). Patent Document 2 describes a heat-resistant polymer foam having a fine cell structure and a method for producing the same, using a microcellular process. However, since the glass transition temperature of the thermoplastic resin disclosed in Patent Document 2 is 120 ° C. or higher, when a foam substrate obtained by foaming is applied as a substrate for an electronic circuit, solder heat resistance and reflow heat resistance are high. Not necessarily enough. It is known that the melting point of commonly used Sn—Pb solder is about 183 ° C., and some Pb-free solders have a melting point of about 220 ° C.
Moreover, a circuit board using thermosetting polyimide is known as an electronic circuit board having excellent heat resistance. Since the plasticizing temperature of thermosetting polyimide is about 420 ° C., it can be said that the material is excellent in solder heat resistance and reflow temperature characteristics. However, the relative dielectric constant of the material is relatively high, such as about 3.2 to 3.8, and there is no problem when used for general telecommunications equipment, but when the high-speed communication band exceeds several GHz, Problems such as transmission loss occur, which is not preferable. Further, since thermosetting polyimide does not have a clear glass transition point, it is difficult to obtain a foam having a small cell diameter and a high cell density by a microcellular process.
本発明の目的は、はんだ耐熱性に優れ、気泡径が小さく、且つ低誘電率の熱可塑性樹脂製の発泡成形体部を有する発泡体基板の製造方法を提供することにある。 An object of the present invention is excellent in solder heat resistance, bubble size is small, and is to provide a method for producing a foam board having a foamed molded part made of a low dielectric constant thermoplastic resin.
本発明者らは、上記目的を達成するため鋭意検討した結果、耐熱性樹脂であり、かつ発泡成形後のガラス転移温度が240℃以上の、特定のポリアミド樹脂からなる熱可塑性樹脂を成形して得られる成形体を非反応性ガス発泡剤と加圧下で接触、浸透させた後に圧力を減少し、その片面に導電体を該熱可塑性樹脂の軟化する温度で熱圧着させると共に、該熱可塑性樹脂成形体部分を発泡させる、熱圧着法を採用して発泡させることにより、良好な気泡径を有する、ガラス転移温度が240℃以上の発泡成形体部を有する発泡体基板が得られることを見出し、本発明を完成させた。 As a result of intensive studies to achieve the above object, the inventors of the present invention molded a thermoplastic resin made of a specific polyamide resin that is a heat-resistant resin and has a glass transition temperature of 240 ° C. or higher after foam molding. The resulting molded body is contacted and infiltrated with a non-reactive gas foaming agent under pressure, and then the pressure is reduced, and the conductor is thermocompression bonded to one surface of the thermoplastic resin at a temperature at which the thermoplastic resin is softened. It is found that a foam substrate having a foam molded body part having a favorable cell diameter and a glass transition temperature of 240 ° C. or higher can be obtained by foaming the molded body part by employing a thermocompression bonding method. The present invention has been completed.
すなわち、本発明は、下記(1)〜(3)に関する発明(以下、併せて本発明ということがある。)である。
(1)芳香族系テトラカルボン酸二無水物と芳香族系ジアミンとを反応させて得られる熱可塑性ポリイミドからなる熱可塑性樹脂成形体を非反応性ガスと加圧下で接触、浸透させた後に圧力を減少し、次いでその片面に導電体を該熱可塑性樹脂の軟化する温度で熱圧着させると共に、該熱可塑性樹脂成形体部分を発泡させる、該発泡成形体部のガラス転移温度が240℃以上である発泡体基板の製造方法。(2)前記発泡体基板中の発泡成形体部の平均気泡径が0.01〜10μmである前記(1)に記載の発泡体基板の製造方法。
(3)前記導電体が金属、金属合金、導電性樹脂、及びカーボンから選択された1種以上である、前記(1)又は(2)のいずれかに記載の発泡体基板の製造方法。
That is, the present invention is an invention related to the following (1) to ( 3 ) (hereinafter sometimes referred to as the present invention).
(1) Pressure after contacting and infiltrating a non-reactive gas with a non-reactive gas and a thermoplastic resin molded body made of a thermoplastic polyimide obtained by reacting an aromatic tetracarboxylic dianhydride and an aromatic diamine. Then, the conductor is thermocompression-bonded on one side at a temperature at which the thermoplastic resin softens, and the thermoplastic resin molded part is foamed. The glass transition temperature of the foamed molded part is 240 ° C. or higher. A method for manufacturing a foam substrate. ( 2 ) The method for producing a foam substrate according to (1), wherein an average cell diameter of the foam molded body portion in the foam substrate is 0.01 to 10 μm.
( 3 ) The method for producing a foam substrate according to (1) or (2) , wherein the conductor is one or more selected from metals, metal alloys, conductive resins, and carbon.
本発明の発泡体基板の製造方法により得られる発泡体基板は、はんだ耐熱性に優れ気泡径が小さく、且つ低誘電率であるので、高付加価値の高速通信用・高周波対応の回路基板(フレキシブル回路基板)に使用可能であり、緩衝材、断熱材としても有用である。また、該発泡体基板は、樹脂製の発泡体と導電体との間に接着層がないためハロゲンフリーで環境性能が高く、気泡径が小さいため微細なパターンが形成できる。
更に、発明の製造方法によれば、上記優れた機能を有する特定の熱可塑性ポリアミド樹脂製の発泡成形体部を有する発泡体基板を簡易にかつ効率良く製造することができ、その実用的価値は大きい。
The foam substrate obtained by the foam substrate manufacturing method of the present invention is excellent in solder heat resistance, has a small bubble diameter, and has a low dielectric constant. It can be used for a circuit board) and is also useful as a buffer material and a heat insulating material. In addition, since the foam substrate has no adhesive layer between the resin foam and the conductor, it is halogen-free and has high environmental performance, and since the bubble diameter is small, a fine pattern can be formed.
Furthermore, according to the manufacturing method of the invention, a foam substrate having a foamed molded body part made of a specific thermoplastic polyamide resin having the above-mentioned excellent function can be easily and efficiently manufactured, and its practical value is large.
