JP2009221397A - Polyimide precursor solution composition, and polyimide film - Google Patents
Polyimide precursor solution composition, and polyimide film Download PDFInfo
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- JP2009221397A JP2009221397A JP2008069188A JP2008069188A JP2009221397A JP 2009221397 A JP2009221397 A JP 2009221397A JP 2008069188 A JP2008069188 A JP 2008069188A JP 2008069188 A JP2008069188 A JP 2008069188A JP 2009221397 A JP2009221397 A JP 2009221397A
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- 229920001721 polyimide Polymers 0.000 title claims abstract description 153
- 239000000203 mixture Substances 0.000 title claims abstract description 113
- 239000004642 Polyimide Substances 0.000 title claims abstract description 66
- 239000002243 precursor Substances 0.000 title claims abstract description 53
- 238000010438 heat treatment Methods 0.000 claims abstract description 42
- 239000000758 substrate Substances 0.000 claims abstract description 25
- 239000007787 solid Substances 0.000 claims description 17
- 239000000463 material Substances 0.000 claims description 12
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 238000001175 rotational moulding Methods 0.000 claims description 4
- 229920005575 poly(amic acid) Polymers 0.000 abstract description 57
- 239000002253 acid Substances 0.000 abstract description 40
- 238000000576 coating method Methods 0.000 abstract description 18
- 239000011248 coating agent Substances 0.000 abstract description 16
- HLBLWEWZXPIGSM-UHFFFAOYSA-N 4-Aminophenyl ether Chemical compound C1=CC(N)=CC=C1OC1=CC=C(N)C=C1 HLBLWEWZXPIGSM-UHFFFAOYSA-N 0.000 abstract description 12
- WKDNYTOXBCRNPV-UHFFFAOYSA-N bpda Chemical compound C1=C2C(=O)OC(=O)C2=CC(C=2C=C3C(=O)OC(C3=CC=2)=O)=C1 WKDNYTOXBCRNPV-UHFFFAOYSA-N 0.000 abstract description 10
- 238000003860 storage Methods 0.000 abstract description 8
- 239000000126 substance Substances 0.000 abstract description 5
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- 238000006243 chemical reaction Methods 0.000 description 35
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- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 20
- 229910001873 dinitrogen Inorganic materials 0.000 description 20
- 150000004985 diamines Chemical class 0.000 description 19
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- 238000000034 method Methods 0.000 description 14
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- GTDPSWPPOUPBNX-UHFFFAOYSA-N ac1mqpva Chemical compound CC12C(=O)OC(=O)C1(C)C1(C)C2(C)C(=O)OC1=O GTDPSWPPOUPBNX-UHFFFAOYSA-N 0.000 description 4
- 239000012528 membrane Substances 0.000 description 4
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- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- 125000003118 aryl group Chemical group 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000001879 gelation Methods 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- LFBALUPVVFCEPA-UHFFFAOYSA-N 4-(3,4-dicarboxyphenyl)phthalic acid Chemical class C1=C(C(O)=O)C(C(=O)O)=CC=C1C1=CC=C(C(O)=O)C(C(O)=O)=C1 LFBALUPVVFCEPA-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 2
- -1 aromatic tetracarboxylic acid Chemical class 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 125000005462 imide group Chemical group 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000005191 phase separation Methods 0.000 description 2
- 239000002798 polar solvent Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- HHVIBTZHLRERCL-UHFFFAOYSA-N sulfonyldimethane Chemical compound CS(C)(=O)=O HHVIBTZHLRERCL-UHFFFAOYSA-N 0.000 description 2
- YFNKIDBQEZZDLK-UHFFFAOYSA-N triglyme Chemical compound COCCOCCOCCOC YFNKIDBQEZZDLK-UHFFFAOYSA-N 0.000 description 2
- AVQQQNCBBIEMEU-UHFFFAOYSA-N 1,1,3,3-tetramethylurea Chemical compound CN(C)C(=O)N(C)C AVQQQNCBBIEMEU-UHFFFAOYSA-N 0.000 description 1
- CYSGHNMQYZDMIA-UHFFFAOYSA-N 1,3-Dimethyl-2-imidazolidinon Chemical compound CN1CCN(C)C1=O CYSGHNMQYZDMIA-UHFFFAOYSA-N 0.000 description 1
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- MBDUIEKYVPVZJH-UHFFFAOYSA-N 1-ethylsulfonylethane Chemical compound CCS(=O)(=O)CC MBDUIEKYVPVZJH-UHFFFAOYSA-N 0.000 description 1
- YWKSINPSASCIMZ-UHFFFAOYSA-N 4,5-dimethyl-4,5-dihydro-1h-imidazole Chemical compound CC1NC=NC1C YWKSINPSASCIMZ-UHFFFAOYSA-N 0.000 description 1
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
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- 241000721047 Danaus plexippus Species 0.000 description 1
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 1
- SUAKHGWARZSWIH-UHFFFAOYSA-N N,N‐diethylformamide Chemical compound CCN(CC)C=O SUAKHGWARZSWIH-UHFFFAOYSA-N 0.000 description 1
- ZWXPDGCFMMFNRW-UHFFFAOYSA-N N-methylcaprolactam Chemical compound CN1CCCCCC1=O ZWXPDGCFMMFNRW-UHFFFAOYSA-N 0.000 description 1
- AZWHFTKIBIQKCA-UHFFFAOYSA-N [Sn+2]=O.[O-2].[In+3] Chemical compound [Sn+2]=O.[O-2].[In+3] AZWHFTKIBIQKCA-UHFFFAOYSA-N 0.000 description 1
- 239000006230 acetylene black Substances 0.000 description 1
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- 239000000654 additive Substances 0.000 description 1
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- 239000000956 alloy Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 150000008064 anhydrides Chemical class 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- 150000004984 aromatic diamines Chemical class 0.000 description 1
- 238000007611 bar coating method Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 1
- 239000006231 channel black Substances 0.000 description 1
- 239000007809 chemical reaction catalyst Substances 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
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- 238000006297 dehydration reaction Methods 0.000 description 1
- CCAFPWNGIUBUSD-UHFFFAOYSA-N diethyl sulfoxide Chemical compound CCS(=O)CC CCAFPWNGIUBUSD-UHFFFAOYSA-N 0.000 description 1
- NJLLQSBAHIKGKF-UHFFFAOYSA-N dipotassium dioxido(oxo)titanium Chemical compound [K+].[K+].[O-][Ti]([O-])=O NJLLQSBAHIKGKF-UHFFFAOYSA-N 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
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- 239000000945 filler Substances 0.000 description 1
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- 229910002804 graphite Inorganic materials 0.000 description 1
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- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
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- 150000004706 metal oxides Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- AJFDBNQQDYLMJN-UHFFFAOYSA-N n,n-diethylacetamide Chemical compound CCN(CC)C(C)=O AJFDBNQQDYLMJN-UHFFFAOYSA-N 0.000 description 1
- 239000012766 organic filler Substances 0.000 description 1
- WMHSAFDEIXKKMV-UHFFFAOYSA-N oxoantimony;oxotin Chemical compound [Sn]=O.[Sb]=O WMHSAFDEIXKKMV-UHFFFAOYSA-N 0.000 description 1
- 125000004430 oxygen atom Chemical group O* 0.000 description 1
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- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- 125000004151 quinonyl group Chemical group 0.000 description 1
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- ZUHZGEOKBKGPSW-UHFFFAOYSA-N tetraglyme Chemical compound COCCOCCOCCOCCOC ZUHZGEOKBKGPSW-UHFFFAOYSA-N 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical compound O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 description 1
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Abstract
Description
本発明は、ポリイミド前駆体溶液組成物に関する。本発明は、特定の化学構造からなるポリイミド前駆体溶液組成物であって、優れた機械的特性を有するポリイミド膜を安定して容易に得ることができる。また、このポリイミド前駆体は、高濃度且つ低粘度の溶液組成物としたときでも、優れた機械的特性を有するポリイミド膜を安定して容易に得ることができる。 The present invention relates to a polyimide precursor solution composition. The present invention is a polyimide precursor solution composition having a specific chemical structure, and can stably and easily obtain a polyimide film having excellent mechanical properties. Moreover, even when this polyimide precursor is used as a high-concentration and low-viscosity solution composition, a polyimide film having excellent mechanical properties can be obtained stably and easily.
ポリイミド膜は、優れた耐熱性や機械的特性を有しており、フィルム形状に加工されたものはフレキシブル絶縁基板や耐熱性テープ基材として、また管状形状に加工されたものは加熱物品の搬送用ベルト、電子写真方式の定着ベルト或いは中間転写ベルトなどとして好適に用いられている。通常、このようなポリイミド膜はポリイミド前駆体である高分子量（数平均分子量が１００００〜３００００程度）のポリアミック酸溶液組成物を用いて製造される。中間転写ベルトを好適に製造することができるポリアミック酸溶液組成物としては、特許文献１に記載されている３，３’，４，４’−ビフェニルテトラカルボン酸二無水物と４，４’−ジアミノジフェニルエーテルとをほぼ等モル反応させて得られたポリアミック酸溶液組成物がある。
しかし、前記ポリアミック酸溶液組成物は、保存時に徐々に部分的なゲル化が起こることがあり、ゲル化が極微量であっても最終物であるポリイミド膜の物性に悪影響を与えるので、例えば導電性カーボンブラックを混合したポリアミック酸溶液組成物から電子写真方式の中間転写ベルトを製造すると、平面性の悪化や電気抵抗のバラツキの増大を招くことがある。また、前記ポリアミック酸溶液組成物を、高濃度且つ低粘度の溶液組成物にした（ポリイミド前駆体の対数粘度を小さくした）ときには、ポリイミド膜を容易に得ることが容易ではなかった。
低濃度のポリアミック酸溶液組成物では、一度に厚いポリイミド膜を成形するのは困難であり、溶液組成物として多量の溶媒を必要とするとともに、その多量の溶媒を蒸発除去するために多くの時間とエネルギーを必要とする問題があった。
Polyimide membranes have excellent heat resistance and mechanical properties. Films processed as flexible insulating substrates and heat-resistant tape base materials, and those processed into tubular shapes are used for transporting heated articles It is preferably used as an application belt, an electrophotographic fixing belt or an intermediate transfer belt. Usually, such a polyimide film is manufactured using a polyamic acid solution composition having a high molecular weight (number average molecular weight of about 10,000 to 30,000) which is a polyimide precursor. Examples of the polyamic acid solution composition that can suitably produce an intermediate transfer belt include 3,3 ′, 4,4′-biphenyltetracarboxylic dianhydride and 4,4′- There is a polyamic acid solution composition obtained by reacting diaminodiphenyl ether with an approximately equimolar amount.
However, the polyamic acid solution composition may gradually undergo partial gelation during storage, and even if the gelation is extremely small, the physical properties of the final polyimide film are adversely affected. When an electrophotographic intermediate transfer belt is produced from a polyamic acid solution composition mixed with conductive carbon black, the planarity may be deteriorated and the electric resistance may be increased. Moreover, when the polyamic acid solution composition was made into a high-concentration and low-viscosity solution composition (the logarithmic viscosity of the polyimide precursor was reduced), it was not easy to obtain a polyimide film.
