JP4067417B2 - Electrophotographic photoreceptor - Google Patents
Electrophotographic photoreceptor Download PDFInfo
- Publication number
- JP4067417B2 JP4067417B2 JP2003030953A JP2003030953A JP4067417B2 JP 4067417 B2 JP4067417 B2 JP 4067417B2 JP 2003030953 A JP2003030953 A JP 2003030953A JP 2003030953 A JP2003030953 A JP 2003030953A JP 4067417 B2 JP4067417 B2 JP 4067417B2
- Authority
- JP
- Japan
- Prior art keywords
- polycarbonate resin
- molecular weight
- reaction
- methylene chloride
- average molecular
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 108091008695 photoreceptors Proteins 0.000 title claims description 36
- 239000004431 polycarbonate resin Substances 0.000 claims description 94
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 93
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- 239000011230 binding agent Substances 0.000 claims description 43
- 238000006243 chemical reaction Methods 0.000 claims description 42
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- 239000003054 catalyst Substances 0.000 claims description 27
- 150000001875 compounds Chemical class 0.000 claims description 27
- -1 nitrogen-containing heterocyclic compound Chemical class 0.000 claims description 17
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 10
- 150000003839 salts Chemical class 0.000 claims description 8
- 238000012695 Interfacial polymerization Methods 0.000 claims description 6
- 238000005227 gel permeation chromatography Methods 0.000 claims description 4
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- 230000000379 polymerizing effect Effects 0.000 claims description 2
- 239000010410 layer Substances 0.000 description 108
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 51
- 238000004519 manufacturing process Methods 0.000 description 44
- 239000000243 solution Substances 0.000 description 35
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Description
【0001】
【発明の属する技術分野】
本発明は、電子写真感光体に関し、詳しくは分子量分布の狭いポリカーボネート樹脂を感光層のバインダー樹脂として用いて形成された電子写真感光体に関する。
【0002】
【従来の技術】
電子写真技術は、即時性、高品質の画像が得られることなどから、近年では複写機の分野にとどまらず、各種プリンタ−の分野でも広く使われ、応用されてきている。電子写真技術の中核となる感光体については、その光導電材料として従来からのセレニウム、ヒ素−セレニウム合金、硫化カドミニウム、酸化亜鉛といった無機系の光導電体から、最近では、無公害で成膜が容易、製造が容易である等の利点を有する有機系の光導電材料を使用した感光体が主として利用されている。しかしながら、有機感光体は、アモルファスシリコン等の無機感光体に比べて寿命が短かく、更なる改良が求められている。
【0003】
電子写真感光体は、電子写真プロセスすなわち帯電、露光、現像、転写、クリーニング、除電等のサイクルで繰り返し使用されるためその間様々なストレスを受け劣化する。このような劣化としては例えば、帯電器として普通用いられるコロナ帯電器から発生する強酸化性のオゾンやNOxが感光層に化学的なダメージを与えたり、像露光で生成したキャリアー(電流)が感光層内を流れることや、除電光、外部からの光によって感光層組成物が分解するなどによる化学的、電気的劣化がある。またこれとは別の劣化としてクリーニングブレード、磁気ブラシなどの摺擦や現像剤、紙との接触等による感光層表面の摩耗や傷の発生、膜の剥がれといった機械的劣化がある。特にこの様な感光層表面に生じる損傷はコピー画像上に現れやすく、直接画像品質を損うため感光体の寿命を制限する大きな要因となっている。また、感光層の摩耗が大きいと、すぐに膜厚が薄くなり十分な帯電を得ることが出来なくなって、寿命を短いものにしてしまう。すなわち高寿命の感光体を開発するためには電気的、化学的耐久性を高めると同時に機械的強度を高めることも必須条件である。