以下、本発明を詳細に説明する。
(1)物性の測定法
本明細書において、各発泡体および発泡体基板の物性の測定は以下の方法によった。
(i)ガラス転移温度
DSC法により、示差走査熱量計を用いてガラス転移温度を測定した。
(ii)平均気泡径
ASTM D3576−77に準じて平均気泡径を求めた。すなわち、成形体の断面のSEM写真を撮影し、SEM写真上に水平方向と垂直方向に直線を引き、直線が横切る気泡の弦の長さtを平均した。写真の倍率をMとして、下記式に代入して平均気泡径dを求めた。
d=t/(0.616×M)
(iii)体積発泡率
水置換法により発泡体の密度(Pf)を求め、無発泡シートの密度(Po)から、以下の計算式により体積発泡率を算出した。
体積発泡率=(1−Pf/Po)×100 (%)
(iv)比誘電率
IEC 60240に準拠して比誘電率を測定した。使用した測定器は、誘電体損測定装置TR-10C(安藤電気(株)製)で、測定周波数を1kHzとした。
Hereinafter, the present invention will be described in detail.
(1) Measuring method of physical property In this specification, the physical property of each foam and foam substrate was measured by the following method.
(I) Glass transition temperature The glass transition temperature was measured by a DSC method using a differential scanning calorimeter.
(Ii) Average bubble diameter The average bubble diameter was determined according to ASTM D3576-77. That is, a SEM photograph of the cross section of the molded body was taken, straight lines were drawn in the horizontal direction and the vertical direction on the SEM photograph, and the lengths t of the bubble chords crossed by the straight line were averaged. Assuming that the magnification of the photograph is M, the average bubble diameter d was determined by substituting it into the following equation.
d = t / (0.616 × M)
(Iii) Volume foaming rate The density (Pf) of the foam was determined by the water displacement method, and the volume foaming rate was calculated from the density (Po) of the non-foamed sheet by the following formula.
Volume foaming rate = (1−Pf / Po) × 100 (%)
(Iv) Relative permittivity The relative permittivity was measured according to IEC 60240. The measuring instrument used was a dielectric loss measuring apparatus TR-10C (manufactured by Ando Electric Co., Ltd.), and the measurement frequency was 1 kHz.
(2)熱可塑性樹脂
本発明で使用する熱可塑性樹脂について以下に記載する。
本発明において使用する熱可塑性樹脂は、発泡成形後のガラス転移温度(Tg)が240℃以上となる下記に例示の熱可塑性ポリアミド樹脂(A)又は添加剤を含む熱可塑性ポリアミド樹脂組成物(B)である。
尚、溶融成形して得られる成形体を発泡させる際の発泡前後のTgは殆ど同じであるので、本発明において実質的には、溶融成形(溶融成形後の熱処理も含む)して得られる成形体のTgが240℃以上となる熱可塑性樹脂が使用可能である。
(i)熱可塑性樹脂(A)
本発明の発泡体基材の素材として用いられる熱可塑性樹脂(A)は発泡成形後のガラス転移温度が240℃以上となるもので、発泡剤として用いる非反応性ガスを加圧下で浸透し易いものが好ましい。このような熱可塑性樹脂(A)は、以下に記載の芳香族系ジアミンと芳香族系テトラカルボン酸二無水物から合成されるポリイミド、又は該ポリイミドを主成分とする組成物が例示できる。
(2) Thermoplastic resin The thermoplastic resin used in the present invention is described below.
The thermoplastic resin used in the present invention has a glass transition temperature (Tg) of the thermoplastic polyamide resin composition comprising the following to be 240 ° C. or more exemplary thermoplastic polyamide resin (A) or additives after the foam molding (B ).
In addition, since the Tg before and after foaming when foaming a molded product obtained by melt molding is almost the same, molding obtained by melt molding (including heat treatment after melt molding) is substantially used in the present invention. A thermoplastic resin having a Tg of 240 ° C. or higher can be used.
(I) Thermoplastic resin (A)
The thermoplastic resin (A) used as a raw material for the foam base material of the present invention has a glass transition temperature of 240 ° C. or higher after foam molding, and easily penetrates non-reactive gas used as a foaming agent under pressure. Those are preferred. Such thermoplastic resin (A), aromatic diamine and the polyimide synthesized from aromatic tetracarboxylic dianhydride, or a composition consisting mainly of the polyimide can be exemplified as described below.
前記芳香族系ジアミンとしては、4,4−ビス(3−アミノフェノキシ)ビフェニル(以下、APBIと記すことがある。)、1,3−ビス(3−アミノフェノキシ)ベンゼン(以下、APBEと記すことがある。)、4,4’−ジアミノジフェニルエーテル等から選ばれた少なくとも一種の芳香族系ジアミンが好ましい。
前記芳香族系テトラカルボン酸二無水物としては、ピロメリット酸二無水物(以下、PMDAと記すことがある。)、3,3’,4,4’−ジフェニルエーテルテトラカルボン酸二無水物、3,3’,4,4’−ベンゾフェノンテトラカルボン酸二無水物、3,3’,4,4’−ビフェニルテトラカルボン酸二無水物、3,3’,4,4’−ジフェニルスルホンテトラカルボン酸二無水物(以下、PSTCと記すことがある。)から選ばれる少なくとも一種の芳香族系テトラカルボン酸二無水物が好ましい。
熱可塑性樹脂(A)としては、例えば、上記した芳香族系ジアミンと芳香族系テトラカルボン酸二無水物から合成される、具体的には、APBIとPMDAとの重合物(三井化学(株)製の商品名:オーラム等)、PSTCと芳香族ジアミンとの重合物(新日本理化(株)製の商品名:リカコート(SN−20、PN−20等))等が例示できる。
Examples of the aromatic diamine include 4,4-bis (3-aminophenoxy) biphenyl (hereinafter sometimes referred to as APBI) and 1,3-bis (3-aminophenoxy) benzene (hereinafter referred to as APBE). And at least one aromatic diamine selected from 4,4′-diaminodiphenyl ether and the like.
Examples of the aromatic tetracarboxylic dianhydride include pyromellitic dianhydride (hereinafter sometimes referred to as PMDA), 3,3 ′, 4,4′-diphenyl ether tetracarboxylic dianhydride, 3 , 3 ′, 4,4′-benzophenonetetracarboxylic dianhydride, 3,3 ′, 4,4′-biphenyltetracarboxylic dianhydride, 3,3 ′, 4,4′-diphenylsulfonetetracarboxylic acid At least one aromatic tetracarboxylic dianhydride selected from dianhydrides (hereinafter sometimes referred to as PSTC) is preferred.
As the thermoplastic resin (A), for example, synthesized from the above-mentioned aromatic diamine and aromatic tetracarboxylic dianhydride, specifically, a polymer of APBI and PMDA (Mitsui Chemicals, Inc.) Product name: Aurum, etc.), and a polymer of PSTC and aromatic diamine (trade names: Rika Coat (SN-20, PN-20, etc.) manufactured by Shin Nippon Rika Co., Ltd.).