With a low concentration polyamic acid solution composition, it is difficult to form a thick polyimide film at a time, and a large amount of solvent is required as a solution composition, and a lot of time is required to evaporate and remove the large amount of solvent. And there was a problem that required energy.
特許文献２には、２種以上の芳香族テトラカルボン酸成分と芳香族ジアミンとの略等モル量を反応して得られる芳香族アミド酸オリゴマー、カーボンブラック、及び有機極性溶媒を含有してなる半導電性芳香族アミド酸組成物が開示され、前記半導電性芳香族アミド酸組成物を用いて、電子写真方式の中間転写ベルトに好適な半導電性無端管状ポリイミドフィルムを得ることが記載されている。
中間転写ベルトとして好適な３，３’，４，４’−ビフェニルテトラカルボン酸二無水物と４，４’−ジアミノジフェニルエーテルとをほぼ等モル反応させて得られたポリアミック酸溶液組成については、保存安定性において改良の余地があった。また、前記組成のポリアミック酸の対数粘度を小さくして得られる高濃度且つ低粘度のアミック酸オリゴマー溶液組成物を調製し、この溶液組成物を基材に塗布して膜状物に成形し次いで加熱処理してポリイミド膜を得ようとしても、加熱処理する際に、膜にひび割れが発生して良好なポリイミド膜を得ることが容易ではなかった。
したがって、本発明の目的は、中間転写ベルトとして好適な３，３’，４，４’−ビフェニルテトラカルボン酸二無水物と４，４’−ジアミノジフェニルエーテルからなるポリアミック酸溶液組成を用いて得られるポリイミド膜と同等乃至それ以上の優れた機械的特性を有し、保存安定性が優れ、且つ高濃度且つ低粘度のアミック酸オリゴマー溶液組成を基材に塗布して膜状物に成形し次いで加熱処理してポリイミド膜を得る場合でも、加熱処理時に膜にひび割れを発生することなしにポリイミド膜を得ることが可能な、特定の化学構造を有するポリイミド前駆体（ポリアミック酸乃至アミック酸オリゴマー）溶液組成物を提供することである。
The polyamic acid solution composition obtained by reacting 3,3 ′, 4,4′-biphenyltetracarboxylic dianhydride and 4,4′-diaminodiphenyl ether, which are suitable as an intermediate transfer belt, with an approximately equimolar reaction is preserved. There was room for improvement in stability. Further, a high concentration and low viscosity amic acid oligomer solution composition obtained by reducing the logarithmic viscosity of the polyamic acid having the above composition is prepared, and this solution composition is applied to a substrate to form a film-like product, Even if it was going to heat-process and obtain a polyimide film, when heat-processing, the film | membrane cracked and it was not easy to obtain a favorable polyimide film.
Therefore, the object of the present invention can be obtained by using a polyamic acid solution composition comprising 3,3 ′, 4,4′-biphenyltetracarboxylic dianhydride and 4,4′-diaminodiphenyl ether suitable as an intermediate transfer belt. Excellent mechanical properties equivalent to or better than polyimide film, excellent storage stability, high concentration and low viscosity amic acid oligomer solution composition applied to substrate, molded into film and then heated Even when a polyimide film is obtained by treatment, a polyimide precursor (polyamic acid or amic acid oligomer) solution composition having a specific chemical structure capable of obtaining a polyimide film without causing cracks in the film during heat treatment Is to provide things.
このポリイミド前駆体溶液組成物は、対数粘度が大きな（高分子量の）ポリアミック酸からなる場合でも対数粘度が小さい（低分子量化した）アミック酸オリゴマーからなる場合でも、最高加熱処理温度が２８０〜３９０℃の温度範囲で加熱処理することによって、中間転写ベルトとして好適な無端管状ポリイミド膜などのポリイミド膜を好適に製造することができる。 This polyimide precursor solution composition has a maximum heat treatment temperature of 280 to 390 regardless of whether it is made of a polyamic acid having a large logarithmic viscosity (high molecular weight) or an amic acid oligomer having a low logarithmic viscosity (lower molecular weight). By performing the heat treatment in a temperature range of ° C., a polyimide film such as an endless tubular polyimide film suitable as an intermediate transfer belt can be suitably produced.
本発明は以下の次項に関する。
１． 下記一般式（１）の繰返し単位を有するポリイミド前駆体を含有することを特徴とするポリイミド前駆体溶液組成物。
The present invention relates to the following items.
1. A polyimide precursor solution composition comprising a polyimide precursor having a repeating unit of the following general formula (1).
２． ポリイミド換算の固形分濃度が２０質量％以上であって且つ３０℃における溶液粘度が５０Ｐａ・ｓｅｃ以下であることを特徴とする項１に記載のポリイミド前駆体溶液組成物。 2. Item 2. The polyimide precursor solution composition according to Item 1, wherein the solid content concentration in terms of polyimide is 20% by mass or more and the solution viscosity at 30 ° C. is 50 Pa · sec or less.
３． 項１〜２のいずれかに記載のポリイミド前駆体溶液組成物を、基材に塗布して膜状物に成形し、最高加熱処理温度が２８０〜３９０℃の温度範囲で加熱処理してポリイミド膜を得ることを特徴とするポリイミド膜の製造方法。
４． 項１〜２のいずれかに記載のポリイミド前駆体溶液組成物を、回転成形法にて管状物に成形し、最高加熱処理温度が２８０〜３９０℃の温度範囲で加熱処理して無端管状ポリイミド膜を得ることを特徴とするポリイミド膜の製造方法。
3. The polyimide precursor solution composition according to any one of Items 1 and 2 is applied to a substrate and formed into a film-like material, and is subjected to a heat treatment within a temperature range of 280 to 390 ° C. to obtain a polyimide film. A method for producing a polyimide film, comprising:
4). The polyimide precursor solution composition according to any one of Items 1 and 2 is molded into a tubular product by a rotational molding method, and heat-treated at a maximum heat treatment temperature in a temperature range of 280 to 390 ° C. to endless tubular polyimide film A method for producing a polyimide film, comprising:
５． 項３〜４のいずれかに記載の製造方法によって製造されたことを特徴とするポリイミド膜。
６． 項５に記載の製造方法によって製造されたことを特徴とする電子写真方式の中間転写ベルトに用いられる半導電性無端管状ポリイミド膜。
5. Item 5. A polyimide film produced by the production method according to any one of Items 3 to 4.
6). A semiconductive endless tubular polyimide film used for an electrophotographic intermediate transfer belt, which is produced by the production method according to Item 5.
７． 下記一般式（５）の繰返し単位を有するポリイミドからなり、引張り破断強度が１７０ＭＰａ以上であり、引張弾性率が２．９ＧＰａ以上であり、引張破断伸度が５０％以上であることを特徴とするポリイミド膜。 7. It consists of a polyimide having a repeating unit of the following general formula (5), has a tensile breaking strength of 170 MPa or more, a tensile modulus of elasticity of 2.9 GPa or more, and a tensile breaking elongation of 50% or more. Polyimide film.
本願発明によって、中間転写ベルトとして好適な３，３’，４，４’−ビフェニルテトラカルボン酸二無水物と４，４’−ジアミノジフェニルエーテルからなるポリアミック酸溶液組成を用いて得られるポリイミド膜と同等乃至それ以上の優れた機械的特性を有し、保存安定性が優れ、且つ高濃度且つ低粘度のアミック酸オリゴマー溶液組成を基材に塗布して膜状物に成形し次いで加熱処理してポリイミド膜を得る場合でも、加熱処理時に膜にひび割れを発生することなしにポリイミド膜を好適に得ることができる、特定の化学構造からなるポリイミド前駆体（ポリアミック酸及び／又はアミック酸オリゴマー）溶液組成物を提供することができる。 Equivalent to a polyimide film obtained by using a polyamic acid solution composition comprising 3,3 ′, 4,4′-biphenyltetracarboxylic dianhydride and 4,4′-diaminodiphenyl ether suitable as an intermediate transfer belt according to the present invention A polyimide having an excellent mechanical property, excellent storage stability, a high-concentration and low-viscosity amic acid oligomer solution composition applied to a substrate, formed into a film-like material, and then heat-treated. Even when a film is obtained, a polyimide precursor (polyamic acid and / or amic acid oligomer) solution composition having a specific chemical structure, which can suitably obtain a polyimide film without causing cracks in the film during heat treatment Can be provided.
このポリイミド前駆体溶液組成物は、対数粘度が大きな（高分子量の）ポリアミック酸からなる場合でも対数粘度が小さい（低分子量化した）アミック酸オリゴマーからなる場合でも、最高加熱処理温度が２８０〜３９０℃の温度範囲で加熱処理することによって、中間転写ベルトとして好適な無端管状ポリイミド膜などのポリイミド膜を好適に製造することができる。 This polyimide precursor solution composition has a maximum heat treatment temperature of 280 to 390 regardless of whether it is made of a polyamic acid having a large logarithmic viscosity (high molecular weight) or an amic acid oligomer having a low logarithmic viscosity (lower molecular weight). By performing the heat treatment in a temperature range of ° C., a polyimide film such as an endless tubular polyimide film suitable as an intermediate transfer belt can be suitably produced.
本発明において、「ポリイミド前駆体」は、比較的高分子量（通常は数平均分子量が１００００以上）のポリアミック酸及び／又は比較的低分子量（通常は数平均分子量が１００００未満）のアミック酸オリゴマーを意味する用語として用いる。 In the present invention, the “polyimide precursor” is a polyamic acid having a relatively high molecular weight (usually a number average molecular weight of 10,000 or more) and / or an amic acid oligomer having a relatively low molecular weight (usually a number average molecular weight of less than 10,000). Used as a term to mean.
本発明のポリイミド前駆体溶液組成物は、前記一般式（１）の繰返し単位を有するポリイミド前駆体（ポリアミック酸及び／又はアミック酸オリゴマー）を有機溶媒に溶解した溶液組成物である。このポリイミド前駆体溶液組成物、特に比較的高分子量のポリアミック酸からなるポリイミド前駆体溶液組成物は、有機溶媒中で、３，３’，４，４’−ビフェニルテトラカルボン酸類からなるテトラカルボン酸成分と、５０〜９５モル％の４，４’−ジアミノジフェニルエーテルと５０〜５モル％の２，４−トルエンジアミンとからなるジアミン成分とを、イミド化を抑制するために１２０℃以下、好ましくは１００℃以下、より好ましくは８０℃以下の温度で、例えば０．１〜５０時間程度反応することによって好適に調製することができる。 The polyimide precursor solution composition of the present invention is a solution composition in which a polyimide precursor (polyamic acid and / or amic acid oligomer) having the repeating unit of the general formula (1) is dissolved in an organic solvent. This polyimide precursor solution composition, in particular, a polyimide precursor solution composition comprising a relatively high molecular weight polyamic acid is a tetracarboxylic acid comprising 3,3 ′, 4,4′-biphenyltetracarboxylic acids in an organic solvent. In order to suppress imidization, the component and a diamine component composed of 50 to 95 mol% of 4,4′-diaminodiphenyl ether and 50 to 5 mol% of 2,4-toluenediamine, It can be suitably prepared by reacting at a temperature of 100 ° C. or lower, more preferably 80 ° C. or lower, for about 0.1 to 50 hours.