【0004】
有機系の光導電材料を使用した感光体としては、光導電性微粉末をバインダー樹脂中に分散させたいわゆる分散型感光体、電荷発生層及び電荷輸送層を積層した積層型感光体が知られている。また、積層型感光体では電荷発生層及び電荷輸送層を導電性基体上にこの順で積層した順積層型感光体と、電荷輸送層及び電荷発生層をこの順に積層した逆積層型感光体が知られている。積層型感光体は、それぞれ効率の高い電荷発生物質、及び電荷輸送物質を組み合わせることにより高感度な感光体が得られること、材料選択範囲が広く安全性の高い感光体が得られること、また塗布の生産性が高く比較的コスト面でも有利なことから感光体の主流として鋭意開発され実用化されている。
一般に順積層型感光体の場合に、電気的、化学的または機械的負荷を受けるのは、最外層にある電荷輸送層である。電荷輸送層は通常バインダー樹脂と電荷輸送物質からなっており、実質的に強度を決めるのはバインダー樹脂であるが、十分な機械強度を持たせるには至っておらず、より耐久性の高い有機感光体が望まれている。
感光体の電荷輸送層を形成するためのバインダー樹脂としては、ポリメチルメタクリレート、ポリスチレン、ポリ塩化ビニル等のビニル重合体、及びその共重合体、ポリカーボネート、ポリエステル、ポリスルホン、フェノキシ、エポキシ、シリコーン樹脂等の熱可塑性樹脂や種々の熱硬化性樹脂が用いられてきているが、なかでもポリカーボネート樹脂が比較的優れた性能を有しており、これまで種々のポリカーボネート樹脂が開発され実用に供されている(特許文献1〜4参照)。
しかし、従来のポリカーボネートを用いた有機感光体では機械的強度が充分でないため、摩耗が大きかったり傷が生じてしまったりするなどの欠点を有しているため、実用上は限られた印刷性能にとどまっているのが現状である。
【0005】
【特許文献1】
特開昭50−98332号公報
【特許文献2】
特開昭59−71057号公報
【特許文献3】
特開昭59−184251号公報
【特許文献4】
特開平5−21478号公報
【0006】
【発明が解決しようとする課題】
本発明の目的は、繰り返し使用において耐刷性、耐摩耗性、滑り性等の機械的性質に優れ、しかも電気特性の優れた電子写真感光体を提供することにある。
【0007】
【課題を解決するための手段】
そこで本発明者らは電子写真感光体の表面の耐摩耗性の改良について鋭意検討を行った結果、特定のポリカーボネート樹脂を感光層のバインダー樹脂として用ることにより、表面強度が著しく改善され耐久性に優れた電子写真感光体が得られることを見いだし本発明に到達した。
即ち本発明の要旨は、
導電性支持体上に、少なくとも感光層を有する電子写真感光体において、該感光層のバインダー樹脂が、カーボネート形成化合物とジヒドロキシ化合物とを反応させてオリゴマーを生成させ、このオリゴマーを触媒の存在下に重合させることにより製造されたポリカーボネート樹脂であって、該触媒として塩酸塩のpKa値として7以下の塩基性度を有する化合物の塩を用い、ポリカーボネート樹脂であり、該ポリカーボネート樹脂におけるゲルパーミエーションクマトグラフィーにより測定したポリスチレン換算の重量平均分子量(Mw)と数平均分子量(Mn)との比(Mw/Mn)が2.4以下であり、かつ下記式(I)で算出される粘度平均分子量(Mv)と分子末端数から算出される数平均分子量(Mn′)との比(Mv/Mn′)が1.4以下であるポリカーボネート樹脂であることを特徴とする電子写真感光体、
に存する。
【0008】
【数2】
ηsp/C=〔η〕×(1+0.28ηsp) 式(I)
〔η〕=1.23×10-4×Mv0.83
(式(I)中、ηspはポリカーボネート樹脂の塩化メチレン溶液について20℃で測定した比粘度であり、Cはこの塩化メチレン溶液の濃度である。塩化メチレン溶液としてはポリカーボネート樹脂の濃度0.6g/dlのものを用いる)
【0009】
【発明の実施の形態】
以下、本発明につき詳細に説明する。本発明におけるポリカーボネート樹脂は、カーボネート形成化合物とジヒドロキシ化合物とを反応させることによって製造される。典型的にはビスフェノールAで代表される2個のフェノール性水酸基を有する芳香族化合物(芳香族ジヒドロキシ化合物)とホスゲンとを反応させてオリゴマーを生成させ、このオリゴマーを末端封止剤の不存在下、かつピリジン塩酸塩又はキノリン塩酸塩のような触媒の存在下に重合させることにより、製造することができる
ここでカーボネート形成化合物とは、縮合反応、交換反応等の重合体生成反応によってポリカーボネート主鎖中にカーボネート結合[−O−CO−O−]を生成し得る化合物であり、具体的には、ホスゲン、炭酸ジエステル等が挙げられる。炭酸ジエステルとしては、例えばジメチルカーボネート、ジエチルカーボネート、ジフェニルカーボネート、ジトリルカーボネート等が挙げられる。
【0010】
またジヒドロキシ化合物としては、脂肪族ジヒドロキシ化合物、芳香族ジヒドロキシ化合物等が挙げられ、芳香族ジヒドロキシ化合物としては例えば、2個のフェノール性水酸基を有する芳香族化合物が挙げられる。
本発明に用いられるジヒドロキシ化合物として好ましいものを具体的に例示すると、ビスフェノールA、ヒドロキノン、レゾルシン、ジヒドロキシジフェノール、ビス(ヒドロキシフェニル)アルカン、ビス(ヒドロキシフェニル)シクロアルカン、ビス(ヒドロキシフェニル)スルフィド、ビス(ヒドロキシフェニル)エーテル、ビス(ヒドロキシフェニル)ケトン、ビス(ヒドロキシフェニル)スルホン、ビス(ヒドロキシフェニル)スルホキシド、ビス(ヒドロキシフェニル)ジアルキルベンゼン、及び核にアルキル又はハロゲン置換基をもったこれらの誘導体が挙げられる。これらのなかでも更に好ましいものとしては、2,2−ビス(4−ヒドロキシフェニル)プロパン、2,2−ビス(3,5−ジメチル−4−ヒドロキシフェニル)プロパン、1,1−ビス(4−ヒドロキシフェニル)シクロヘキサン、及び1,1−ビス(4−ヒドロキシフェニル)−3,3,5−トリメチルシクロヘキサンが挙げられる。
【0011】