熱可塑性樹脂(A)の具体例としては、APBIとPMDAから合成されるポリイミド(以下、APBPMと記すことがある。)が挙げられる。
APBPMの合成法は、例えば、APBIとPMDAとを反応させてポリイミド前駆体(ポリアミド酸)を合成し、このポリイミド前駆体を脱水閉環することによりAPBPMを得ることができる。前記ポリイミド前駆体は、例えば、芳香族系テトラカルボン酸二無水物と芳香族系ジアミンの略等モルを、有機溶媒中、加熱下に3〜20時間程度反応させることにより得られる。ポリイミド前駆体の脱水閉環反応は、例えば、無水酢酸とピリジンの混合物などの脱水環化剤を作用させることにより行われる。
このようにして得たニートのAPBPMはガラス転移温度が245℃であるが、成形後に熱処理することにより、260℃程度まで上げることができる。
Specific examples of the thermoplastic resin (A) include polyimide synthesized from APBI and PMDA (hereinafter sometimes referred to as APBPM).
APBPM can be synthesized by, for example, reacting APBI and PMDA to synthesize a polyimide precursor (polyamide acid) and dehydrating and ring-closing the polyimide precursor. The polyimide precursor can be obtained, for example, by reacting approximately equimolar amounts of an aromatic tetracarboxylic dianhydride and an aromatic diamine in an organic solvent for about 3 to 20 hours under heating. The dehydration cyclization reaction of the polyimide precursor is performed, for example, by the action of a dehydrating cyclization agent such as a mixture of acetic anhydride and pyridine.
The neat APBPM thus obtained has a glass transition temperature of 245 ° C., but can be raised to about 260 ° C. by heat treatment after molding.
(ii)熱可塑性樹脂組成物(B)
本発明の熱可塑性樹脂として熱可塑性樹脂組成物(B)を使用する場合には、上記した熱可塑性樹脂(A)を主成分として、他の熱可塑性樹脂(C)を含む各種添加剤等を配合することが可能である。
例えば、APBPMは、結晶性ポリイミドであるが、結晶化速度が遅いために、結晶化を促進するAPBEとPMDAから得られるポリイミド等の他の熱可塑性樹脂(C)を添加剤として配合することができる。このような改質の熱可塑性樹脂(C)は、上記したポリイミドの例から適宜選択することが可能であり、その特に好ましい配合割合は、発泡成形後(又は溶融成形後)のガラス転移温度が240℃以上の熱可塑性樹脂(A)90〜100質量%、好ましくは95〜100質量%、特に好ましくは97〜100質量%と、ガラス転移温度(溶融成形前後のいずれのものも含む)が200℃以上の上記特定のジアミンと特定のテトラカルボン酸二無水物から合成される熱可塑性ポリイミド(C)0〜10質量%、好ましくは0〜5質量%、特に好ましくは0〜3質量%の熱可塑性ポリイミド混合物でも本発明の発泡体、および発泡体基材の素材として用いることができる。
(Ii) Thermoplastic resin composition (B)
When the thermoplastic resin composition (B) is used as the thermoplastic resin of the present invention, various additives including other thermoplastic resins (C) having the above-mentioned thermoplastic resin (A) as a main component, etc. It is possible to mix.
For example, APBPM is a crystalline polyimide, for crystallization speed is slow, be formulated other thermoplastic resins such as polyimide obtained from APBE and PMDA to promote crystallization of (C) as an additive it can. Such a modified thermoplastic resin ( C ) can be appropriately selected from the above-mentioned examples of polyimide, and the particularly preferred blending ratio thereof is the glass transition temperature after foam molding (or after melt molding). Thermoplastic resin (A) of 240 ° C. or higher 90 to 100% by mass, preferably 95 to 100% by mass, particularly preferably 97 to 100% by mass, and glass transition temperature (including those before and after melt molding) of 200 Thermoplastic polyimide ( C ) synthesized from the above-mentioned specific diamine and a specific tetracarboxylic dianhydride having a temperature of 0 ° C. or more, 0 to 10% by mass, preferably 0 to 5% by mass, particularly preferably 0 to 3% by mass. A plastic polyimide mixture can also be used as a material for the foam and the foam substrate of the present invention.
尚、該熱可塑性樹脂組成物(B)には、通常発泡成形に使用される各種添加剤を適宜添加することもできる。例えば、気泡核剤、滑剤、着色剤、紫外線吸収剤、酸化防止剤、結晶核剤、可塑剤、難燃材、帯電防止剤等を用いることができる。その添加量は通常の熱可塑性樹脂の成形に用いられる添加量が望ましい。 In addition, various additives usually used for foam molding can be appropriately added to the thermoplastic resin composition (B). For example, bubble nucleating agents, lubricants, colorants, ultraviolet absorbers, antioxidants, crystal nucleating agents, plasticizers, flame retardants, antistatic agents, and the like can be used. The addition amount is preferably an addition amount used for molding a normal thermoplastic resin.
(3)熱可塑性樹脂成形体
非反応性ガスを加圧下で接触、浸透させる際に使用する前記熱可塑性樹脂の成形体については、例えば熱可塑性ポリイミドの場合には従来の熱硬化性ポリイミドと異なり、キャスト法でなく押出法等にてもフィルム成形が可能あり、100μm程度の厚膜フィルムを製作する際は、コスト的に優位である。また、前記ポリイミド前駆体をフィルム、シート等に成形した後、脱水閉環させてポリイミドの成形体としてもよく、更に熱可塑性樹脂を溶融状態等で又は溶剤を使用して塗布した後に、シートやフィルム形状等にすることもできる。尚、本発明における成形体とは、特に形状は限定されるものではなく、シートやフィルム及び直方体等の他の角状成形品であってもよい。
(3) Thermoplastic resin molded body The thermoplastic resin molded body used when contacting and permeating non-reactive gas under pressure is different from, for example, a conventional thermosetting polyimide in the case of a thermoplastic polyimide. The film can be formed not only by the casting method but also by the extrusion method or the like, and is advantageous in terms of cost when producing a thick film of about 100 μm. The polyimide precursor may be formed into a film, sheet, etc., and then dehydrated and closed to form a polyimide molded body. Further, after the thermoplastic resin is applied in a molten state or using a solvent, the sheet or film It can also be shaped. In addition, the shape in particular is not limited with the molded object in this invention, Other square shaped articles, such as a sheet | seat, a film, and a rectangular parallelepiped, may be sufficient.