また、比較的低分子量のアミック酸オリゴマーからなるポリイミド前駆体溶液組成物は、前記反応を、水を介在させて、分子量を低分子量へ調節することによって好適に得ることができる。具体例としては、特開昭５７−１３１２４８号公報に記載されているように、テトラカルボン酸二無水物とジアミンとを実質的に等モル使用して、その酸無水物１モルに対して約０．５〜４０モル倍の水を含有する有機溶媒中で１００℃以下の温度で反応させ、その半応益が均一溶液となった後で、その反応液から遊離の水を除去する方法を好適に挙げることができる。或いは、ジアミン成分とジアミン成分に対して過剰モルのテトラカルボン酸二無水物とを、前記テトラカルボン酸成分に対して１／３モル倍を越える量の水を含有する溶媒中で反応し、次いで全体としてジアミンとテトラカルボン酸二無水物とが実質的に等モルになるようにジアミン、又はジアミンとテトラカルボン酸二無水物とを加えて更に反応する方法を好適に挙げることができる。 Moreover, the polyimide precursor solution composition which consists of a comparatively low molecular weight amic acid oligomer can be suitably obtained by adjusting the molecular weight to a low molecular weight by interposing water. As a specific example, as described in JP-A-57-13248, tetracarboxylic dianhydride and diamine are used in substantially equimolar amounts, and about 1 mol of the acid anhydride is used. A method in which free water is removed from the reaction solution after reacting at a temperature of 100 ° C. or less in an organic solvent containing 0.5 to 40 moles of water and the semi-beneficial effect becomes a homogeneous solution. Can be listed. Alternatively, the diamine component and an excess mole of tetracarboxylic dianhydride with respect to the diamine component are reacted in a solvent containing water in an amount exceeding 1/3 mole of the tetracarboxylic acid component, and then A method of further reacting by adding diamine or diamine and tetracarboxylic dianhydride so that the diamine and tetracarboxylic dianhydride become substantially equimolar as a whole can be preferably mentioned.
本発明のポリイミド前駆体溶液組成物は、ジアミン成分とテトラカルボン酸成分とが実質的に等モルであることが好ましい。具体的にはジアミン成分とテトラカルボン酸成分とのモル比が、好ましくは１：０．９５〜１：１．０５、より好ましくは１：０．９８〜１：１．０２である。この範囲外になると得られるポリイミド膜の機械的特性が低下するので好ましくない。なお、本発明のポリイミド前駆体溶液組成物においては、本発明の効果の範囲内において、未反応のジアミン成分或いはテトラカルボン酸成分を少量含んでいても構わない。 In the polyimide precursor solution composition of the present invention, the diamine component and the tetracarboxylic acid component are preferably substantially equimolar. Specifically, the molar ratio of the diamine component to the tetracarboxylic acid component is preferably 1: 0.95 to 1: 1.05, more preferably 1: 0.98 to 1: 1.02. Outside this range, the mechanical properties of the resulting polyimide film are deteriorated, which is not preferable. The polyimide precursor solution composition of the present invention may contain a small amount of an unreacted diamine component or tetracarboxylic acid component within the scope of the effect of the present invention.
ポリイミド前駆体の調製に用いられるテトラカルボン酸成分は、実質的に１００モル％が３，３’，４，４’−ビフェニルテトラカルボン酸類、すなわち、３，３’，４，４’−ビフェニルテトラカルボン酸、その無水化物、或いはそのエステル化物であり、特に好ましくは３，３’，４，４’−ビフェニルテトラカルボン酸二無水物である。他のテトラカルボン酸成分を、この発明の効果の範囲内で用いることもできるが、その際でも１０モル％以下、好ましくは５モル％以下である。
ジアミン成分は、５０〜９５モル％、好ましくは６０〜９５モル％、より好ましくは７０〜９０モル％の４，４’−ジアミノジフェニルエーテルと、５０〜５モル％、好ましくは４０〜５モル％、より好ましくは３０〜１０モル％の２，４−トルエンジアミンとである。この組成で得られるポリイミド膜は、中間転写ベルトとして好適な３，３’，４，４’−ビフェニルテトラカルボン酸二無水物と４，４’−ジアミノジフェニルエーテルからなるポリアミック酸溶液組成を用いて得られるポリイミド膜と同等乃至それ以上の優れた耐熱性や機械的特性を有する。ジアミン成分中の２，４−トルエンジアミンの割合が、この組成の範囲を越えて多くなると機械的特性が低下する。
The tetracarboxylic acid component used for the preparation of the polyimide precursor is substantially 100 mol% 3,3 ′, 4,4′-biphenyltetracarboxylic acid, that is, 3,3 ′, 4,4′-biphenyltetra. Carboxylic acid, its anhydride, or its esterified product, and particularly preferably 3,3 ′, 4,4′-biphenyltetracarboxylic dianhydride. Other tetracarboxylic acid components can also be used within the scope of the effect of the present invention, but in this case, they are also 10 mol% or less, preferably 5 mol% or less.
The diamine component is 50 to 95 mol%, preferably 60 to 95 mol%, more preferably 70 to 90 mol% of 4,4'-diaminodiphenyl ether, 50 to 5 mol%, preferably 40 to 5 mol%, More preferably, it is 30 to 10 mol% 2,4-toluenediamine. A polyimide film obtained with this composition is obtained by using a polyamic acid solution composition composed of 3,3 ′, 4,4′-biphenyltetracarboxylic dianhydride and 4,4′-diaminodiphenyl ether suitable as an intermediate transfer belt. It has excellent heat resistance and mechanical properties equivalent to or higher than those of polyimide films. If the proportion of 2,4-toluenediamine in the diamine component is increased beyond the range of this composition, the mechanical properties deteriorate.
ポリイミド前駆体の調製に用いられる溶媒は、ポリイミド前駆体を溶解し得るものであって、常圧での沸点が３００℃以下の有機極性溶媒が好ましく、例えばＮ，Ｎ−ジメチルアセトアミド、Ｎ，Ｎ−ジエチルアセトアミド、Ｎ，Ｎ−ジメチルホルムアミド、Ｎ，Ｎ−ジエチルホルムアミド、Ｎ−メチル−２−ピロリドン、１，３−ジメチル−２−イミダゾリジノン、Ｎ−メチルカプロラクタムなどの窒素原子を分子内に含有する溶媒、例えばジメチルスルホキシド、ジエチルスルホキシド、ジメチルスルホン、ジエチルスルホン、ヘキサメチルスルホルアミドなどの硫黄原子を分子内に含有する溶媒、例えばクレゾール、フェノール、キシレノールなどフェノール類からなる溶媒、例えばジエチレングリコールジメチルエーテル（ジグライム）、トリエチレングリコールジメチルエーテル（トリグライム）、テトラグライムなどの酸素原子を分子内に含有する溶媒、その他、アセトン、ジメチルイミダゾリン、メタノール、エタノール、エチレングリコール、ジオキサン、テトラヒドロフラン、ピリジン、テトラメチル尿素などを挙げることができる。これらの溶媒は単独で又これらの溶媒を混合して好適に使用される。 The solvent used for the preparation of the polyimide precursor is capable of dissolving the polyimide precursor, and is preferably an organic polar solvent having a boiling point of 300 ° C. or less at normal pressure, for example, N, N-dimethylacetamide, N, N -Nitrogen atoms such as diethylacetamide, N, N-dimethylformamide, N, N-diethylformamide, N-methyl-2-pyrrolidone, 1,3-dimethyl-2-imidazolidinone, N-methylcaprolactam in the molecule Solvents containing, for example, solvents containing sulfur atoms in the molecule such as dimethyl sulfoxide, diethyl sulfoxide, dimethyl sulfone, diethyl sulfone, hexamethylsulfuramide, etc. (Zigrai ), Solvents containing oxygen atoms in the molecule such as triethylene glycol dimethyl ether (triglyme), tetraglyme, and others, acetone, dimethylimidazoline, methanol, ethanol, ethylene glycol, dioxane, tetrahydrofuran, pyridine, tetramethylurea, etc. be able to. These solvents are preferably used alone or as a mixture of these solvents.
本発明のポリイミド前駆体溶液組成物において、ポリイミド前駆体は高分子量でも低分子量でもよく、その対数粘度（ηｉｎｈ）は０．０５〜３．５、好ましくは０．１０〜３．０、より好ましくは０．１５〜２．５の範囲のものが好適に使用できる。また、アミック酸構造の一部（５０モル％以下、好ましくは２０モル％以下、より好ましくは５モル％以下）が脱水反応を起こしてイミド環を形成したものであっても構わない。なぜなら、このポリイミド前駆体は、低分子量でも高分子量でも有機溶媒に対する溶解性が高く、且つイミド環を形成しても溶解性が低下することが少ないからである。この良好な溶解性によって、保存時のゲル化が抑制されて保存安定性（或いは保存後の成形性）が良好になっている。したがって、本発明のポリイミド前駆体溶液組成物は、低濃度の溶液組成物のみでなく、ポリイミド換算の固形分濃度が２０〜６０質量％、好ましくは２５〜６０質量％、より好ましくは３０〜６０質量％であって、且つ３０℃における溶液粘度が５０Ｐａ・ｓｅｃ以下、好ましくは３０Ｐａ・ｓｅｃ以下、より好ましくは２０Ｐａ・ｓｅｃ以下の、高濃度且つ低溶液粘度の溶液組成物として好適に用いることができる。なお、溶液粘度の下限値は好ましくは０．５Ｐａ・ｓｅｃ以上、通常は１Ｐａ・ｓｅｃ以上である。 In the polyimide precursor solution composition of the present invention, the polyimide precursor may be high molecular weight or low molecular weight, and its logarithmic viscosity (ηinh) is 0.05 to 3.5, preferably 0.10 to 3.0, more preferably. Can be preferably used in the range of 0.15 to 2.5. Further, a part of the amic acid structure (50 mol% or less, preferably 20 mol% or less, more preferably 5 mol% or less) may cause a dehydration reaction to form an imide ring. This is because this polyimide precursor has high solubility in an organic solvent regardless of whether it has a low molecular weight or a high molecular weight, and the solubility does not decrease even when an imide ring is formed. Due to this good solubility, gelation during storage is suppressed, and storage stability (or moldability after storage) is improved. Therefore, the polyimide precursor solution composition of the present invention has not only a low concentration solution composition but also a solid content concentration in terms of polyimide of 20 to 60% by mass, preferably 25 to 60% by mass, more preferably 30 to 60%. It is preferably used as a high-concentration and low-solution viscosity solution composition having a mass% and a solution viscosity at 30 ° C. of 50 Pa · sec or less, preferably 30 Pa · sec or less, more preferably 20 Pa · sec or less. it can. The lower limit of the solution viscosity is preferably 0.5 Pa · sec or more, and usually 1 Pa · sec or more.