なお、ジヒドロキシ化合物に、3個以上の官能基を有する分岐剤を少量併用することもできる。このような分岐剤は公知であり、例えば2,4−ビス(4′−ヒドロキシフェニル−イソプロピル)フェノール、2,6−ビス(2′−ヒドロキシ−5′−メチルベンジル)−4−メチルフェノール、2−(4−ヒドロキシフェニル)−2−(2,4−ジヒドロキシフェニル)プロパン、1,4−ビス(4,4′−ジヒドロキシトリフェニルメチル)ベンゼン、2,4−ジヒドロキシ安息香酸、トリメシン酸、塩化シアヌル、ビス(4′−ヒドロキシフェニル)−2−オキソ−2,3−ジヒドロキシインドール、3,3−ビス(4−ヒドロキシ−3−メチルフェニル)−2−オキソ−2,3−ジヒドロインドール等が挙げられる。中でも、3個またはそれ以上のフェノール性水酸基を持つものが好適である。分岐剤の使用量は、目的とする分岐度によっても異なるが、通常、2個のフェノール性水酸基を有する芳香族化合物に対し、0.05〜2モル%となるように使用される。なお、分岐剤を併用すると、粘度平均分子量(Mv)が増加し易いので注意を要する。
【0012】
次に、本発明に用いられる分子量分布の狭いポリカーボネートは、例えば、特開2002−69168に記載されている如く、触媒として塩酸塩のpKa値として7以下、好ましくは6以下、更に好ましくは5.5以下のものを用いることにより製造することが出来る。即ち塩基性度の弱い触媒を使用することでクロロフォーメート分子末端をイオン化させず、他方のイオン化した末端(フェニレン−ONa末端)のみから求核置換反応を優先して起こさせることができる。単一反応のみで進行する従来のポリカーボネート樹脂生成時の縮合重合と反応機構が異なるため、結果としてポアソン分布に従った分子量分布を有するポリカーボネートが得られる。
【0013】
さらに、本発明に関わるポリカーボネート樹脂の製造は、後述するように水相と有機相を存在させる界面重合反応が好ましい。この界面重合反応ではイオン化した末端のみからの求核置換反応で反応が進行するため、必然的に体積当たりの界面積に見合った成長しか生じ得ない逐次反応となるため、界面積が大きい程到達分子量も大きく、縮合種が無くなった段階でクロロフォーメート分子末端が水相中のNaOHにより加水分解を受け、OH末端として分子量伸長が停止する。体積当たりの界面積が小さい場合では、副反応として成長反応に対し分子末端であるクロロフォーメート末端が水相にあるNaOHによる加水分解反応を受けることとなり、結果的にそれ以上の分子量に成長し得ない状態、即ち界面積支配の分子量となる。この様な反応が成立する背景には、成長反応が加水分解反応に比較し非常に速い速度で進行することが挙げられる。
【0014】
従来の一般的なポリカーボネート樹脂生成の際に起きる縮合重合では、この様な反応のアンバランスはない。従来の縮合重合では、pKa値の高い触媒を使用し、クロロフォーメート末端もこのpKa値の高い触媒によりイオン様に活性化された状態となり、イオン化したフェニレン−ONa末端と殆ど遜色の無い反応活性を両分子末端に有することとなり、Floryの最確分布に従った一般的な分子量分布を有する縮合物が得られると同時に、一般に末端停止剤の存在しない場合には超高分子物となってしまう。
【0015】
上記条件を満たす触媒として、含窒素複素環化合物の塩が用いられる。例えばピリジン、キノリン、イソキノリン、ピコリン、アクリジン、ピラジン、ピリダジン、ピリミジン、2,4,6−トリメチルトリアジン等の、環の炭素原子にアルキル基、アルコキシ基、ハロゲン原子などが置換していてもよい不飽和な含窒素六員環を有する化合物の塩が用いられる。また、フェノチアジン、2−メチルイミダゾール、ベンゾイミダゾール、ベンゾトリアゾール、ベンゾチアゾール等のような不飽和な含窒素五員環を有する化合物の塩も用いられる。これらの含窒素複素環化合物のなかでも、ピリジン、キノリン、ピコリン、イミダゾール類、ピラゾール類、トリアゾール類などを用いるのが好ましい。これらの触媒は、原料の2個のフェノール性水酸基を有する芳香族化合物に対し、通常0.01〜1モル%となるように用いられる。好ましくは0.05〜0.5モル%、特に0.05〜0.15モル%となるように用いられる。これらの含窒素複素環化合物は、塩酸塩、硫酸塩、硝酸塩、臭化水素酸塩などの塩型で用いられるが、反応系内においては遊離塩基型と塩型との間で解離平衡の状態にあると考えられる。
【0016】
これらの触媒は、2個のフェノール性水酸基を有する芳香族化合物とホスゲンとの反応の当初から反応系に存在させてもよく、またこの反応の後で反応系に添加してもよい。しかしこの触媒の添加が遅れると、生成するポリカーボネート樹脂の分子量の制御が困難となる。従って触媒は、ホスゲンとの反応の当初から分子量の増大が始まるまでの間、粘度平均分子量(Mv)でいえば、Mvが2000〜3000に達するまでの間に反応系に添加するのが好ましい。
【0017】
一方、縮合触媒としては、二相界面重合法に用いられている公知のものを併用しても構わない。通常はトリアルキルアミン、N−エチルピロリドン、N−エチルピペリジン、N−エチルモルホリン、N−イソプロピルピペリジン、又はN−イソプロピルモルホリンなどを用いる。なかでもトリエチルアミン又はN−エチルピペリジンを用いるのが好ましい。縮合触媒はホスゲンを供給した後に反応系に供給するのが好ましい。反応は、2個のフェノール性水酸基を有する芳香族化合物と苛性ソーダとを水に溶解して調製した水溶液と、不活性有機溶媒とを混合して乳化液を調製し、これにホスゲンを供給して反応させオリゴマーを生成させる。水溶液中における2個のフェノール性水酸基を有する芳香族化合物と苛性ソーダとのモル比は通常1:1.8〜3.5であり、好ましくは1:2.0〜3.2である。水溶液中にはハイドロサルファイト等の還元剤を少量添加するのが好ましい。また、水相に対する有機相の比率は0.2〜1.0(容積比)が好ましい。不活性有機溶媒としては、反応条件下において、原料であるホスゲン、並びに反応で生成するオリゴマー及びポリカーボネート樹脂は溶解するが、水とは相互に溶解しないものを用いる。その使用量は生成するオリゴマーが溶解する量であればよいが、通常は生成するオリゴマー溶液の濃度が10〜40重量%となるように用いる。
【0018】