(4)非反応性ガス発泡剤
本発明の製造方法において、発泡剤として用いられるガスとしては、上記耐熱性を有する熱可塑性樹脂に対して非反応性であり且つ該熱可塑性樹脂に浸透可能なものであれば特に制限されることがなく、例えば、二酸化炭素、窒素ガス、空気等が挙げられる。これらのガスは、単独で使用してもよく、混合して使用してもよい。これらのうち、実用的上、熱可塑性樹脂への浸透量が多く、浸透速度も速い二酸化炭素の使用が特に好ましい。
(5)発泡成形体部
本発明の発泡体基板における発泡成形体部は、熱可塑性樹脂(A)又は熱可塑性樹脂組成物(B)に非反応性ガス発泡剤を添加して、軟化する温度付近で発泡成形することにより得られるガラス転移温度が240℃以上の発泡体である。発泡成形方法は、前記マイクロセルラープロセスを用いることが特に望ましい。ガラス転移温度が240℃以上の熱可塑性樹脂(A)又は熱可塑性樹脂組成物(B)を用いれば、ガラス転移温度が240℃以上の発泡体を容易に得ることができるが、例えばガラス転移温度が200℃程度以上の他の可塑性樹脂を使用しても、成形体を得る際の熱処理等により、その結果としてガラス転移温度が240℃以上となる物性を有していればよい。
(4) Non-reactive gas foaming agent In the production method of the present invention, the gas used as the foaming agent is non-reactive with respect to the heat-resistant thermoplastic resin and can penetrate into the thermoplastic resin. If it is a thing, there will be no restriction | limiting in particular, For example, a carbon dioxide, nitrogen gas, air etc. are mentioned. These gases may be used alone or in combination. Among these, practically, it is particularly preferable to use carbon dioxide having a large amount of penetration into the thermoplastic resin and a high penetration rate.
(5) foam molded body in the foam substrate of the foamed molded part <br/> present invention, the thermoplastic resin (A) or the thermoplastic resin composition (B) in the addition of non-reactive gas blowing agent A foam having a glass transition temperature of 240 ° C. or higher obtained by foam molding near the softening temperature. As the foam molding method, it is particularly desirable to use the microcellular process. If a thermoplastic resin (A) or a thermoplastic resin composition (B) having a glass transition temperature of 240 ° C. or higher is used, a foam having a glass transition temperature of 240 ° C. or higher can be easily obtained. However, even if another plastic resin of about 200 ° C. or higher is used, it may have a physical property that results in a glass transition temperature of 240 ° C. or higher due to heat treatment or the like when obtaining a molded body.
(6)発泡体基板
(i)発泡成形体部の平均気泡径、誘電率等
熱可塑性樹脂製の発泡成形体部は、平均気泡径が0.01〜10μmであることが好ましい。
該発泡成形体部の平均気泡径は、各発泡条件や熱可塑性樹脂成形体部の形状、厚みより平均気泡径や体積発泡率は異なるが、後述する製造方法により0.01〜10μm、好ましくは0.05〜5μm程度の範囲にある。
(6) Foam substrate (i) Average cell diameter, dielectric constant, etc. of foam molded body part The foam molded body part made of thermoplastic resin preferably has an average cell diameter of 0.01 to 10 µm. .
The average cell diameter of the foamed molded part, the foaming conditions and the thermoplastic resin molded article in the shape, the average cell diameter and volume expansion ratio than the thickness differ, 0.01 to 10 [mu] m by the manufacturing method described below, preferably It exists in the range of about 0.05-5 micrometers.
次に体積発泡率と等価比誘電率の関係は、下記の関係式(A.S.ウインデラーの式)で示されることが知られている。
(εi−εc)/(εi−εa)=(F/100)×[3εc/(2εc−εa)]
ここで εc:発泡体の比誘電率、εi:絶縁物の比誘電率、
εa:発泡の比誘電率(εa=1)、F:発泡体の容積比(%)
例えば熱可塑性樹脂、特に熱可塑性ポリイミドの比誘電率が3.0〜4.0であるとした場合、発泡により等価比誘電率を2.9以下(液晶ポリマーに相当する比誘電率)まで下げることを考慮すると、初期比誘電率が3.0の場合5%、4.0の場合22%以上の体積発泡率が必要である。なお、体積発泡率を大とすることで等価比誘電率はさらに小さくなり、低誘電率材料として知られているPTFE樹脂(比誘電率2.2)付近まで下げるためには、初期比誘電率が3.0の場合35%、4.0の場合50%以上の体積発泡率が必要となる。上記したように、シートやフィルムの厚みにより、同じ発泡条件でも体積発泡率等が異なる場合があるが、誘電率低下という点では同様の効果が得られる。
Next, it is known that the relationship between the volume expansion ratio and the equivalent relative dielectric constant is represented by the following relational expression (AS Winder's formula).
(Εi−εc) / (εi−εa) = (F / 100) × [3εc / (2εc−εa)]
Where εc is the dielectric constant of the foam, εi is the dielectric constant of the insulator,
εa: relative dielectric constant of foam (εa = 1), F: volume ratio of foam (%)
For example, if the relative permittivity of a thermoplastic resin, particularly thermoplastic polyimide, is 3.0 to 4.0, the equivalent relative permittivity is lowered to 2.9 or less (relative permittivity corresponding to a liquid crystal polymer) by foaming. Considering this, a volume expansion ratio of 5% is necessary when the initial relative dielectric constant is 3.0, and 22% or more is necessary when 4.0. Note that the equivalent relative dielectric constant is further reduced by increasing the volume foaming rate, and in order to reduce it to the vicinity of PTFE resin (relative dielectric constant 2.2) known as a low dielectric constant material, the initial relative dielectric constant is required. When 3.0 is 3.0, a volume expansion ratio of 35% or more and 50% or more is required. As described above, the volume foaming rate may differ even under the same foaming conditions depending on the thickness of the sheet or film, but the same effect can be obtained in terms of lowering the dielectric constant.
上記から、使用目的を考慮して、比誘電率を2.9以下とするために体積発泡率は好ましくは5〜50%、より好ましくは50〜90%である。
尚、比誘電率を2.9以下とすることが望ましいが、通常その下限界は発泡体の強度等の兼ね合いから1.2程度である。
後述する方法により得られる発泡成形体部は、耐熱性に優れ、均一で微細な気泡を有し、誘電率と相対密度も低い。従って、その耐熱性、機械的性質、耐摩耗性等の優れた性質により、例えば、電子機器等の回路基板などとして好適に使用できる。
From the above, considering the purpose of use, the volume foaming ratio is preferably 5 to 50%, more preferably 50 to 90% in order to make the dielectric constant 2.9 or less.
Although the relative dielectric constant is preferably 2.9 or less, the lower limit is usually about 1.2 in view of the strength of the foam.