本発明のポリイミド前駆体溶液組成物は、基材に塗布して膜状物を形成し、より好ましくは最高加熱温度が２８０〜３９０℃の範囲で加熱処理して膜厚が０．１〜２００μｍ、好ましくは３〜１５０μｍ、より好ましくは５〜１３０μｍのポリイミド膜を好適に得ることができる。
本発明において、基材とは、表面にポリイミド前駆体溶液組成物を塗布して膜状物（塗膜）が形成できるものであり、液体や気体を実質的に透過させない程度の緻密構造を有していれば、形状や材質で特に限定されるものではない。通常のフィルムを製造する際に用いられるそれ自体公知のベルト、金型、ロールなどのフィルム形成用基材、その表面にポリイミド膜を絶縁保護膜として形成する回路基板などの電子部品や電線、表面に皮膜が形成される摺動部品や製品、ポリイミド膜を形成して多層化フィルムや銅張積層基板を形成する際の一方のフィルムや銅箔などを好適に挙げることができる。
The polyimide precursor solution composition of the present invention is applied to a substrate to form a film-like material, and more preferably a heat treatment is performed at a maximum heating temperature in the range of 280 to 390 ° C. to form a film thickness of 0.1 to 200 μm. A polyimide film having a thickness of preferably 3 to 150 μm, more preferably 5 to 130 μm can be suitably obtained.
In the present invention, the base material is a material on which a polyimide precursor solution composition can be applied to form a film (coating film), and has a dense structure that does not substantially allow liquid or gas to permeate. If it does, it will not be specifically limited by a shape or a material. Electronic parts such as belts, molds, rolls, etc. used for the production of ordinary films, such as belts, molds, rolls, etc., electronic components such as circuit boards on which the polyimide film is formed as an insulating protective film, electric wires, surfaces Suitable examples include sliding parts and products on which a film is formed on the surface, one film or copper foil when a polyimide film is formed to form a multilayer film or a copper-clad laminate.
基材に塗布する方法としては、例えばスプレー法、ロールコート法、回転塗布法、バー塗布法、インクジェット法、スクリーン印刷法、スリットコート法などのそれ自体公知の方法を適宜採用することができる。 As a method of applying to the substrate, for example, a method known per se such as a spray method, a roll coating method, a spin coating method, a bar coating method, an ink jet method, a screen printing method, or a slit coating method can be appropriately employed.
この基材に塗布されて形成された膜状物は、例えば減圧下又は常圧下に比較的低温で加熱する方法で脱泡しても構わない。
基材上に形成されたポリイミド前駆体溶液組成物からなる膜状物は、加熱処理することによって溶媒を除去し且つイミド化されてポリイミド膜が形成される。加熱処理は、いきなり高温で加熱処理するよりも最初に１４０℃以下の比較的低温で溶媒を除去し、次いで最高加熱処理温度まで温度を上げてイミド化する段階的な加熱処理が好適である。また、１４０℃以上で０．０１〜３０時間好ましくは０．０１〜１０時間より好ましくは０．０１〜６時間の加熱処理を行って実質的にアミド酸基が残らないようにイミド化することが好適である。最高加熱処理温度は２５０〜６００℃の温度範囲が採用できるが、より好ましくは２８０〜３９０℃の温度範囲である。この温度範囲で０．０１〜２０時間好ましくは０．０１〜６時間より好ましくは０．０１〜５時間加熱処理することが好適である。このように段階的に温度を上げる加熱処理条件としては、例えば８０℃で３０分間、１３０℃で１０分間、２００℃で１０分間、そして最後に最高加熱温度の範囲内で１０分間加熱処理する（但し、次の段階へは１０分間で昇温する）加熱処理条件を例示することができる。
The film-like material formed by applying to this substrate may be defoamed by a method of heating at a relatively low temperature under reduced pressure or normal pressure, for example.
The film-like product made of the polyimide precursor solution composition formed on the substrate is heat-treated to remove the solvent and imidized to form a polyimide film. The heat treatment is preferably a stepwise heat treatment in which the solvent is first removed at a relatively low temperature of 140 ° C. or lower, and then imidized by raising the temperature to the maximum heat treatment temperature, rather than suddenly performing the heat treatment at a high temperature. Moreover, imidation is performed so that amidic acid groups do not substantially remain by performing heat treatment at 140 ° C. or more for 0.01 to 30 hours, preferably 0.01 to 10 hours, more preferably 0.01 to 6 hours. Is preferred. Although the temperature range of 250-600 degreeC can be employ | adopted for the maximum heat processing temperature, More preferably, it is a temperature range of 280-390 degreeC. It is suitable to heat-treat in this temperature range for 0.01 to 20 hours, preferably 0.01 to 6 hours, more preferably 0.01 to 5 hours. As the heat treatment conditions for raising the temperature stepwise in this way, for example, heat treatment is performed at 80 ° C. for 30 minutes, 130 ° C. for 10 minutes, 200 ° C. for 10 minutes, and finally within the maximum heating temperature range for 10 minutes ( However, the heat treatment conditions can be exemplified, where the temperature is raised in 10 minutes to the next stage).
また、本発明のポリイミド前駆体溶液組成物は、回転成形法にて管状物に成形し、この管状物を前記と同じように脱泡したり加熱処理したりすることで容易に無端管状ポリイミド膜を得ることができる。例えば、回転成形法は基材の役割を有する円筒状の金型を回転させながら、金型（内側乃至外側）表面にポリイミド前駆体溶液組成物からなる塗膜を形成し、２００℃以下の比較的低温で加熱処理して溶媒を揮発させて自己支持性膜（溶媒が除去され被膜の流動が発生しない状態、完全ではないが重合及びイミド化反応が進んでいる）を形成し、次いで前記自己支持性膜をそのまま或いは必要に応じて基材から剥がしたり、裏返したり、適度の張力を掛けたりしながら、最高熱処理温度まで直接乃至段階的に昇温する手順で加熱処理することによって無端管状ポリイミド膜を好適に得ることができる。本発明においては、最高加熱処理温度は２５０〜６００℃の温度範囲が採用できるが、好ましくは２８０〜３９０℃、より好ましくは３００〜３９０℃、更に好ましくは３４０〜３８０℃の温度範囲である。２５０℃以下では十分な重合イミド化反応が達成できなくなって良好な機械的強度が得られなくなることがある。また、３９０℃を越えた温度まで加熱すると脆くなって機械的な特性が低下する。 Further, the polyimide precursor solution composition of the present invention is formed into a tubular product by a rotational molding method, and the tubular product is easily defoamed or heat-treated in the same manner as described above to easily endless tubular polyimide film. Can be obtained. For example, the rotational molding method forms a coating film composed of a polyimide precursor solution composition on the surface of a mold (inner side to outer side) while rotating a cylindrical mold having a role of a base material, and the comparison is performed at 200 ° C. or lower. Heat treatment at a low temperature to volatilize the solvent to form a self-supporting membrane (the solvent is removed and no flow of the coating occurs, the polymerization and imidization reactions are not complete, but the self-supporting membrane is in progress) Endless tubular polyimide by heat-treating directly or stepwise up to the maximum heat treatment temperature while peeling the supporting film as it is or peeling off from the base material as needed, applying appropriate tension A film can be suitably obtained. In the present invention, the maximum heat treatment temperature can be in the temperature range of 250 to 600 ° C, preferably 280 to 390 ° C, more preferably 300 to 390 ° C, and still more preferably 340 to 380 ° C. If it is 250 ° C. or lower, a sufficient polymerization imidization reaction cannot be achieved, and good mechanical strength may not be obtained. Moreover, if it heats to the temperature exceeding 390 degreeC, it will become weak and a mechanical characteristic will fall.
本発明のポリイミド前駆体溶液組成物を用いれば、厚さが０．１〜２００μｍのポリイミド膜を好適に得ることができる。特にポリイミド前駆体溶液組成物を高濃度且つ低溶液粘度をとしたとき、すなわちポリイミド前駆体の対数粘度（ηｉｎｈ）が０．４以下、特に０．３以下、更に０．２以下のときでも、好適にポリイミド膜を得ることができる。そして、得られたポリイミド膜は、引張強度が１７０ＭＰａ以上、好ましくは１９０ＭＰａ以上、より好ましくは２００ＭＰａ以上であり、引張弾性率が３．０ＭＰａ以上であり、引張伸度が４０％以上、好ましくは５０％以上、より好ましくは６０％以上であるので、中間転写ベルトとして好適な３，３’，４，４’−ビフェニルテトラカルボン酸二無水物と４，４’−ジアミノジフェニルエーテルとをほぼ等モル反応させて得られたポリアミック酸溶液組成物を用いたポリイミド膜と同等乃至それ以上の機械的特性を有している。すなわち、本発明のポリイミド前駆体溶液組成物を用いれば容易に優れた中間転写ベルトとして用いることができる半導電性無端管状ポリイミド膜を得ることができる。 If the polyimide precursor solution composition of the present invention is used, a polyimide film having a thickness of 0.1 to 200 μm can be suitably obtained. Especially when the polyimide precursor solution composition has a high concentration and a low solution viscosity, that is, even when the logarithmic viscosity (ηinh) of the polyimide precursor is 0.4 or less, particularly 0.3 or less, and further 0.2 or less, A polyimide film can be suitably obtained. The obtained polyimide film has a tensile strength of 170 MPa or more, preferably 190 MPa or more, more preferably 200 MPa or more, a tensile modulus of 3.0 MPa or more, and a tensile elongation of 40% or more, preferably 50 % Or more, more preferably 60% or more. Therefore, an approximately equimolar reaction of 3,3 ′, 4,4′-biphenyltetracarboxylic dianhydride and 4,4′-diaminodiphenyl ether suitable as an intermediate transfer belt is performed. It has a mechanical property equivalent to or higher than that of a polyimide film using the polyamic acid solution composition obtained by the above process. That is, if the polyimide precursor solution composition of the present invention is used, a semiconductive endless tubular polyimide film that can be easily used as an excellent intermediate transfer belt can be obtained.
本発明のポリイミド前駆体溶液組成物を用いて中間転写ベルトを形成するときには、中間転写ベルトとして要求される半導電性などの特性を付与するために、組成物中にカーボンブラックなどの導電性材料を添加して用いる。このような用途での配合は、例えば特許文献１、２に記載されたような公知の配合を好適に採用することができる。
すなわち、中間転写ベルトの転写面の表面抵抗率は、１×１０１０Ω／ｍ２〜１×１０１４Ω／ｍ２の範囲であり、好ましくは１×１０１１Ω／ｍ２〜１×１０１２Ω／ｍ２の半導電性の範囲である。このような半導電性の表面抵抗率を有する中間転写ベルトは、電子導電性を付与するための導電材を均一に分散したポリイミド前駆体溶液組成物を、例えば基材の役割を有する円筒状の金型を回転させながら、金型（内側乃至外側）表面にポリイミド前駆体溶液組成物からなる塗膜を形成して加熱処理する方法によって好適に得ることができる。
When an intermediate transfer belt is formed using the polyimide precursor solution composition of the present invention, a conductive material such as carbon black is added to the composition in order to impart characteristics such as semiconductivity required for the intermediate transfer belt. Is used. For such blending, for example, a known blending described in Patent Documents 1 and 2 can be suitably employed.
That is, the surface resistivity of the transfer surface of the intermediate transfer belt is in the range of 1 × 10 10 Ω / m 2 to 1 × 10 14 Ω / m 2 , and preferably 1 × 10 11 Ω / m 2 to 1 × 10. This is a semiconductive range of 12 Ω / m 2 . Such an intermediate transfer belt having a semiconductive surface resistivity is obtained by using a polyimide precursor solution composition in which a conductive material for imparting electronic conductivity is uniformly dispersed, for example, a cylindrical shape having the role of a substrate. It can be suitably obtained by a method of forming a coating film composed of the polyimide precursor solution composition on the surface of the mold (inner side to outer side) while rotating the mold and heat-treating it.