代表的な不活性有機溶媒としては、ヘキサン及びn−ヘプタンのような脂肪族炭化水素、塩化メチレン、クロロホルム、四塩化炭素、ジクロロエタン、トリクロロエタン、テトラクロロエタン、ジクロロプロパン及び1,2−ジクロロエチレンのような塩素化脂肪族炭化水素、ベンゼン、トルエン及びキシレンのような芳香族炭化水素、クロロベンゼン、o−ジクロロベンゼン及びクロロトルエンのような塩素化芳香族炭化水素、その他ニトロベンゼン及びアセトフェノンのような置換芳香族炭化水素などが挙げられる。中でも、塩素化された炭化水素、例えば塩化メチレンまたはクロロベンゼンが好適に使用される。 これらの不活性有機溶媒は、単独又は他の溶媒との混合物として、使用することができる。 オリゴマー生成反応は80℃以下、好ましくは70℃以下で行われる。反応温度が高過ぎると、副反応が増大してホスゲン原単位が悪化する。逆に反応温度が低いことは反応制御上有利であるが、反応は大きな発熱反応なので、反応系の温度が低いほどこの温度を維持するための費用が増加する。従って、これらの点を考慮して通常は10〜65℃で反応を行わせる。
【0019】
上記により生成させたオリゴマーは、次いで重合させてポリカーボネート樹脂とする。通常は上記のオリゴマー生成工程で得られた反応混合液を、水相とオリゴマーが溶解している有機相とに分離し、この有機相のオリゴマー濃度が5〜30重量%となるように、必要に応じて不活性有機溶媒を追加する。次いでこのオリゴマー溶液に新たに苛性ソーダ水溶液を加え、更に前述の触媒を添加して界面重合させる。この際の有機相に対する水相の比率は0.2〜2.0(容積比)であるのが好ましい。界面重合反応の温度は用いる有機溶媒により異なるが、塩化メチレンの場合には通常10〜35℃で行われる。
【0020】
重合終了後は、有機相をポリカーボネート樹脂のクロロホーメート基の含有量が0.1μeq/g以下になるまで苛性ソーダ水溶液で洗浄し、次いで酸水溶液で洗浄してアルカリを中和すると共に触媒を除去し、更に水洗して電解質を完全に除去する。最後に有機相から有機溶媒を蒸発させて除去し、ポリカーボネート樹脂を取得する。このポリカーボネート樹脂は、界面重縮合反応により生成したままの状態で、すなわち分別沈澱や低分子量成分の抽出除去などの分子量分布を調整する処理を行わなくても、極めて狭い分子量分布を有する。
【0021】
上記の方法により得られたポリカーボネート樹脂は、オリゴマーの生成反応及びオリゴマーからポリカーボネート樹脂への重合反応のいずれの段階においても、末端封止剤を用いないで反応を行わせるので、分子末端は水酸基である。もし分子末端が長鎖アルキル基などで封止されたポリカーボネート樹脂を所望の場合には、上記で得られたポリカーボネート樹脂に長鎖アルコールや長鎖カルボン酸又はこれらの反応性誘導体を反応させることにより、所望の程度に末端が封止されたポリカーボネート樹脂とすることができる。
【0022】
本発明におけるポリカーボネート樹脂は上記の方法により製造することができ、ゲルパーミエーションクロマトグラフィーにより測定したポリスチレン換算の重量平均分子量(Mw)と数平均分子量(Mn)との比(Mw/Mn)が2.4以下であり、かつ下記式(I)で算出される粘度平均分子量(Mv)と分子末端数から算出される数平均分子量(Mn′)との比(Mv/Mn′)が1.4以下である。
【0023】
【数3】
ηsp/C=〔η〕×(1+0.28ηsp) 式(I)
〔η〕=1.23×10-4×Mv0.83
(式中、ηspはポリカーボネート樹脂の塩化メチレン溶液について20℃で測定した比粘度であり、Cはこの塩化メチレン溶液の濃度である。塩化メチレン溶液としてはポリカーボネート樹脂の濃度0.6g/dlのものを用いる)
【0024】
本発明における好ましいポリカーボネート樹脂は、Mw/Mnが2.4以下、特に2.0以下である。またMv/Mn′は1.3以下、特に1.2以下であるのが好ましい。Mw/Mn及びMv/Mn′はいずれも分子量分布の幅を表わす指標であり、これらが小さいことは分子量分布が狭いことを意味する。従来からも分子量分布の狭いポリカーボネート樹脂の製法の提案はあるが、これらの従来の製法によって得られる物は、ガラス転移点から算出されるMw/Mnから、その値が2を遙かに越えて3に近い値となるので、本発明で使用するポリカーボネート樹脂はこれとは異なり、著しく狭い分子量分布を有している。
【0025】
Mvは、好ましくは5,000〜200,000であり、より好ましくは10,000〜150,000であり、最も好ましくは20,000〜100,000である。Mvが5,000未満であると強度が不十分で実用的でなく、200,000を超えると適当な膜厚に塗布することが困難である。
【0026】
<導電性支持体>
本発明の電子写真感光体は、導電性支持体上に感光層を形成して構成される。感光層が形成される導電性支持体としては周知の電子写真感光体に採用されているものがいずれも使用できる。具体的には例えばアルミニウム、ステンレス鋼、銅、ニッケル、亜鉛、インジウム、金、銀等の金属材料からなるドラム、シートあるいはこれらの金属箔のラミネート物、蒸着物、あるいは表面にアルミニウム、銅、パラジウム、酸化すず、酸化インジウム、導電性高分子等の導電性層を設けたポリエステルフィルム、紙、ガラス等の絶縁性支持体が挙げられる。更に、金属粉末、カーボンブラック、ヨウ化銅、高分子電解質等の導電性物質を適当なバインダーとともに塗布して導電処理したプラスチックフィルム、プラスチックドラム、紙、紙管等が挙げられる。また、金属粉末、カーボンブラック、炭素繊維等の導電性物質を含有し、導電性となったプラスチックのシートやドラムが挙げられる。又、酸化スズ、酸化インジウム等の導電性金属酸化物で導電処理したプラスチックフィルムやベルトが挙げられる。このように導電性支持体の表面は、画質に影響のない範囲で各種の処理、例えば、表面の酸化処理や薬品処理を行うことができる。形状はドラム、シート、ベルト、シームレスベルト等の任意の形状を取ることができる。
【0027】
<ブロツキング層>