The foamed molded part obtained by the method described later has excellent heat resistance, uniform and fine bubbles, and a low dielectric constant and relative density. Accordingly, it can be suitably used as, for example, a circuit board of an electronic device or the like due to its excellent properties such as heat resistance, mechanical properties, and wear resistance.
(ii)発泡体基板
発泡体基板には、後述する方法により該発泡成形体部の1つの面に導電体を積層する必要がある。このような導電体としては、金属、金属合金、導電性樹脂、及びカーボンから選択された1種以上が例示できる。前記金属と金属合金としては、金、銀、白金、ルテニウム、ニッケルあるいはこれらの合金が例示できるが、銅がもっとも好ましい。
本発明の発泡体基板を製造する方法は高圧容器中で炭酸ガス等を加圧下に浸透させたシート、フィルム等の成形体を、圧力開放させた後に熱プレス機で導電体と熱圧着させる際に同時に発泡させる方法である。
(iii)フレキシブルプリント回路基板
発泡体基板は、はんだ耐熱性に優れ気泡径が小さく、且つ低誘電率であるので、高付加価値の高速通信用・高周波対応のフレキシブルプリント回路基板に使用可能である。
The (ii) the foam board foam board, it is necessary to laminate the conductor on one surface of the foamed molded part by the method described below. Examples of such a conductor include one or more selected from metals, metal alloys, conductive resins, and carbon. Examples of the metal and metal alloy include gold, silver, platinum, ruthenium, nickel, and alloys thereof, but copper is most preferable.
The method for producing a foam substrate according to the present invention is a method in which a molded body such as a sheet or a film in which carbon dioxide gas or the like is infiltrated under pressure in a high-pressure vessel is pressure- released and then thermocompression-bonded with a conductor using a hot press machine. It is the method of making it foam simultaneously.
( Iii ) Flexible printed circuit board Foamed substrate is excellent in solder heat resistance, has a small bubble diameter, and has a low dielectric constant. Therefore, it can be used for a flexible printed circuit board for high-value-added high-speed communication and high frequency. .
(iv)物理的発泡剤、発泡温度等
発泡体基板の製造方法においては、発泡成形後のガラス転移温度が240℃以上となる熱可塑性樹脂を成形して得た、成形体を非反応性ガスと加圧下で接触、浸透させ(ガス浸透工程)、その後に圧力を減少し(圧力減少工程)、次いで後述する熱圧着法を採用して加熱・軟化により発泡させる(加熱発泡工程)。
発泡に使用する物理的発泡剤は、適宜選択できるが、例えば二酸化炭素を用いる場合には、浸透させる際の圧力は数MPa〜100MPa、好ましくは5MPa以上である、また発泡剤ガスの臨界圧以下の条件を選択することが好ましい。ガス浸透工程における温度は、用いるガスの種類や熱可塑性樹脂のガラス転移温度等によってその好ましい条件は異なる。またガス浸透時間についても、用いるガスの種類や高圧容器の容積、浸透時の温度、熱可塑性樹脂フィルムの厚みや形状により異なる。例えば厚みが数十〜100μmの熱可塑性ポリイミドフィルムに炭酸ガスを浸透させる場合は、温度や圧力条件等にもよるが浸透時間は数十分〜数時間程度である。
(Iv) a physical blowing agent, in the method for manufacturing a foaming temperature such <br/> foam substrate, the glass transition temperature after foaming molding obtained by molding the thermoplastic resin to be 240 ° C. or higher, the green body Contact and permeate under pressure with non-reactive gas (gas permeation process), then reduce the pressure (pressure reduction process), and then foam by heating and softening using the thermocompression bonding method described later (heating foaming process) ).
The physical foaming agent used for foaming can be selected as appropriate. For example, when carbon dioxide is used, the pressure at the time of permeation is several MPa to 100 MPa, preferably 5 MPa or more, and below the critical pressure of the foaming agent gas. It is preferable to select these conditions. The preferable conditions for the temperature in the gas infiltration step vary depending on the type of gas used, the glass transition temperature of the thermoplastic resin, and the like. The gas permeation time also varies depending on the type of gas used, the volume of the high-pressure vessel, the temperature during permeation, and the thickness and shape of the thermoplastic resin film. For example, when carbon dioxide gas permeates a thermoplastic polyimide film having a thickness of several tens to 100 μm, the permeation time is about several tens of minutes to several hours depending on temperature and pressure conditions.
発泡方法としては、前記マイクロセルラープロセスを使用できる。すなわちこの製法は、シート状、フィルム状等の成形体に対して、高圧容器中にて炭酸ガスなどの発泡剤を熱可塑性樹脂に加圧浸透させる。その後、高圧容器中のガスを急激に放出させて熱可塑性樹脂中に浸透したガスを過飽和状態にすることにより、ガスを少しだけ成長させる。これが気泡の核になり、この状態の熱可塑性樹脂シート、フィルム等をその材料の軟化する温度まで加熱することによって気泡の核を成長させ樹脂発泡体を得るものであり、本方法によれば、平均発泡径が0.01〜10μmの均一で微細な発泡成形体を得ることが可能である。 The microcellular process can be used as the foaming method. That is, in this production method, a foaming agent such as carbon dioxide gas is pressed and infiltrated into a thermoplastic resin in a high-pressure container with respect to a molded body such as a sheet or film. Thereafter, the gas in the high-pressure vessel is suddenly released to bring the gas that has penetrated into the thermoplastic resin into a supersaturated state, so that the gas is slightly grown. This becomes the core of the bubble, and by heating the thermoplastic resin sheet, film, etc. in this state to the temperature at which the material softens, the core of the bubble is grown to obtain a resin foam. It is possible to obtain a uniform and fine foam molded article having an average foam diameter of 0.01 to 10 μm.
また、本発明の方法の好ましい態様では、熱可塑性樹脂が軟らかくなりすぎて気泡が過度に成長し、ガス抜け、気泡が合一して気泡の存在密度の低下、及び気泡成長過程で熱可塑性樹脂が変形することを防止するために、例えば軟化する温度を、1×107Pa〜1×1011Pa程度(熱可塑性樹脂の未発泡状態で測定した弾性率)となる温度に設定するのが望ましい。これらの工程は、バッチ方式、又は連続方式で行うことができる。 Further, in a preferred embodiment of the method of the present invention, the thermoplastic resin becomes too soft and bubbles grow excessively, outgassing, the bubbles coalesce and the density of bubbles is reduced, and the thermoplastic resin in the bubble growth process In order to prevent deformation, for example, the softening temperature is set to a temperature that is about 1 × 10 7 Pa to 1 × 10 11 Pa (elastic modulus measured in an unfoamed state of the thermoplastic resin). desirable. These steps can be performed in a batch mode or a continuous mode.