電子導電性を付与するための導電材としては、カーボンブラック、グラファイト、アルミニウム、銅合金等の金属もしくは合金、酸化錫、酸化亜鉛、チタン酸カリウム、酸化錫−酸化インジウムもしくは酸化錫−酸化アンチモン複合酸化物等の金属酸化物等の導電性或いは半導電性の微粉末が好適に用いられる。これらの導電材は単独でも複数種を併用して用いることもできる。これらの中では、分散性、分散安定性、半導電性ポリイミド無端ベルトの抵抗バラツキ、電界依存性、電気抵抗の経時での安定性などを考慮すると、カーボンブラック、特に表面にカルボキシル基、キノン基、ラクトン基、水酸基等を付与して製造したｐＨ５以下の酸化処理カーボンブラックを好適に用いることができる。またカーボンブラックとしては、その揮発成分が１〜２５質量％、好ましくは３〜１５質量％程度のものが好適である。カーボンブラックとしては、アセチレンブラック、ファーネスブラック、ケッチェンブラック、チャンネルブラック等が挙げられる。
具体的には、デグサ社製の「プリンテックス１５０Ｔ」（ｐＨ４．５、揮発分１０．０質量％）、同「スペシャルブラック３５０」（ｐＨ３．５、揮発分２．２質量％）、同「スペシャルブラック１００」（ｐＨ３．３、揮発分２．２質量％）、同「スペシャルブラック２５０」（ｐＨ３．１、揮発分２．０質量％）、同「スペシャルブラック５」（ｐＨ３．０、揮発分１５．０質量％）、同「スペシャルブラック４」（ｐＨ３．０、揮発分１４．０質量％）、同「スペシャルブラック４Ａ」（ｐＨ３．０、揮発分１４．０質量％）、同「スペシャルブラック５５０」（ｐＨ２．８、揮発分２．５質量％）、同「スペシャルブラック６」（ｐＨ２．５、揮発分１８．０質量％）、同「カラーブラックＦＷ２００」（ｐＨ２．５、揮発分２０．０質量％）、同「カラーブラックＦＷ２」（ｐＨ２．５、揮発分１６．５質量％）、同「カラーブラックＦＷ２Ｖ」（ｐＨ２．５、揮発分１６．５質量％）、キャボット社製「ＭＯＮＡＲＣＨ１０００」（ｐＨ２．５、揮発分９．５質量％）、キャボット社製「ＭＯＮＡＲＣＨ１３００」（ｐＨ２．５、揮発分９．５質量％）、キャボット社製「ＭＯＮＡＲＣＨ１４００」（ｐＨ２．５、揮発分９．０質量％）、同「ＭＯＧＵＬ−Ｌ」（ｐＨ２．５、揮発分５．０質量％）、同「ＲＥＧＡＬ４００Ｒ」（ｐＨ４．０、揮発分３．５質量％）などを好適に挙げることができる。
分散方法としては公知の方法が適用でき、ボールミル、サンドミル、バスケットミル、超音波分散などを好適に挙げることができる。添加量は、限定するものではないが、ポイミドに換算した固形分に対して１０〜１７質量％程度が好適である。
Conductive materials for imparting electronic conductivity include metals or alloys such as carbon black, graphite, aluminum and copper alloys, tin oxide, zinc oxide, potassium titanate, tin oxide-indium oxide or tin oxide-antimony oxide composite. Conductive or semiconductive fine powders such as metal oxides such as oxides are preferably used. These conductive materials can be used alone or in combination of two or more. Among these, considering the dispersibility, dispersion stability, resistance variation of the semiconductive polyimide endless belt, electric field dependency, stability of electrical resistance over time, etc., carbon black, especially carboxyl group and quinone group on the surface. In addition, an oxidized carbon black having a pH of 5 or less produced by adding a lactone group, a hydroxyl group or the like can be preferably used. Moreover, as carbon black, the thing whose volatile component is 1-25 mass%, Preferably about 3-15 mass% is suitable. Examples of carbon black include acetylene black, furnace black, ketjen black, and channel black.
Specifically, “Printex 150T” (pH 4.5, volatile content 10.0% by mass), “Special Black 350” (pH 3.5, volatile content 2.2% by mass), “ "Special Black 100" (pH 3.3, volatile matter 2.2 mass%), "Special Black 250" (pH 3.1, volatile matter 2.0 mass%), "Special Black 5" (pH 3.0, volatile) 15.0% by mass), “Special Black 4” (pH 3.0, volatile content 14.0% by mass), “Special Black 4A” (pH 3.0, volatile content 14.0% by mass), “ “Special Black 550” (pH 2.8, volatile content 2.5% by mass), “Special Black 6” (pH 2.5, volatile content 18.0% by mass), “Color Black FW200” (pH 2.5, volatile) Minute 20. %), “Color Black FW2” (pH 2.5, volatile content 16.5% by mass), “Color Black FW2V” (pH 2.5, volatile content 16.5% by mass), “MONARCH1000” manufactured by Cabot Corporation. (PH 2.5, volatile matter 9.5 mass%), “MONARCH 1300” manufactured by Cabot (pH 2.5, volatile content 9.5 mass%), “MONARCH 1400” manufactured by Cabot (pH 2.5, volatile content 9.0) (Mass%), “MOGUL-L” (pH 2.5, volatile matter 5.0% by mass), “REGAL400R” (pH 4.0, volatile matter 3.5% by mass) and the like can be preferably mentioned.
As a dispersion method, a known method can be applied, and a ball mill, a sand mill, a basket mill, an ultrasonic dispersion and the like can be preferably exemplified. The addition amount is not limited, but is preferably about 10 to 17% by mass with respect to the solid content converted to poimide.
本発明のポリイミド前駆体溶液組成物は、前記導電材以外の種々の添加剤や充填材を用いても構わない。それらの例としては、消泡剤、界面活性剤、顔料や染料などの着色剤、反応触媒、アルミナなどの無機や有機の充填材、補強繊維などを好適に挙げることができる。 The polyimide precursor solution composition of the present invention may use various additives and fillers other than the conductive material. Preferred examples thereof include antifoaming agents, surfactants, colorants such as pigments and dyes, reaction catalysts, inorganic and organic fillers such as alumina, and reinforcing fibers.
以下本発明を実施例によって更に説明する。なお、本発明は以下の実施例に限定されるものではない。 The invention is further illustrated by the following examples. In addition, this invention is not limited to a following example.
以下の例で用いた化合物の略号や測定方法について説明する。
ｓ−ＢＰＤＡ：３，３’，４，４’−ビフェニルテトラカルボン酸二無水物
ＯＤＡ：オキシジアニリン（４，４’−ジアミノジフェニルエーテル）
２，４−ＴＤＡ：２，４−トルエンジアミン
ＮＭＰ：Ｎ−メチル−２−ピロリドン
The abbreviations and measurement methods of the compounds used in the following examples will be described.
s-BPDA: 3,3 ′, 4,4′-biphenyltetracarboxylic dianhydride ODA: oxydianiline (4,4′-diaminodiphenyl ether)
2,4-TDA: 2,4-toluenediamine NMP: N-methyl-2-pyrrolidone
〔固形分濃度〕
試料溶液（その質量をｗ１とする）を、熱風乾燥機中１２０℃で１０分間、２５０℃で１０分間、次いで３５０℃で３０分間加熱処理して、加熱処理後の質量（その質量をｗ２とする）を測定する。ポリイミド換算の固形分濃度［質量％］は次式によって算出した。
固形分濃度＝（ｗ２／ｗ１）×１００
[Solid concentration]
The sample solution (whose mass is designated as w1) is heat-treated in a hot air dryer at 120 ° C. for 10 minutes, 250 ° C. for 10 minutes, and then at 350 ° C. for 30 minutes. Measure). The solid content concentration [% by mass] in terms of polyimide was calculated by the following formula.
Solid content concentration = (w2 / w1) × 100
〔対数粘度〕
試料溶液を、固形分濃度に基づいて濃度が０．５ｇ／ｄｌ（溶媒はＮＭＰ）になるように希釈した。この希釈液を、３０℃にて、キャノンフェンスケＮｏ．１００を用いて流下時間（Ｔ１）を測定した。対数粘度は、ブランクのＮＭＰの流下時間（Ｔ０）を用いて、次式から算出した。
対数粘度＝｛ｌｎ（Ｔ１／Ｔ０）｝／０．５
(Logarithmic viscosity)
The sample solution was diluted to a concentration of 0.5 g / dl (solvent is NMP) based on the solid content concentration. This diluted solution was added to Cannon Fenceke No. The flow-down time (T 1 ) was measured using 100. The logarithmic viscosity was calculated from the following equation using the flow time (T 0 ) of blank NMP.
Logarithmic viscosity = {ln (T 1 / T 0 )} / 0.5
〔溶液粘度（回転粘度）〕
トキメック社製Ｅ型粘度計を用いて３０℃で測定した。
[Solution viscosity (rotational viscosity)]
It measured at 30 degreeC using the Tokimec E-type viscosity meter.
〔溶液安定性〕
試料を、５℃の温度に調整された雰囲気中に保管し、１ケ月後の試料溶液を目視によって観察し、濁りや相分離・析出の有無を確認した。濁りや相分離・析出があるものは×、変化がないものを○とした。
(Solution stability)
The sample was stored in an atmosphere adjusted to a temperature of 5 ° C., and the sample solution after one month was visually observed to check for turbidity and phase separation / precipitation. Those with turbidity or phase separation / precipitation were marked with x, and those without change were marked with ◯.
〔製膜性（ポリイミド膜の状態）〕
ガラス基板上に、得られるポリイミド膜を所定の厚みとなるように試料溶液を塗布し、熱風乾燥機中、１２０℃で３０分間、１５０℃で１０分間、２００℃で１０分間、２５０℃で１０分間、次いで最高加熱温度で１０分間加熱処理して、溶媒の除去及び重合イミド化反応を行わせてポリイミド膜を製造した。得られたポリイミド膜の状態を次のとおり目視観察した。すなわち、目視によってフクレ、割れ、粉化等の不具合の有無を確認し、フクレ、割れ、粉化等の不具合がないものを○、フクレ、割れ、粉化等の不具合が生じたものを×とした。
[Film forming properties (state of polyimide film)]
A sample solution is applied on a glass substrate so that the obtained polyimide film has a predetermined thickness. In a hot air dryer, 120 ° C. for 30 minutes, 150 ° C. for 10 minutes, 200 ° C. for 10 minutes, and 250 ° C. for 10 minutes. Heat treatment was performed for 10 minutes at the maximum heating temperature for 10 minutes, and the removal of the solvent and polymerization imidization reaction were performed to produce a polyimide film. The state of the obtained polyimide film was visually observed as follows. That is, visually check for defects such as blisters, cracks, powdering, etc., with no defects such as blisters, cracks, powdering, etc. did.