導電性支持体と感光層との間には通常使用されるような公知のブロッキング層が設けられていてもよい。ブロッキング層としては、例えばアルミニウムの陽極酸化被膜、酸化アルミニウム、水酸化アルミニウム等の無機層、ポリビニルアルコール、カゼイン、ポリビニルピロリドン、ポリアクリル酸、セルロース類、ゼラチン、デンプン、ポリウレタン、ポリイミド、ポリアミドなどの有機層が使用される。有機層をブロッキング層として用いる場合には単独あるいはチタニア、アルミナ、シリカ、酸化ジルコニウム等の金属酸化物あるいは銅、銀、アルミニウム等の金属微粉末を分散させて用いてもよい。
【0028】
これらのブロッキング層の膜厚は適宜設定できるが、通常、0.05〜20μm、好ましくは0.1〜10μmの範囲である。
<感光層の構成>
感光層は、いわゆる積層型の感光層、あるいは分散型の感光層のいずれの形態も用いることができるが、感光体の機械的物性、電気特性、製造安定性など総合的に勘案して、順積層型の感光体が好ましい。
【0029】
<電荷発生物質>
感光層に含有される電荷発生物質としては、酸化チタン等の酸化物系半導体、アモルファスシリコン等のシリコン系材料、その他の無機光導電物質、フタロシアニン、アゾ色素、キナクリドン、多環キノン、ピリリウム塩、ペリレン、インジゴ、チオインジゴ、アントアントロン、ピラントロン、シアニン等の各種有機顔料、色素が使用できる。中でも、ペリレン、無金属フタロシアニンや、銅、塩化インジウム、ガリウム、シリコン、錫、チタニウム、亜鉛、バナジウム等の金属、又はその酸化物、塩化物、水酸化物の配位したフタロシアニン類、あるいはモノアゾ、ビスアゾ、トリスアゾ、ポリアゾ類等のアゾ顔料が望ましい。
また、1回転目の帯電性の改良、光疲労の低減、感度の調整といった目的で2種類以上の電荷発生物質を混合して用いても良い。
【0030】
<電荷輸送物質>
本発明において、感光層に用いられる電荷輸送物質としては、ジフェノキノン誘導体、2,4,7−トリニトロフルオレノンなどの芳香族ニトロ化合物、カルバゾール誘導体、インドール誘導体、イミダゾール誘導体、オキサゾール誘導体、ピラゾール誘導体、オキサジアゾール誘導体、ピラゾリン誘導体、チアジアゾール誘導体などの複素環化合物、アニリン誘導体、ヒドラゾン化合物、芳香族アミン誘導体、スチルベン誘導体、ブタジエン誘導体、エナミン化合物、これらの化合物が複数結合されたもの、あるいはこれらの化合物からなる基を主鎖もしくは側鎖に有する重合体などが挙げられる。なお、上記電荷輸送材料は、2種類以上を混合して使用しても良い。
【0031】
<分散型感光層>
本発明の電子写真感光体が分散型の感光層を有する場合は、電荷発生物質は電荷輸送物質と共に、本発明のポリカーボネート樹脂を含有する層中に分散または溶解して用いられる。
この際、電荷発生物質の粒子径は充分小さいことが必要であり、好ましくは1μm以下、より好ましくは、0.5μm以下で使用される。
感光層内に分散または溶解される電荷発生物質の量は、例えば0.5〜50重量%の範囲であるが、少なすぎると充分な感度が得られず、多すぎると帯電性の低下、感度の低下などの弊害があり、より好ましくは1〜20重量%の範囲で使用される。
さらに、感光層には、必要に応じて酸化防止剤、電子吸引性化合物、レベリング剤、滑剤、紫外線吸収剤、増感剤等の各種添加剤を含んでいてもよい。
またこの他に、塗膜の機械的強度や、耐久性向上のための種々の添加剤を用いることもできる。この様な添加剤としては、周知の可塑剤や、種々の安定剤、流動性付与剤、架橋剤等が挙げられる。
得られる塗布液を導電性支持体上に塗布、乾燥し、感光層を形成するが、通常、数μm〜数十μm、好ましくは10〜45μm、さらに好ましくは20〜35μmで用いられる。
【0032】
<積層型感光層>
i)電荷発生層
本発明の電子写真感光体が積層型感光層を持つ場合は、電荷発生物質は単独で、またはバインダー樹脂と共に用いられて、電荷発生層を形成する。
電荷発生物質をボールミル、超音波分散器、ペイントシェイカー、アトライター、サンドグラインダ等により適当な分散媒に分散、溶解し、必要に応じてバインダー樹脂を添加して塗布液を調整し、この塗布液をディッピング法、スプレー法、バーコーター法、ブレード法、ロールコーター法、ワイヤーバー塗工法、ナイフコーター塗工法、等の塗布法により塗布液、乾燥する。
【0033】
バインダー樹脂としては、例えばポリエステル樹脂、ポリビニルアセテート、ポリエステル、ポリカーボネート、ポリビニルアセトアセタール、ポリビニルプロピオナール、ポリビニルブチラール、フェノキシ樹脂、エポキシ樹脂、ウレタン樹脂、セルロースエステル、セルロースエーテル、スチレン、酢酸ビニル、塩化ビニル、アクリル酸エステル、メタクリル酸エステル、ビニルアルコール、エチルビニルエーテル等のビニル化合物の重合体および共重合体、ポリアミド、けい素樹脂等が挙げられる。この場合、電荷発生物質はバインダー樹脂100重量部に対して通常5〜500重量部であり、好ましくは20〜300重量部である。電荷発生層の膜厚は通常0.01〜5μm、好ましくは0.05〜2μm、より好ましくは0.15〜0.8μmである。また電荷発生層は必要に応じて塗布性を改善するためのレベリング剤や酸化防止剤、増感剤等の各種添加剤を含んでいてもよい。
電荷発生物質が単独で用いられる場合には、上記分散液にバインダーを添加せずに塗布液を調整し、塗布しても良いし、蒸着やスパッタリング等の方法で形成しても良い。
【0034】
ii)電荷輸送層
本発明の電子写真感光体が機能分離型の感光層を有する場合、電荷輸送物質は、本発明のポリカーボネート樹脂を含有するバインダー樹脂に混合されて、電荷輸送層を形成する。
電荷輸送物質およびバインダー樹脂の割合は、バインダー樹脂100重量部に対して、通常、電荷輸送物質が10〜200重量部、好ましくは30〜150重量部の範囲で使用される。
電荷輸送層の膜厚は、通常、10〜50μm、好ましくは13〜35μmの厚みで使用されるのがよい。
さらに、電荷輸送層には、必要に応じて酸化防止剤、電子吸引性化合物、レベリング剤、滑剤、紫外線吸収剤、増感剤等の各種添加剤並びに他の電荷輸送材料を含んでいてもよい。
またこの他に、塗膜の機械的強度や、耐久性向上のための種々の添加剤を用いることができる。この様な添加剤としては、周知の可塑剤や、種々の安定剤、流動性付与剤、架橋剤等が挙げられる。
【0035】
<感光層形成用塗布液>