このようにして得られた発泡体基板は、耐熱性に優れる上、均一で微細な気泡を有し、相対密度も低い。例えば、該発泡成形体部の平均気泡径は、0.01〜10μm、好ましくは0.01〜1μm程度の範囲にある。 The foam substrate thus obtained is excellent in heat resistance, has uniform and fine bubbles, and has a low relative density. For example, the average cell diameter of the foamed molded part is in the range of about 0.01 to 10 μm, preferably about 0.01 to 1 μm.
(v)発泡体基板の製造方法
本発明の発泡体基板の製造方法として、熱圧着法を利用する。本方法の製造方法は、従来法の一つである金属体と樹脂シートを熱硬化性接着剤で張り合わせる方法と異なり、接着剤を使用せずに熱可塑性樹脂成形体に導電体を直接積層させる方法のため、低コストかつハロゲンフリーな方法といえる。
本発明の熱圧着法は、高圧容器中で炭酸ガス等を前記加圧下に浸透させたシート、フィルム等の成形体を、圧力開放させた後に熱プレス機で導電体と熱圧着させる際に同時に発泡させる方法である。
( V ) Method for Producing Foam Substrate As a method for producing the foam substrate of the present invention, a thermocompression bonding method is used. The manufacturing method of this method is different from the conventional method in which a metal body and a resin sheet are laminated with a thermosetting adhesive, and a conductor is directly laminated on a thermoplastic resin molded body without using an adhesive. Therefore, it can be said to be a low-cost and halogen-free method.
Thermocompression bonding of the present invention, a sheet impregnated with carbon dioxide gas in the pressure in the high pressure vessel, a molded body such as a film, at the same time to conductor thermocompression bonding by hot press machine After pressure release This is a foaming method .
本発明の発泡体基板の製造方法は、発泡成形後のガラス転移温度が240℃以上となる熱可塑性樹脂を成形して得られる成形体を非反応性ガスと加圧下で接触、浸透させた後に圧力を減少し、次いでその片面に導電体を該熱可塑性樹脂の軟化する温度で熱圧着させると共に、該成形体部分を発泡させて、ガラス転移温度が240℃以上の発泡体部分を有する発泡体基板を得ることを特徴とする。
本発明の製造方法を以下に例示するが、本発明の製造方法はこれに限定されるものではない。
本発明では、発泡成形後のガラス転移温度が240℃以上となる熱可塑性樹脂の成形体に非反応性ガスを加圧下で接触、浸透させた後に圧力を減少して、非反応性ガスを浸透させた成形体を得る。
次に非反応性ガスを浸透させた成形体と導電体をプレス機等にセットして、使用した熱可塑性樹脂の軟化する温度近くに加熱しながら、ローラ等により加圧することにより、成形体部を発泡させると共に導電体を熱圧着させる。
In the method for producing a foam substrate of the present invention, a molded product obtained by molding a thermoplastic resin having a glass transition temperature of 240 ° C. or higher after foam molding is brought into contact with and infiltrated with a non-reactive gas under pressure. A foam having a foam part having a glass transition temperature of 240 ° C. or more by reducing pressure and then thermocompression bonding the conductor on one side at a temperature at which the thermoplastic resin softens and foaming the molded part A substrate is obtained.
Although the manufacturing method of this invention is illustrated below, the manufacturing method of this invention is not limited to this.
In the present invention , a non-reactive gas is brought into contact with and infiltrated under pressure into a thermoplastic resin molded article having a glass transition temperature of 240 ° C. or higher after foam molding, and then the pressure is reduced to infiltrate the non-reactive gas. A molded body is obtained.
Next, the molded body and conductor are infiltrated with non-reactive gas, and set in a press machine, etc., and heated by a roller or the like while being heated near the temperature at which the used thermoplastic resin is softened. And the conductor is thermocompression bonded.
以下に、実施例、参考例を用いて本発明をさらに詳しく説明するが、本発明はこれによって限定されるものではない。
尚、本実施例、参考例で使用した熱可塑性ポリイミドは、ピロメリット酸二無水物(PMDA)と4,4−ビス(3−アミノフェノキシ)ビフェニル(APBI)から合成された熱可塑性ポリイミド(APBPM)(商品名:「オーラム(PI−PA)」、三井化学(株)製)である。
[参考例1]
前記熱可塑性ポリイミド(APBPM)を押出成形法(Tダイ法)により成形して得た厚み50μmのフィルム(ガラス転移温度:258℃)を加圧容器中に設置し、そこに6.0MPaの炭酸ガスを導入し、30分間放置して炭酸ガスを浸透させた。次に炭酸ガスを浸透したフィルムを樹脂軟化する温度(約240〜300℃)に設定した空気式循環恒温槽内にて数十秒間保持し、発泡させることにより、平均気泡径500nm程度、体積発泡率20%の発泡熱可塑性ポリイミドフィルムを作製した。
得られた発泡熱可塑性ポリイミドフィルムのガラス転移温度は、258℃であり、その誘電率を測定した結果、比誘電率は発泡前の3.1に対し、発泡後は2.6にまで低下した。
Hereinafter, the present invention will be described in more detail with reference to Examples and Reference Examples , but the present invention is not limited thereto.
The thermoplastic polyimide used in the examples and reference examples is a thermoplastic polyimide (APBPM) synthesized from pyromellitic dianhydride (PMDA) and 4,4-bis (3-aminophenoxy) biphenyl (APBI). (Trade name: “Aurum (PI-PA)”, manufactured by Mitsui Chemicals, Inc.).
[ Reference Example 1]
A film (glass transition temperature: 258 ° C.) having a thickness of 50 μm obtained by molding the thermoplastic polyimide (APBPM) by an extrusion molding method (T-die method) is placed in a pressure vessel, and 6.0 MPa of carbonic acid therein. Gas was introduced and allowed to stand for 30 minutes to infiltrate carbon dioxide. Next, the film is infiltrated with carbon dioxide gas and held in a pneumatic circulation thermostat set at a temperature for softening the resin (about 240 to 300 ° C.) for several tens of seconds. A 20% foamed thermoplastic polyimide film was produced.
The obtained thermoplastic thermoplastic polyimide film had a glass transition temperature of 258 ° C., and the dielectric constant was measured. As a result, the relative dielectric constant decreased to 3.1 after foaming and to 2.6 after foaming. .