〔引張破断強度〕
引張り試験機（オリエンテック社製ＲＴＣ−１２２５Ａ）を用いて、ＡＳＴＭ Ｄ８８２に準拠して測定した。
[Tensile strength at break]
It measured based on ASTM D882 using the tensile tester (Orientec RTC-1225A).
〔引張破断伸度〕
引張り試験機（オリエンテック社製ＲＴＣ−１２２５Ａ）を用いて、ＡＳＴＭ Ｄ８８２に準拠して測定した。
(Tensile elongation at break)
It measured based on ASTM D882 using the tensile tester (Orientec RTC-1225A).
〔引張弾性率〕
引張り試験機（オリエンテック社製ＲＴＣ−１２２５Ａ）を用いて、ＡＳＴＭ Ｄ８８２に準拠して測定した。
[Tensile modulus]
It measured based on ASTM D882 using the tensile tester (Orientec RTC-1225A).
〔実施例１〕
撹拌機、撹拌羽根、還流冷却器、窒素ガス導入管を備えた１ＬのセパラブルフラスコにＮＭＰ６７０．００ｇ、水３．６７ｇ、ｓ−ＢＰＤＡ７９．８０ｇ、及びＯＤＡ２４．４４ｇ（水のモル比［水／酸成分］が３／４、水の含有率が０．４７質量％、酸成分のモル比［酸成分／ジアミン成分］が２／１）を秤取り、７０℃の反応温度で３時間撹拌して反応させた。次いで、この反応溶液へＯＤＡ９７．７７ｇと２，４−ＴＤＡ８．２８ｇとを溶解させ、さらにｓ−ＢＰＤＡ１１９．７０ｇを添加して、反応温度５０℃で２０時間撹拌しながら反応させた。
得られた反応溶液は、対数粘度が０．２４、溶液粘度が８．５Ｐａ・ｓｅｃ、固形分濃度が３０．８質量％、含水率が０．３３質量％の溶液であった。このポリアミック酸溶液組成物の溶液安定性は○であった。
このポリアミック酸溶液組成物を、基材のガラス板上にバーコーターによって塗布し、その塗膜を、減圧下２５℃で３０分間、脱泡及び予備乾燥した後で、常圧下、窒素ガス雰囲気下に熱風乾燥器に入れて、１２０℃で６０分間、１５０℃で３０分間、２００℃で１０分間、２５０℃で１０分間、次いで３５０℃で１０分間加熱処理して、厚さが５０μｍのポリイミド膜を形成した。このポリイミド膜には発泡、割れ等は見られなかった。
このポリアミック酸溶液組成物及びポリイミドフィルムの特性等について結果を表１に示した。
[Example 1]
In a 1 L separable flask equipped with a stirrer, a stirring blade, a reflux condenser, and a nitrogen gas introduction tube, NMP 670.00 g, water 3.67 g, s-BPDA 79.80 g, and ODA 24.44 g (molar ratio of water [water / The acid component] is 3/4, the water content is 0.47% by mass, and the molar ratio of the acid component [acid component / diamine component] is 2/1) and stirred at a reaction temperature of 70 ° C. for 3 hours. And reacted. Next, 97.77 g of ODA and 8.28 g of 2,4-TDA were dissolved in this reaction solution, and 119.70 g of s-BPDA was further added, and the mixture was reacted at a reaction temperature of 50 ° C. with stirring for 20 hours.
The obtained reaction solution was a solution having a logarithmic viscosity of 0.24, a solution viscosity of 8.5 Pa · sec, a solid content concentration of 30.8% by mass, and a water content of 0.33% by mass. The solution stability of this polyamic acid solution composition was good.
This polyamic acid solution composition was applied onto a glass plate of a substrate by a bar coater, the coating film was defoamed and pre-dried at 25 ° C. for 30 minutes under reduced pressure, and then under normal pressure and nitrogen gas atmosphere. And heat treatment at 120 ° C. for 60 minutes, 150 ° C. for 30 minutes, 200 ° C. for 10 minutes, 250 ° C. for 10 minutes, then 350 ° C. for 10 minutes to give a polyimide film having a thickness of 50 μm Formed. No foaming or cracking was observed in this polyimide film.
The results of the properties of the polyamic acid solution composition and the polyimide film are shown in Table 1.
〔実施例２〕
撹拌機、撹拌羽根、還流冷却器、窒素ガス導入管を備えた１ＬのセパラブルフラスコにＮＭＰ８００ｇを加え、これにＯＤＡの６６．９１ｇと２，４−ＴＤＡ１０．２１ｇとｓ−ＢＰＤＡの１２２．８８ｇとを加え、５０℃で１０時間撹拌して、固形分濃度１８．０質量％、溶液粘度１９．５Ｐａ・ｓ、対数粘度０．９３のポリアミック酸溶液を得た。このポリアミック酸溶液組成物の溶液安定性は○であった。
このポリアミック酸溶液組成物を、基材のガラス板上にバーコーターによって塗布し、その塗膜を、減圧下２５℃で３０分間、脱泡及び予備乾燥した後で、常圧下、窒素ガス雰囲気下に熱風乾燥器に入れて、１２０℃で６０分間、１５０℃で３０分間、２００℃で１０分間、２５０℃で１０分間、次いで３５０℃で１０分間加熱処理して、厚さが５０μｍのポリイミド膜を形成した。このポリイミド膜には発泡、割れ等は見られなかった。
このポリアミック酸溶液組成物及びポリイミドフィルムの特性等について結果を表１に示した。
[Example 2]
800 g of NMP was added to a 1 L separable flask equipped with a stirrer, a stirring blade, a reflux condenser, and a nitrogen gas introduction tube, and 66.91 g of ODA, 10.21 g of 2,4-TDA and 122.88 g of s-BPDA. And stirred at 50 ° C. for 10 hours to obtain a polyamic acid solution having a solid content concentration of 18.0% by mass, a solution viscosity of 19.5 Pa · s, and a logarithmic viscosity of 0.93. The solution stability of this polyamic acid solution composition was good.
This polyamic acid solution composition was applied onto a glass plate of a substrate by a bar coater, the coating film was defoamed and pre-dried at 25 ° C. for 30 minutes under reduced pressure, and then under normal pressure and nitrogen gas atmosphere. And heat treatment at 120 ° C. for 60 minutes, 150 ° C. for 30 minutes, 200 ° C. for 10 minutes, 250 ° C. for 10 minutes, then 350 ° C. for 10 minutes to give a polyimide film having a thickness of 50 μm Formed. No foaming or cracking was observed in this polyimide film.
The results of the properties of the polyamic acid solution composition and the polyimide film are shown in Table 1.
〔実施例３〕
撹拌機、撹拌羽根、還流冷却器、窒素ガス導入管を備えた１ＬのセパラブルフラスコにＮＭＰ６７０．００ｇ、水３．７３ｇ、ｓ−ＢＰＤＡ８１．１０ｇ、及びＯＤＡ２２．０８ｇ（水のモル比［水／酸成分］が３／４、水の含有率が０．４８質量％、酸成分のモル比［酸成分／ジアミン成分］が２／１）を秤取り、７０℃の反応温度で３時間撹拌して反応させた。次いで、この反応溶液へＯＤＡ８８．３２ｇと２，４−ＴＤＡ１６．８４ｇとを溶解させ、さらにｓ−ＢＰＤＡ１２１．６５ｇを添加して、反応温度５０℃で２０時間撹拌しながら反応させた。
得られた反応溶液は、対数粘度が０．２２、溶液粘度が９．４Ｐａ・ｓｅｃ、固形分濃度が３１．２質量％、含水率が０．４４質量％の溶液であった。このポリアミック酸溶液組成物の溶液安定性は○であった。
このポリアミック酸溶液組成物を、基材のガラス板上にバーコーターによって塗布し、その塗膜を、減圧下２５℃で３０分間、脱泡及び予備乾燥した後で、常圧下、窒素ガス雰囲気下に熱風乾燥器に入れて、１２０℃で６０分間、１５０℃で３０分間、２００℃で１０分間、２５０℃で１０分間、次いで３５０℃で１０分間加熱処理して、厚さが５０μｍのポリイミド膜を形成した。このポリイミド膜には発泡、割れ等は見られなかった。
このポリアミック酸溶液組成物及びポリイミドフィルムの特性等について結果を表１に示した。
Example 3
In a 1 L separable flask equipped with a stirrer, a stirring blade, a reflux condenser, and a nitrogen gas introduction tube, NMP 670.00 g, water 3.73 g, s-BPDA 81.10 g, and ODA 22.08 g (molar ratio of water [water / The acid component] is 3/4, the water content is 0.48% by mass, the molar ratio of the acid component [acid component / diamine component] is 2/1), and the mixture is stirred at a reaction temperature of 70 ° C. for 3 hours. And reacted. Next, 88.32 g of ODA and 16.84 g of 2,4-TDA were dissolved in this reaction solution, 121.65 g of s-BPDA was further added, and the mixture was reacted at a reaction temperature of 50 ° C. for 20 hours with stirring.
The obtained reaction solution was a solution having a logarithmic viscosity of 0.22, a solution viscosity of 9.4 Pa · sec, a solid content concentration of 31.2% by mass, and a water content of 0.44% by mass. The solution stability of this polyamic acid solution composition was good.
This polyamic acid solution composition was applied onto a glass plate of a substrate by a bar coater, the coating film was defoamed and pre-dried at 25 ° C. for 30 minutes under reduced pressure, and then under normal pressure and nitrogen gas atmosphere. And heat treatment at 120 ° C. for 60 minutes, 150 ° C. for 30 minutes, 200 ° C. for 10 minutes, 250 ° C. for 10 minutes, then 350 ° C. for 10 minutes to give a polyimide film having a thickness of 50 μm Formed. No foaming or cracking was observed in this polyimide film.
The results of the properties of the polyamic acid solution composition and the polyimide film are shown in Table 1.
〔実施例４〕
撹拌機、撹拌羽根、還流冷却器、窒素ガス導入管を備えた１ＬのセパラブルフラスコにＮＭＰ６７０．００ｇ、水３．７９ｇ、ｓ−ＢＰＤＡ８２．４５ｇ、及びＯＤＡ１９．６４ｇ（水のモル比［水／酸成分］が３／４、水の含有率が０．４９質量％、酸成分のモル比［酸成分／ジアミン成分］が２／１）を秤取り、７０℃の反応温度で３時間撹拌して反応させた。次いで、この反応溶液へＯＤＡ７８．５６ｇと２，４−ＴＤＡ２５．６８ｇとを溶解させ、さらにｓ−ＢＰＤＡ１２３．６７ｇを添加して、反応温度５０℃で２０時間撹拌しながら反応させた。
得られた反応溶液は、対数粘度が０．２２、溶液粘度が７．６Ｐａ・ｓｅｃ、固形分濃度が３１．３質量％、含水率が０．３５質量％の溶液であった。このポリアミック酸溶液組成物の溶液安定性は○であった。
このポリアミック酸溶液組成物を、基材のガラス板上にバーコーターによって塗布し、その塗膜を、減圧下２５℃で３０分間、脱泡及び予備乾燥した後で、常圧下、窒素ガス雰囲気下に熱風乾燥器に入れて、１２０℃で６０分間、１５０℃で３０分間、２００℃で１０分間、２５０℃で１０分間、次いで３５０℃で１０分間加熱処理して、厚さが５０μｍのポリイミド膜を形成した。このポリイミド膜には発泡、割れ等は見られなかった。
このポリアミック酸溶液組成物及びポリイミドフィルムの特性等について結果を表１に示した。
Example 4
In a 1 L separable flask equipped with a stirrer, a stirring blade, a reflux condenser, and a nitrogen gas introduction tube, NMP 670.00 g, water 3.79 g, s-BPDA 82.45 g, and ODA 19.64 g (water molar ratio [water / The acid component] is 3/4, the water content is 0.49% by mass, the molar ratio of the acid component [acid component / diamine component] is 2/1), and stirred at a reaction temperature of 70 ° C. for 3 hours. And reacted. Next, ODA 78.56 g and 2,4-TDA 25.68 g were dissolved in this reaction solution, s-BPDA 123.67 g was further added, and the reaction was carried out with stirring at a reaction temperature of 50 ° C. for 20 hours.