上記各層を塗布する際に使用される溶媒、分散媒としては、ブチルアミン、ジエチルアミン、エチレンジアミン、イソプロパノールアミン、トリエタノールアミン、トリエチレンジアミン、N,N−ジメチルホルムアミド、アセトン、メチルエチルケトン、シクロヘキサノン、ベンゼン、トルエン、キシレン、クロロホルム、1,2−ジクロルエタン、1,2−ジクロルプロパン、1,1,2−トリクロルエタン、1,1,1−トリクロルエタン、トリクロルエチレン、テトラクロルエタン、ジクロルメタン、テトラヒドロフラン、ジオキサン、メチルアルコール、エチルアルコール、イソプロピルアルコール、酢酸エチル、酢酸ブチル、ジメチルスルホキシド、メチルセルソルブ、等が挙げられる。
これらの溶媒は、1種類単独で使用してもよく、或いは2種類以上を混合して用いても良い。
【0036】
<感光層形成方法>
感光層の塗布方法としては、スプレー塗布法、スパイラル塗布法、リング塗布法、浸漬塗布法等がある。
スプレー塗布法としては、エアスプレー、エアレススプレー、静電エアスプレー、静電エアレススプレー、回転霧化式静電スプレー、ホットスプレー、ホットエアレススプレー等があるが、均一な膜厚を得るための微粒化度、付着効率等を考えると回転霧化式静電スプレーにおいて、再公表平1−805198号公報に開示されている搬送方法、すなわち円筒状ワークを回転させながらその軸方向に間隔を開けることなく連続して搬送することにより、総合的に高い付着効率で膜厚の均一性に優れた電子写真感光体を得ることができる。
【0037】
スパイラル塗布法としては、特開昭52−119651号公報に開示されている注液塗布機またはカーテン塗布機を用いた方法、特開平1−231966号公報に開示されている微小開口部から塗料を筋状に連続して飛翔させる方法、特開平3−193161号公報に開示されているマルチノズル体を用いた方法等がある。
浸漬塗布法は、一例としては以下のような電荷輸送層の塗布形成手順が挙げられる。
電荷輸送物質、バインダー樹脂、溶剤等を用いて、全固形分濃度が15%以上であってより好ましくは40%以下の、かつ粘度が通常50センチポアーズ以上700センチポアーズ以下、好ましくは100センチポアーズ以上500センチポアーズ以下の電荷輸送層形成用の塗布液を調整する。
塗膜形成後塗膜を乾燥するが、必要且つ充分な乾燥が行われる様に乾燥温度、時間を調整する。乾燥温度は、通常100〜250℃、好ましくは、110〜170℃、さらに好ましくは、115〜140℃の範囲である。乾燥方法としては、熱風乾燥機、蒸気乾燥機、赤外線乾燥機及び遠赤外線乾燥機等を用いることができる。
このようにして得られた本発明の電子写真感光体は長期間にわたって優れた耐刷性と滑り性を維持し、複写機、プリンター、ファックス、製版機等の電子写真分野に好適である。
【0038】
【実施例】
以下、本発明を実施例により更に詳細に説明するが、本発明はその要旨を超えない限り、以下の実施例に限定されるものではない。なお、実施例及び比較例中で用いる「部」は特に断りがない限り「重量部」を示す。
<バインダー樹脂の作製>
製造例における評価方法は以下のとおりである。
(1)ゲルパーミエーションクロマトグラフィーの測定
装置;東ソー株式会社製品、HLC−8020
カラム;充填剤としてそれぞれTSK 5000HLX、4000HLX、3000HLX及び2000HLX(いずれも東ソー株式会社製品)を充填した4本のカラム(直径7.8mmφ、長さ300mm)を接続して用いた。
検出器;屈折率計
溶離液;テトラヒドロフラン
検量線;(株)ケムコ製の標準ポリスチレン(分子量;761(Mw/Mn≦1.14)、2000(Mw/Mn≦1.20)、4000(Mw/Mn≦1.06)、9000(Mw/Mn≦1.04)、17500(Mw/Mn≦1.03)、50000(Mw/Mn≦1.03)、233000(Mw/Mn≦1.05)、600000(Mw/Mn≦1.05)及び900000(Mw/Mn≦1.05)を用いて作成した。
操作;屈折率差により検出して得られたチャートより、Mw及びMnをポリスチレン換算で求め、Mw/Mnを算出した。この時のベースラインは、装置が完全に安定した状態で、高分子量の立ち上り前のベースをそのまま忠実に延長し、低分子側の元のベースラインに戻った地点とをつないで計算した。なお、上記の標準ポリスチレンを測定して全て規格内におさまっていることを確認した。
【0039】
(2)数平均分子量(Mn′)の測定
末端封止剤を用いないで製造したポリカーボネート樹脂の末端及び停止剤で停止されなかった残存末端は全てOH基である。この末端OH基は、酢酸酸性下で四塩化チタンにより発色させ、480nmの波長の吸光度を測定することにより末端基を定量した。数平均分子量(Mn′)は下記式(II)により算出した。
Mn′=106/(末端基数(μeq/g)×1/2) 式(II)
【0040】
また重合に際し末端封止剤を用いた場合には、末端封止剤は全て末端に結合しているものとして、上記の測定で得られた末端OH基数と封止剤の添加量から算出される封止末端基数との合計を末端基数とした。なお、予備実験により末端封止剤の存在下に重合したポリカーボネート樹脂をアルカリ加水分解して、結合している末端封止剤量を定量し、使用した末端封止剤が全て分子末端に結合していることを確認してある。
【0041】
(3)粘平均分子量(Mv)の測定
下記式(I)に基づいて求めた。
【0042】
【数4】
ηsp/C=〔η〕×(1+0.28ηsp) 式(I)
〔η〕=1.23×10-4×Mv0.83
式中、ηspはポリカーボネート樹脂の塩化メチレン溶液について20℃で測定した比粘度であり、Cはこの塩化メチレン溶液の濃度である。塩化メチレン溶液としてはポリカーボネート樹脂の濃度0.6g/dlのものを用いた。
【0043】
[製造例1]