[比較例1]
厚さ50μmの熱硬化性ポリイミド(商品名:カプトン、東レ・デュポン(株)製)シートを用い、参考例1に記載したと同様の操作を行って発泡体の製造を行った。尚、発泡温度は400℃である。しかしながら、良好な発泡成形体は得られなかった。発泡前後の該熱硬化性ポリイミドの誘電率測定値にも顕著な差は観察できなかった。
[Comparative Example 1]
Using a thermosetting polyimide (trade name: Kapton, manufactured by Toray DuPont Co., Ltd.) sheet having a thickness of 50 μm, the same operation as described in Reference Example 1 was performed to produce a foam. The foaming temperature is 400 ° C. However, a good foamed molded product was not obtained. No significant difference was observed in the measured dielectric constant of the thermosetting polyimide before and after foaming.
[参考例2]
前記熱可塑性ポリイミド(APBPM)を押出成形法により成形して得た厚み50μmのフィルム(ガラス転移温度:258℃)を加圧容器中に設置し、そこに6.0MPaの炭酸ガスを導入して、30時間放置することにより、炭酸ガスを浸透させた。
次に炭酸ガスを浸透したフィルムを該樹脂が樹脂軟化する温度(240〜300℃)に設定した空気式循環恒温槽内にて数分間保持し、発泡させることにより、平均気泡径500nm程度、体積発泡率30%の発泡熱可塑性ポリイミドフィルムを作製した。
次に該発泡体と厚み10μmの銅箔を熱プレス機にセットし、加圧・加温させることで樹脂と金属箔の複合体(発泡樹脂基板)を作製した。
該発泡樹脂基板中の発泡体部分のガラス転移温度は、258℃であった。
[ Reference Example 2]
A film (glass transition temperature: 258 ° C.) having a thickness of 50 μm obtained by molding the thermoplastic polyimide (APBPM) by an extrusion molding method was placed in a pressure vessel, and 6.0 MPa of carbon dioxide gas was introduced therein. The carbon dioxide gas was infiltrated by leaving it for 30 hours.
Next, the film infiltrated with carbon dioxide gas is held for several minutes in a pneumatic circulating thermostat set to a temperature at which the resin softens the resin (240 to 300 ° C.) and foamed to obtain an average bubble diameter of about 500 nm and volume. A foamed thermoplastic polyimide film having a foaming rate of 30% was produced.
Next, the foam and a copper foil having a thickness of 10 μm were set in a hot press machine, and a composite of resin and metal foil (foamed resin substrate) was produced by applying pressure and heating.
The glass transition temperature of the foam part in the foamed resin substrate was 258 ° C.
[実施例1]
前記熱可塑性ポリイミド(APBPM)を押出成形法により成形して得た厚み50μmのフィルム(ガラス転移温度:258℃)を加圧容器中に設置し、そこに6.0MPaの炭酸ガスを導入し、30分間放置することにより、炭酸ガスを浸透させ、その後圧力を減少させた。次に該フィルムと厚み10μmの銅箔を熱プレス機にセットし、加圧(4.9MPa)・加温(300℃)させることで樹脂と金属箔の複合体を形成した。
該複合体を形成させる際の加熱により樹脂内部の炭酸ガスが発泡し、平均気泡径500nm程度、体積発泡率10%の発泡体基板が形成された。
該発泡樹脂基板中の発泡体部分のガラス転移温度は、258℃であった。
[Example 1 ]
A 50 μm-thick film (glass transition temperature: 258 ° C.) obtained by molding the thermoplastic polyimide (APBPM) by an extrusion molding method was placed in a pressure vessel, and 6.0 MPa carbon dioxide gas was introduced therein, By allowing to stand for 30 minutes, carbon dioxide gas was infiltrated, and then the pressure was reduced. Next, the film and a copper foil having a thickness of 10 μm were set in a hot press machine, and a composite of resin and metal foil was formed by applying pressure (4.9 MPa) and heating (300 ° C.).
The carbon dioxide gas inside the resin was foamed by heating when forming the composite, and a foam substrate having an average cell diameter of about 500 nm and a volume foaming rate of 10% was formed.
The glass transition temperature of the foam part in the foamed resin substrate was 258 ° C.
[参考例3]
前記熱可塑性ポリイミド(APBPM)を押出成形法により成形して得た厚み50μmのフィルム(ガラス転移温度:258℃)と厚み10μmの銅箔を熱プレス機にセットし、加圧・加温させることで樹脂と金属箔の複合体を形成した。その後、該複合材を加圧容器中に設置し、そこに6.0MPaの炭酸ガスを導入し、30分間放置することにより、炭酸ガスを浸透させた。次に炭酸ガス浸透フィルムを該樹脂が軟化する温度(240〜300℃)に設定した空気式循環恒温槽内に数分間保持し、発泡させることにより、平均気泡径300nm程度、体積発泡率20%の発泡樹脂基板を作製した。
該発泡樹脂基板中の発泡体部分のガラス転移温度は、258℃であった。
[ Reference Example 3 ]
A film having a thickness of 50 μm (glass transition temperature: 258 ° C.) obtained by molding the thermoplastic polyimide (APBPM) by an extrusion molding method and a copper foil having a thickness of 10 μm are set in a hot press machine and pressed and heated. Thus, a composite of resin and metal foil was formed. Thereafter, the composite material was placed in a pressurized container, and 6.0 MPa of carbon dioxide gas was introduced therein and allowed to stand for 30 minutes, whereby carbon dioxide gas was permeated. Then the carbon dioxide gas and penetration film was held for several minutes on the set pneumatic circulation constant temperature bath at a temperature (240 to 300 ° C.) to the resin is softened, by foaming, average cell diameter 300nm approximately, the volume expansion ratio 20 % Foamed resin substrate.
The glass transition temperature of the foam part in the foamed resin substrate was 258 ° C.
[参考例4]
前記熱可塑性ポリイミド(APBPM)を押出成形法により成形して得た厚み50μmのフィルム(ガラス転移温度:258℃)を加圧容器中に設置し、そこに6.0MPaの炭酸ガスを導入し、30分間放置することにより、炭酸ガスを浸透させた。
次に炭酸ガス浸透フィルムを該樹脂が軟化する温度(240〜300℃)に設定した空気式循環恒温槽内にて数十秒間保持し、発泡させることにより、平均気泡径500nm程度、体積発泡率20%の発泡熱可塑性ポリイミドフィルムを作製した。該発泡樹脂フィルムを、無電解ニッケルめっきにて厚み0.1μmの成膜を行った後、電解めっきにて銅を5μmの厚みに積層させた。その結果、発泡体両面に導電層を設けた発泡樹脂基板を得ることができた。
該発泡樹脂基板中の発泡体部分のガラス転移温度は、258℃であった。
更に、本発泡樹脂基板を240℃に設定した空気循環式恒温槽中に1分間放置し、樹脂と金属体の界面に膨れが生じないか確認したが、外観上の問題は観察されなかった。
[ Reference Example 4 ]
A 50 μm-thick film (glass transition temperature: 258 ° C.) obtained by molding the thermoplastic polyimide (APBPM) by an extrusion molding method was placed in a pressure vessel, and 6.0 MPa carbon dioxide gas was introduced therein, Carbon dioxide gas was infiltrated by leaving it for 30 minutes.