The obtained reaction solution was a solution having a logarithmic viscosity of 0.22, a solution viscosity of 7.6 Pa · sec, a solid content concentration of 31.3 mass%, and a water content of 0.35 mass%. The solution stability of this polyamic acid solution composition was good.
This polyamic acid solution composition was applied onto a glass plate of a substrate by a bar coater, the coating film was defoamed and pre-dried at 25 ° C. for 30 minutes under reduced pressure, and then under normal pressure and nitrogen gas atmosphere. And heat treatment at 120 ° C. for 60 minutes, 150 ° C. for 30 minutes, 200 ° C. for 10 minutes, 250 ° C. for 10 minutes, then 350 ° C. for 10 minutes to give a polyimide film having a thickness of 50 μm Formed. No foaming or cracking was observed in this polyimide film.
The results of the properties of the polyamic acid solution composition and the polyimide film are shown in Table 1.
〔実施例５〕
撹拌機、撹拌羽根、還流冷却器、窒素ガス導入管を備えた１ＬのセパラブルフラスコにＮＭＰ６００．００ｇ、水６．１２ｇ、ｓ−ＢＰＤＡ１２４．９２ｇ、及びＯＤＡ２３．８１ｇ（水のモル比［水／酸成分］が４／５、水の含有率が０．７４質量％、酸成分のモル比［酸成分／ジアミン成分］が５／２）を秤取り、７０℃の反応温度で５時間撹拌して反応させた。次いで、この反応溶液へＯＤＡ９５．２３ｇと２，４−ＴＤＡ３１．１２ｇとを溶解させ、さらにｓ−ＢＰＤＡ１２４．９２ｇを添加して、反応温度５０℃で２０時間撹拌しながら反応させた。
得られた反応溶液は、対数粘度が０．１７、溶液粘度が５０．０Ｐａ・ｓｅｃ、固形分濃度が３８．４質量％、含水率が０．３６質量％の溶液であった。このポリアミック酸溶液組成物の溶液安定性は○であった。
このポリアミック酸溶液組成物を、基材のガラス板上にバーコーターによって塗布し、その塗膜を、減圧下２５℃で３０分間、脱泡及び予備乾燥した後で、常圧下、窒素ガス雰囲気下に熱風乾燥器に入れて、１２０℃で６０分間、１５０℃で３０分間、２００℃で１０分間、２５０℃で１０分間、次いで３５０℃で１０分間加熱処理して、厚さが５０μｍのポリイミド膜を形成した。このポリイミド膜には発泡、割れ等は見られなかった。
このポリアミック酸溶液組成物及びポリイミドフィルムの特性等について結果を表１に示した。
Example 5
In a 1 L separable flask equipped with a stirrer, a stirring blade, a reflux condenser, and a nitrogen gas introduction tube, NMP 600.00 g, water 6.12 g, s-BPDA 124.92 g, and ODA 23.81 g (molar ratio of water [water / The acid component] is 4/5, the water content is 0.74 mass%, the molar ratio of the acid component [acid component / diamine component] is 5/2), and the mixture is stirred at a reaction temperature of 70 ° C. for 5 hours. And reacted. Next, 95.23 g of ODA and 31.12 g of 2,4-TDA were dissolved in this reaction solution, 124.92 g of s-BPDA was further added, and the mixture was reacted at a reaction temperature of 50 ° C. with stirring for 20 hours.
The obtained reaction solution had a logarithmic viscosity of 0.17, a solution viscosity of 50.0 Pa · sec, a solid content concentration of 38.4% by mass, and a water content of 0.36% by mass. The solution stability of this polyamic acid solution composition was good.
This polyamic acid solution composition was applied onto a glass plate of a substrate by a bar coater, the coating film was defoamed and pre-dried at 25 ° C. for 30 minutes under reduced pressure, and then under normal pressure and nitrogen gas atmosphere. And heat treatment at 120 ° C. for 60 minutes, 150 ° C. for 30 minutes, 200 ° C. for 10 minutes, 250 ° C. for 10 minutes, then 350 ° C. for 10 minutes to give a polyimide film having a thickness of 50 μm Formed. No foaming or cracking was observed in this polyimide film.
The results of the properties of the polyamic acid solution composition and the polyimide film are shown in Table 1.
〔実施例６〕
実施例５で得られたポリアミック酸溶液組成物を、基材のガラス板上にバーコーターによって塗布し、その塗膜を、減圧下２５℃で３０分間、脱泡及び予備乾燥した後で、常圧下、窒素ガス雰囲気下に熱風乾燥器に入れて、１２０℃で６０分間、１５０℃で３０分間、２００℃で１０分間、２５０℃で１０分間、次いで３５０℃で１０分間加熱処理して、厚さが８０μｍのポリイミド膜を形成した。このポリイミド膜には発泡、割れ等は見られなかった。
このポリアミック酸溶液組成物及びポリイミドフィルムの特性等について結果を表１に示した。
Example 6
After the polyamic acid solution composition obtained in Example 5 was applied onto a glass plate of a substrate by a bar coater, the coating film was defoamed and pre-dried at 25 ° C. under reduced pressure for 30 minutes. In a hot air dryer under pressure and nitrogen gas atmosphere, heat treatment is performed at 120 ° C. for 60 minutes, 150 ° C. for 30 minutes, 200 ° C. for 10 minutes, 250 ° C. for 10 minutes, then 350 ° C. for 10 minutes. A polyimide film having a thickness of 80 μm was formed. No foaming or cracking was observed in this polyimide film.
The results of the properties of the polyamic acid solution composition and the polyimide film are shown in Table 1.
〔実施例７〕
撹拌機、撹拌羽根、還流冷却器、窒素ガス導入管を備えた１ＬのセパラブルフラスコにＮＭＰ６７０．００ｇ、水３．９２ｇ、ｓ−ＢＰＤＡ８５．２７ｇ、及びＯＤＡ１４．５１ｇ（水のモル比［水／酸成分］が３／４、水の含有率が０．５１質量％、酸成分のモル比［酸成分／ジアミン成分］が２／１）を秤取り、７０℃の反応温度で３時間撹拌して反応させた。次いで、この反応溶液へＯＤＡ５８．０４ｇと２，４−ＴＤＡ４４．２６ｇとを溶解させ、さらにｓ−ＢＰＤＡ１２７．９１ｇを添加して、反応温度５０℃で２０時間撹拌しながら反応させた。
得られた反応溶液は、対数粘度が０．２１、溶液粘度が７．８Ｐａ・ｓｅｃ、固形分濃度が３１．０質量％、含水率が０．２６質量％の溶液であった。このポリアミック酸溶液組成物の溶液安定性は○であった。
このポリアミック酸溶液組成物を、基材のガラス板上にバーコーターによって塗布し、その塗膜を、減圧下２５℃で３０分間、脱泡及び予備乾燥した後で、常圧下、窒素ガス雰囲気下に熱風乾燥器に入れて、１２０℃で６０分間、１５０℃で３０分間、２００℃で１０分間、２５０℃で１０分間、次いで３５０℃で１０分間加熱処理して、厚さが５０μｍのポリイミド膜を形成した。このポリイミド膜には発泡、割れ等は見られなかった。
このポリアミック酸溶液組成物及びポリイミドフィルムの特性等について結果を表１に示した。
Example 7
In a 1 L separable flask equipped with a stirrer, a stirring blade, a reflux condenser and a nitrogen gas introduction tube, NMP 670.00 g, water 3.92 g, s-BPDA 85.27 g, and ODA 14.51 g (molar ratio of water [water / The acid component] is 3/4, the water content is 0.51% by mass, the molar ratio of the acid component [acid component / diamine component] is 2/1), and the mixture is stirred at a reaction temperature of 70 ° C. for 3 hours. And reacted. Next, 58.04 g of ODA and 44.26 g of 2,4-TDA were dissolved in this reaction solution, 127.91 g of s-BPDA was further added, and the mixture was allowed to react with stirring at a reaction temperature of 50 ° C. for 20 hours.
The obtained reaction solution had a logarithmic viscosity of 0.21, a solution viscosity of 7.8 Pa · sec, a solid content concentration of 31.0% by mass, and a water content of 0.26% by mass. The solution stability of this polyamic acid solution composition was good.
This polyamic acid solution composition was applied onto a glass plate of a substrate by a bar coater, the coating film was defoamed and pre-dried at 25 ° C. for 30 minutes under reduced pressure, and then under normal pressure and nitrogen gas atmosphere. And heat treatment at 120 ° C. for 60 minutes, 150 ° C. for 30 minutes, 200 ° C. for 10 minutes, 250 ° C. for 10 minutes, then 350 ° C. for 10 minutes to give a polyimide film having a thickness of 50 μm Formed. No foaming or cracking was observed in this polyimide film.
The results of the properties of the polyamic acid solution composition and the polyimide film are shown in Table 1.
〔参考例１〕
撹拌機、撹拌羽根、還流冷却器、窒素ガス導入管を備えた１ＬのセパラブルフラスコにＮＭＰ８００ｇを加え、これにＯＤＡの８１．００ｇとｓ−ＢＰＤＡの１１９．００ｇとを加え、５０℃で１０時間撹拌して、固形分濃度１８．３質量％、溶液粘度５．１Ｐａ・ｓ、対数粘度０．７３のポリアミック酸溶液を得た。このポリアミック酸溶液組成物の溶液安定性は○であった。
このポリアミック酸溶液組成物を、基材のガラス板上にバーコーターによって塗布し、その塗膜を、減圧下２５℃で３０分間、脱泡及び予備乾燥した後で、常圧下、窒素ガス雰囲気下に熱風乾燥器に入れて、１２０℃で６０分間、１５０℃で３０分間、２００℃で１０分間、２５０℃で１０分間、次いで３５０℃で１０分間加熱処理して、厚さが５０μｍのポリイミド膜を形成した。このポリイミド膜には発泡、割れ等は見られなかった。
このポリアミック酸溶液組成物及びポリイミドフィルムの特性等について結果を表１に示した。
[Reference Example 1]
800 g of NMP was added to a 1 L separable flask equipped with a stirrer, stirring blade, reflux condenser, and nitrogen gas introduction tube, and 81.00 g of ODA and 119.00 g of s-BPDA were added thereto. The mixture was stirred for a time to obtain a polyamic acid solution having a solid content concentration of 18.3% by mass, a solution viscosity of 5.1 Pa · s, and a logarithmic viscosity of 0.73. The solution stability of this polyamic acid solution composition was good.