ハイドロサルファイトが溶解している苛性ソーダ水溶液に2,2−ビス(4−ヒドロキシフェニル)プロパン(以下「ビスフェノールA」と記す)を35℃で溶解したのち25℃まで冷却した水溶液と、5℃に冷却した塩化メチレンとを、内径6mmのステンレススチール製のパイプに連続的に供給して混合し、混合液をホモミキサー(特殊機化社製品、T.KホモミックラインフローLF−500型)に通して乳化し、乳濁液を調製した。パイプへの供給量はビスフェノールA16.31kg/Hr、苛性ソーダ5.93kg/Hr、水101.1kg/Hr、ハイドロサルファイト0.018kg/Hr、及び塩化メチレン68.0kg/Hrである。生成した乳濁液を内径6mmのパイプを経て、内径6mm、長さ34mの PTFE(ポリテトラフルオロエチレン)製パイプリアクターに流入させた。パイプリアクターに同時に0℃に冷却した液化ホスゲンを7.5kg/Hrで供給して反応させ、オリゴマーを生成させた。パイプリアクターの流速は1.7m/秒である。ホスゲンとしては、直径55mm、高さ500mmの円筒形容器に下記の活性炭(太平化学社製 商品名:ヤシコールS)を充填したものに、−5℃に冷却したホスゲンをSV=3で通液させて精製したものを用いた。
【0044】
活性炭 ヤシコールS(太平化学社製品)の各種物性
真密度:2.1g/ml
空隙率:40%
比表面積:1200m2/g
細孔容積:0.86ml/g
【0045】
なおパイプリアクターでは温度は60℃まで上昇するが、外部冷却により出口では35℃であった。反応混合物は静置分離して水相と油相とに分離した。得られた油相から30kgを分取して、内容積200リットルのファウドラー翼付き反応槽に仕込んだ。
次いでこれに塩化メチレン16kg、水32kgを仕込み、窒素雰囲気下、攪拌しながら3℃迄冷却後、触媒としてピリジン塩酸塩をビスフェノールAに対して0.02モル%の割合で加え、また、25%苛性ソーダ水溶液4.15kgを加え60分間、400rpmの撹拌回転数で攪拌しながら重合反応を行い、ポリカーボネート樹脂を生成させた。このとき重合の内温は11℃まで上昇した。
【0046】
この反応混合液に末端停止剤として塩化ベンゾイルをビスフェノールAに対して3.04モル%と、停止剤と当量のカセイソーダを加え、同温度を維持したままで60分間攪拌反応した。反応混合液に塩化メチレン35kg及び水10kgを加え、室温で20分間撹拌したのち静置して、水相と有機相を分離した。有機相に0.1規定の塩酸28kgを加えて15分間撹拌したのち、静置して水相と有機相とを分離した。この有機相に、純水28kgを加えて15分間撹拌したのち静置して水相と油相とに分離する洗浄操作を3回反復した結果、水相中に塩素イオンが検出されなくなったので、洗浄操作を中止した。有機相からニーダーで塩化メチレンを蒸発させて除き、得られた粉末を乾燥してポリカーボネート樹脂を得た。重合条件、得られたポリカーボネート樹脂の物性を表1に示す。
【0047】
[製造例2]
製造例1において、重合反応時の攪拌回転数を420に代え、また、末端停止剤及び末端停止剤と同時に加えるカセイソーダの量をビスフェノールAに対して2.45モル%の代えた以外は実施例1と同様にポリカーボネート樹脂の製造を行った。得られたポリカーボネート樹脂の物性を表1に示す。
【0048】
[製造例3]
ハイドロサルファイトが溶解している苛性ソーダ水溶液に1,1−ビス(4−ヒドロキシフェニル)シクロヘキサン(以下「ビスフェノールZ」と記す)を35℃で溶解したのち25℃まで冷却した水溶液と、5℃に冷却した塩化メチレンとを、内径6mmのステンレススチール製のパイプに連続的に供給して混合し、混合液をホモミキサー(特殊機化社製品、T.KホモミックラインフローLF−500型)に通して乳化し、乳濁液を調製した。パイプへの供給量はビスフェノールZ 8.63kg/Hr、苛性ソーダ3.86kg/Hr、水110.9kg/Hr、ハイドロサルファイト0.018kg/Hr、及び塩化メチレン68.0kg/Hrである。生成した乳濁液を内径6mmのパイプを経て、内径6mm、長さ34mのPTFE製パイプリアクターに流入させた。パイプリアクターに同時に0℃に冷却した液化ホスゲンを3.4kg/Hrで供給して反応させ、オリゴマーを生成させた。パイプリアクターの流速は1.7m/秒である。ホスゲンとしては、直径55mm、高さ500mmの円筒形容器に上記の活性炭(太平化学社製 ヤシコールS)を充填したものに、−5℃に冷却したホスゲンをSV=3で通液させて精製したものを用いた。
【0049】
なおパイプリアクターでは温度は60℃まで上昇するが、外部冷却により出口では35℃であった。反応混合物は静置分離して水相と油相とに分離した。得られた油相から33kgを分取して、内容積200リットルのファウドラー翼付き反応槽に仕込んだ。
次いでこれに塩化メチレン4.8kg、水33kgを仕込み、窒素雰囲気下、攪拌しながら3℃迄冷却後、触媒としてピリジン塩酸塩をビスフェノールAに対して0.20モル%の割合で加え、また、25%苛性ソーダ水溶液5.41kgを加え60分間、420rpmの撹拌回転数で攪拌しながら重合反応を行い、ポリカーボネート樹脂を生成させた。このとき重合の内温は11℃まで上昇した。
【0050】
この反応混合液に塩化メチレン35kg及び水10kgを加え、室温で20分間撹拌したのち静置して、水相と有機相を分離した。有機相に0.1規定の塩酸28kgを加えて15分間撹拌したのち、静置して水相と有機相とを分離した。この有機相に、純水28kgを加えて15分間撹拌したのち静置して水相と油相とに分離する洗浄操作を3回反復した結果、水相中に塩素イオンが検出されなくなったので、洗浄操作を中止した。有機相からニーダーで塩化メチレンを蒸発させて除き、得られた粉末を乾燥してポリカーボネート樹脂を得た。重合条件、得られたポリカーボネート樹脂の物性を表1に示す。
【0051】
[製造例4]
製造例3において、重合反応時の攪拌回転数を430rpmに代えた以外は製造例3と同様にしてポリカーボネート樹脂の製造を行った。得られたポリカーボネート樹脂の物性を表1に示す。
【0052】
[製造例5]
ハイドロサルファイトが溶解している苛性ソーダ水溶液に2,2−ビス(3−メチル−4−ヒドロキシフェニル)プロパン(以下「ビスフェノールC」と記す)及び、1,1−ビス(4−ヒドロキシフェニル)−1−フェニルエタン(以下「ビスフェノールP」と記す)を35℃で溶解したのち25℃まで冷却した水溶液と、5℃に冷却した塩化メチレンとを、内径6mmのステンレススチール製のパイプに連続的に供給して混合し、混合液をホモミキサー(特殊機化社製品、T.KホモミックラインフローLF−500型)に通して乳化し、乳濁液を調製した。パイプへの供給量はビスフェノールC 8.11kg/Hr、ビスフェノールP 8.20kg/Hr、苛性ソーダ5.28kg/Hr、水101.8kg/Hr、ハイドロサルファイト0.018kg/Hr、及び塩化メチレン68.0kg/Hrである。生成した乳濁液を内径6mmのパイプを経て、内径6mm、長さ34mのPTFE製パイプリアクターに流入させた。パイプリアクターに同時に0℃に冷却した液化ホスゲンを6.3kg/Hrで供給して反応させ、オリゴマーを生成させた。パイプリアクターの流速は1.7m/秒である。ホスゲンとしては、直径55mm、高さ500mmの円筒形容器に上記の活性炭(太平化学社製 ヤシコールS)を充填したものに、−5℃に冷却したホスゲンをSV=3で通液させて精製したものを用いた。