Then the carbon dioxide gas and penetration film several tens of seconds holding at the set pneumatic circulation thermostat to a temperature (240 to 300 ° C.) to the resin is softened, by foaming, average cell diameter 500nm approximately, volume expansion A 20% foamed thermoplastic polyimide film was produced. After depositing the foamed resin film to a thickness of 0.1 μm by electroless nickel plating, copper was laminated to a thickness of 5 μm by electrolytic plating. As a result, it was possible to obtain a foamed resin substrate having conductive layers on both surfaces of the foam.
The glass transition temperature of the foam part in the foamed resin substrate was 258 ° C.
Furthermore, this foamed resin substrate was left in an air circulation thermostat set at 240 ° C. for 1 minute to confirm whether swelling occurred at the interface between the resin and the metal body, but no problem in appearance was observed.
[参考例5]
前記熱可塑性ポリイミド(APBPM)を押出成形法により成形して得た厚み100μmのフィルム(ガラス転移温度:258℃)を加圧容器中に設置し、そこに6.0MPaの炭酸ガスを導入し、30分間放置することにより、炭酸ガスを浸透させた。
次に炭酸ガス浸透フィルムを該樹脂が軟化する温度(240〜300℃)に設定した空気式循環恒温槽内にて数十秒間保持し、発泡させることにより、平均気泡径500nm程度、体積発泡率45%の発泡熱可塑性ポリイミドフィルムを作製した。該発泡樹脂フィルムを、無電解ニッケルめっきにて厚み0.1μmの成膜を行った後、電解めっきにて銅を5μmの厚みに積層させた。その結果、発泡体両面に導電層を設けた可撓性を有する発泡樹脂基板(銅張積層板)を得ることができた。
該銅張積層板を使用し、銅表面をエッチング加工により回路パターン形成させた後に、導体保護を行うためカバーレイフィルムを積層した両面フレキシブルプリント回路基板を作製した。次に基板表面にPbフリー半田バンプを形成し、抵抗等の電子部品を表面実装させてリフロー半田付けを行った。この時の温度プロファイルは245℃(10秒未満)である。リフロー後に半田付け部の接合不備及び基材の膨れ等の確認を行ったが、外観上の問題は観察されなかった。
[ Reference Example 5 ]
A 100 μm-thick film (glass transition temperature: 258 ° C.) obtained by molding the thermoplastic polyimide (APBPM) by an extrusion molding method was placed in a pressure vessel, and 6.0 MPa carbon dioxide gas was introduced therein, Carbon dioxide gas was infiltrated by leaving it for 30 minutes.
Then the carbon dioxide gas and penetration film several tens of seconds holding at the set pneumatic circulation thermostat to a temperature (240 to 300 ° C.) to the resin is softened, by foaming, average cell diameter 500nm approximately, volume expansion A foamed thermoplastic polyimide film having a rate of 45% was produced. After depositing the foamed resin film to a thickness of 0.1 μm by electroless nickel plating, copper was laminated to a thickness of 5 μm by electrolytic plating. As a result, a flexible foamed resin substrate (copper-clad laminate) having conductive layers provided on both surfaces of the foam could be obtained.
The copper-clad laminate was used to form a circuit pattern on the copper surface by etching, and then a double-sided flexible printed circuit board on which a coverlay film was laminated for conductor protection was produced. Next, Pb-free solder bumps were formed on the substrate surface, and electronic components such as resistors were mounted on the surface to perform reflow soldering. The temperature profile at this time is 245 ° C. (less than 10 seconds). After reflowing, it was confirmed that the soldering part was not properly joined and the base material was swollen. However, no appearance problems were observed.
[参考例6]
参考例5で作製した発泡熱可塑性ポリイミドフィルムにおいて、容積法によりGHz帯域の比誘電率測定を実施した。使用した測定器はヒューレットパッカード製のインピーダンスアナライザ(HP4291B)である。この結果、1GHzの測定周波数において、発泡前の比誘電率3.1に対し発泡後のフィルムは2.1であった。次に発泡前、発泡後の2つのフィルムを参考例5と同様な製法で両面導電層を積層させ、エッチング加工により回路長100mmのテストプリントパターンを設けたフレキシブルプリント基板を作成した。TDR(時間領域反射)測定法より電気信号の伝播時間を測定した結果、未発泡基板では伝播時間が約1.2ns程度要していたが、発泡基板では1ns以下と、約20%程度改善される効果を得た。
[ Reference Example 6 ]
In foamed thermoplastic polyimide films made created in Reference Example 5 were carried out relative dielectric constant measured in GHz band by volumetric method. The measuring instrument used is an impedance analyzer (HP4291B) manufactured by Hewlett-Packard. As a result, at the measurement frequency of 1 GHz, the film after foaming was 2.1 with respect to the relative dielectric constant 3.1 before foaming. Next, a double-sided conductive layer was laminated on the two films before foaming and after foaming in the same manner as in Reference Example 5, and a flexible printed board provided with a test print pattern with a circuit length of 100 mm was produced by etching. As a result of measuring the propagation time of the electrical signal by the TDR (time domain reflection) measurement method, the propagation time was about 1.2 ns for the non-foamed substrate, but about 20% was improved to 1 ns or less for the foamed substrate. The effect was obtained.
本発明の特定の熱可塑性ポリアミド樹脂製の発泡成形体部を有する発泡体基板は、はんだ耐熱性に優れ気泡径が小さく、且つ低誘電率であるので、高付加価値の高速通信用・高周波対応の回路基板(フレキシブル回路基板、プリント配線基板)に使用可能である。また本発明の発泡体基板は、回路用基板のみならず、絶縁体、断熱体、緩衝材等にも応用が可能である。 The foam substrate having a foamed molded body portion made of the specific thermoplastic polyamide resin of the present invention has excellent heat resistance of solder and a small bubble diameter and a low dielectric constant. It can be used for a circuit board (flexible circuit board, printed wiring board). The foam substrate of the present invention can be applied not only to a circuit board but also to an insulator, a heat insulator, a buffer material, and the like.
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