This polyamic acid solution composition was applied onto a glass plate of a substrate by a bar coater, the coating film was defoamed and pre-dried at 25 ° C. for 30 minutes under reduced pressure, and then under normal pressure and nitrogen gas atmosphere. And heat treatment at 120 ° C. for 60 minutes, 150 ° C. for 30 minutes, 200 ° C. for 10 minutes, 250 ° C. for 10 minutes, then 350 ° C. for 10 minutes to give a polyimide film having a thickness of 50 μm Formed. No foaming or cracking was observed in this polyimide film.
The results of the properties of the polyamic acid solution composition and the polyimide film are shown in Table 1.
〔参考例２〕
撹拌機、撹拌羽根、還流冷却器、窒素ガス導入管を備えた１ＬのセパラブルフラスコにＮＭＰ６７０．００ｇ、水３．６１ｇ、ｓ−ＢＰＤＡ７８．５４ｇ、及びＯＤＡ２６．７３ｇ（水のモル比［水／酸成分］が３／４、水の含有率が０．４６質量％、酸成分のモル比［酸成分／ジアミン成分］が２／１）を秤取り、７０℃の反応温度で３時間撹拌して反応させた。次いで、この反応溶液へＯＤＡ１０６．９２ｇを溶解させ、さらにｓ−ＢＰＤＡ１１７．８１ｇを添加して、反応温度５０℃で２０時間撹拌しながら反応させた。
得られた反応溶液は、対数粘度が０．２４、溶液粘度が８．９Ｐａ・ｓｅｃ、固形分濃度が３１．０質量％、含水率が０．３２質量％の溶液であった。このポリアミック酸溶液組成物の溶液安定性は○であった。
このポリアミック酸溶液組成物を、基材のガラス板上にバーコーターによって塗布し、その塗膜を、減圧下２５℃で３０分間、脱泡及び予備乾燥した後で、常圧下、窒素ガス雰囲気下に熱風乾燥器に入れて、１２０℃で６０分間、１５０℃で３０分間、２００℃で１０分間、２５０℃で１０分間、次いで３５０℃で１０分間加熱処理して、厚さが５０μｍのポリイミド膜を形成しようとしたが、ポリイミド膜の表面に割れが生じた。
このポリアミック酸溶液組成物の特性等について結果を表１に示した。
[Reference Example 2]
In a 1 L separable flask equipped with a stirrer, a stirring blade, a reflux condenser, and a nitrogen gas introduction tube, NMP 670.00 g, water 3.61 g, s-BPDA 78.54 g, and ODA 26.73 g (molar ratio of water [water / The acid component] is 3/4, the water content is 0.46% by mass, the molar ratio of the acid component [acid component / diamine component] is 2/1), and stirred at a reaction temperature of 70 ° C. for 3 hours. And reacted. Next, 106.92 g of ODA was dissolved in this reaction solution, 117.81 g of s-BPDA was further added, and the mixture was reacted at a reaction temperature of 50 ° C. with stirring for 20 hours.
The obtained reaction solution had a logarithmic viscosity of 0.24, a solution viscosity of 8.9 Pa · sec, a solid content concentration of 31.0% by mass, and a water content of 0.32% by mass. The solution stability of this polyamic acid solution composition was good.
This polyamic acid solution composition was applied onto a glass plate of a substrate by a bar coater, the coating film was defoamed and pre-dried at 25 ° C. for 30 minutes under reduced pressure, and then under normal pressure and nitrogen gas atmosphere. And heat treatment at 120 ° C. for 60 minutes, 150 ° C. for 30 minutes, 200 ° C. for 10 minutes, 250 ° C. for 10 minutes, then 350 ° C. for 10 minutes to give a polyimide film having a thickness of 50 μm However, cracks occurred on the surface of the polyimide film.
The results of the characteristics and the like of this polyamic acid solution composition are shown in Table 1.
〔参考例３〕
実施例４で得られたポリアミック酸溶液組成物を、基材のガラス板上にバーコーターによって塗布し、その塗膜を、減圧下２５℃で３０分間、脱泡及び予備乾燥した後で、常圧下、窒素ガス雰囲気下に熱風乾燥器に入れて、１２０℃で６０分間、１５０℃で３０分間、２００℃で１０分間、２５０℃で１０分間、次いで４００℃で１０分間加熱処理して、厚さが８０μｍのポリイミド膜を形成した。このポリイミド膜には発泡、割れ等は見られなかった。
このポリアミック酸溶液組成物及びポリイミドフィルムの特性等について結果を表１に示した。
[Reference Example 3]
After the polyamic acid solution composition obtained in Example 4 was applied onto a glass plate of a substrate by a bar coater, the coating film was defoamed and pre-dried at 25 ° C. under reduced pressure for 30 minutes. In a hot air dryer under pressure and nitrogen gas atmosphere, heat treatment is performed at 120 ° C. for 60 minutes, 150 ° C. for 30 minutes, 200 ° C. for 10 minutes, 250 ° C. for 10 minutes, and then at 400 ° C. for 10 minutes. A polyimide film having a thickness of 80 μm was formed. No foaming or cracking was observed in this polyimide film.
The results of the properties of the polyamic acid solution composition and the polyimide film are shown in Table 1.
〔参考例４〕
撹拌機、撹拌羽根、還流冷却器、窒素ガス導入管を備えた１ＬのセパラブルフラスコにＮＭＰ６７０．００ｇ、水４．０６ｇ、ｓ−ＢＰＤＡ８８．３０ｇ、及びＯＤＡ９．０２ｇ（水のモル比［水／酸成分］が３／４、水の含有率が０．５３質量％、酸成分のモル比［酸成分／ジアミン成分］が２／１）を秤取り、７０℃の反応温度で３時間撹拌して反応させた。次いで、この反応溶液へＯＤＡ３６．０６ｇと２，４−ＴＤＡ６４．１７ｇとを溶解させ、さらにｓ−ＢＰＤＡ１３２．４５ｇを添加して、反応温度５０℃で２０時間撹拌しながら反応させた。
得られた反応溶液は、対数粘度が０．２０、溶液粘度が７．１Ｐａ・ｓｅｃ、固形分濃度が３１．０質量％、含水率が０．３２質量％の溶液であった。このポリアミック酸溶液組成物の溶液安定性は○であった。
このポリアミック酸溶液組成物を、基材のガラス板上にバーコーターによって塗布し、その塗膜を、減圧下２５℃で３０分間、脱泡及び予備乾燥した後で、常圧下、窒素ガス雰囲気下に熱風乾燥器に入れて、１２０℃で６０分間、１５０℃で３０分間、２００℃で１０分間、２５０℃で１０分間、次いで３５０℃で１０分間加熱処理して、厚さが５０μｍのポリイミド膜を形成した。このポリイミド膜には発泡、割れ等は見られなかった。
このポリアミック酸溶液組成物及びポリイミドフィルムの特性等について結果を表１に示した。
[Reference Example 4]
In a 1 L separable flask equipped with a stirrer, a stirring blade, a reflux condenser, and a nitrogen gas introduction tube, NMP 670.00 g, water 4.06 g, s-BPDA 88.30 g, and ODA 9.02 g (molar ratio of water [water / The acid component] is 3/4, the water content is 0.53% by mass, the molar ratio of the acid component [acid component / diamine component] is 2/1), and stirred at a reaction temperature of 70 ° C. for 3 hours. And reacted. Next, 36.06 g of ODA and 64.17 g of 2,4-TDA were dissolved in this reaction solution, 132.45 g of s-BPDA was further added, and the mixture was reacted at a reaction temperature of 50 ° C. with stirring for 20 hours.
The obtained reaction solution had a logarithmic viscosity of 0.20, a solution viscosity of 7.1 Pa · sec, a solid content concentration of 31.0% by mass, and a water content of 0.32% by mass. The solution stability of this polyamic acid solution composition was good.
This polyamic acid solution composition was applied onto a glass plate of a substrate by a bar coater, the coating film was defoamed and pre-dried at 25 ° C. for 30 minutes under reduced pressure, and then under normal pressure and nitrogen gas atmosphere. And heat treatment at 120 ° C. for 60 minutes, 150 ° C. for 30 minutes, 200 ° C. for 10 minutes, 250 ° C. for 10 minutes, then 350 ° C. for 10 minutes to give a polyimide film having a thickness of 50 μm Formed. No foaming or cracking was observed in this polyimide film.
The results of the properties of the polyamic acid solution composition and the polyimide film are shown in Table 1.
本願発明によって、中間転写ベルトとして好適な３，３’，４，４’−ビフェニルテトラカルボン酸二無水物と４，４’−ジアミノジフェニルエーテルからなるポリアミック酸溶液組成を用いて得られるポリイミド膜と同等乃至それ以上の優れた機械的特性を有し、保存安定性が優れ、且つ高濃度且つ低粘度のアミック酸オリゴマー溶液組成を基材に塗布して膜状物に成形し次いで加熱処理してポリイミド膜を得る場合でも、加熱処理時に膜にひび割れを発生することなしにポリイミド膜を好適に得ることができる、特定の化学構造からなるポリイミド前駆体（ポリアミック酸及び／又はアミック酸オリゴマー）溶液組成物を提供することができる。 Equivalent to a polyimide film obtained by using a polyamic acid solution composition comprising 3,3 ′, 4,4′-biphenyltetracarboxylic dianhydride and 4,4′-diaminodiphenyl ether suitable as an intermediate transfer belt according to the present invention A polyimide having an excellent mechanical property, excellent storage stability, a high-concentration and low-viscosity amic acid oligomer solution composition applied to a substrate, formed into a film-like material, and then heat-treated. Even when a film is obtained, a polyimide precursor (polyamic acid and / or amic acid oligomer) solution composition having a specific chemical structure, which can suitably obtain a polyimide film without causing cracks in the film during heat treatment Can be provided.
このポリイミド前駆体溶液組成物は、対数粘度が大きな（高分子量の）ポリアミック酸からなる場合でも対数粘度が小さい（低分子量化した）アミック酸オリゴマーからなる場合でも、最高加熱処理温度が２８０〜３９０℃の温度範囲で加熱処理することによって、中間転写ベルトとして好適な無端管状ポリイミド膜などのポリイミド膜を好適に製造することができる。 This polyimide precursor solution composition has a maximum heat treatment temperature of 280 to 390 regardless of whether it is made of a polyamic acid having a large logarithmic viscosity (high molecular weight) or an amic acid oligomer having a low logarithmic viscosity (lower molecular weight). By performing the heat treatment in a temperature range of ° C., a polyimide film such as an endless tubular polyimide film suitable as an intermediate transfer belt can be suitably produced.
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| WO2012081644A1 (en) | 2010-12-15 | 2012-06-21 | 宇部興産株式会社 | Polyimide seamless belt and process for production thereof, and polyimide precursor solution composition |
| JP2014040503A (en) * | 2012-08-21 | 2014-03-06 | Tokyo Ohka Kogyo Co Ltd | Method of manufacturing polyimide resin, method of manufacturing polyimide film, method of manufacturing polyamic acid solution, polyimide film and polyamic acid solution |
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