【0053】
なおパイプリアクターでは温度は60℃まで上昇するが、外部冷却により出口では35℃であった。反応混合物は静置分離して水相と油相とに分離した。得られた油相から32kgを分取して、内容積200リットルのファウドラー翼付き反応槽に仕込んだ。
次いでこれに塩化メチレン11.5kg、水30kgを仕込み、窒素雰囲気下、攪拌しながら3℃迄冷却後、触媒としてピリジン塩酸塩をビスフェノールAに対して0.02モル%の割合で加え、また、25%苛性ソーダ水溶液4.65kgを加え60分間、390rpmの撹拌回転数で攪拌しながら重合反応を行い、ポリカーボネート樹脂を生成させた。このとき重合の内温は10℃まで上昇した。
【0054】
この反応混合液に塩化メチレン35kg及び水10kgを加え、室温で20分間撹拌したのち静置して、水相と有機相を分離した。有機相に0.1規定の塩酸28kgを加えて15分間撹拌したのち、静置して水相と有機相とを分離した。この有機相に、純水28kgを加えて15分間撹拌したのち静置して水相と油相とに分離する洗浄操作を3回反復した結果、水相中に塩素イオンが検出されなくなったので、洗浄操作を中止した。有機相からニーダーで塩化メチレンを蒸発させて除き、得られた粉末を乾燥してポリカーボネート樹脂を得た。重合条件、得られたポリカーボネート樹脂の物性を表1に示す。
【0055】
[製造例6]
製造例2において、末端停止剤としてパラ−t−ブチルフェノールをビスフェノールAに対して2.4モル%用い、重合反応時の触媒としてトリエチルアミンをビスフェノールAに対して1.15モル%用いた以外は製造例2と全く同様にしてポリカーボネート樹脂を製造した。重合条件及び得られたポリカーボネート樹脂の物性を表2に示す。
【0056】
[製造例7]
製造例2において、末端停止剤としてパラ−t−ブチルフェノールをビスフェノールAに対して1.6モル%用い、重合反応時の触媒としてトリエチルアミンをビスフェノールAに対して1.15モル%用いた以外は製造例2と全く同様にしてポリカーボネート樹脂を製造した。重合条件及び得られたポリカーボネート樹脂の物性を表2に示す。
【0057】
[製造例8]
製造例3において、末端停止剤としてパラ−t−ブチルフェノールをビスフェノールZに対して1.8モル%用い、重合反応時の触媒としてトリエチルアミンをビスフェノールZに対して1.15モル%用いた以外は製造例3と全く同様にしてポリカーボネート樹脂を製造した。重合条件及び得られたポリカーボネート樹脂の物性を表2に示す。
【0058】
[製造例9]
製造例3において、末端停止剤としてパラ−t−ブチルフェノールをビスフェノールZに対して1.6モル%用い、重合反応時の触媒としてトリエチルアミンをビスフェノールZに対して1.15モル%用いた以外は製造例3と全く同様にしてポリカーボネート樹脂を製造した。重合条件及び得られたポリカーボネート樹脂の物性を表2に示す。
【0059】
[製造例10]
製造例5において、末端停止剤としてパラ−t−ブチルフェノールをビスフェノールZに対して1.7モル%用い、重合反応時の触媒としてトリエチルアミンをビスフェノールZに対して1.15モル%用いた以外は製造例5と全く同様にしてポリカーボネート樹脂を製造した。重合条件及び得られたポリカーボネート樹脂の物性を表2に示す。
【0060】
【表1】
【0061】
【表2】
【0062】
<電荷発生層用分散液の作製>
<下引き層用分散液の作製>
酸化チタン(石原産業(株)製:商品名TTO55N(平均一次粒子径約40nm))にメチルジメトキシシランを3重量%処理したチタニアを、ボールミルによりメタノール/n−プロパノール=7/3の混合溶媒中で分散し、その酸化チタンスラリーに、下記構造式(1)の共重合ポリアミド溶解液を混合し、更に超音波分散処理を行い、溶媒組成が、メタノール/n−プロパノール=7/3で、酸化チタン/ポリアミド=3/1で、固形分濃度16重量%の分散液を調整し、下引き層用分散液を作製した。
【0063】
【化1】
【0064】
CuKα線によるX線回折においてブラック角(2θ±0.2)9.3°、10.6°、13.2°、15.1°、15.7°、16.1°、20.8°、23.3°、26.3°、27.1°に強い回折ピークを示すオキシチタニウムフタロシアニン10部を、1,2−ジメトキシエタン150部に加え、サンドグラインドミルにて粉砕分散処理を行い、顔料分散液を作製した。
【0065】
ポリビニルブチラール(電気化学工業(株)製、商品名デンカブチラール#6000C)5部を1,2−ジメトキシエタン95部に溶解し、固形分濃度5%のバインダー溶液1を作製した。
フェノキシ樹脂(ユニオンカーバイド社製、商品名PKHH)5部を1,2−ジメトキシエタン95部に溶解し、固形分濃度5%のバインダー溶液2を作製した。
先に作製した顔料分散液160部に、バインダー溶液1を50部、バインダー溶液2を50部、適量の1,2−ジメトキシエタンと、適量の4−メトキシ−4−メチルペンタノン−2を加え固形分濃度4.0%、1,2−ジメトキシエタン:4−メトキシ−4−メチルペンタノン−2=9:1の電荷発生層用分散液αを調製した。
【0066】
CuKα線によるX線回折においてブラッグ角(2θ±0.2)27.3゜に最大回折ピークを示すオキシチタニウムフタロシアニン10部を、1,2−ジメトキシエタン150部に加え、サンドグラインドミルにて粉砕分散処理を行い、顔料分散液を作製した。
この顔料分散液160部に、ポリビニルブチラール(電気化学工業(株)製、商品名デンカブチラール#6000C)5部を1,2−ジメトキシエタン95部に溶解した、固形分濃度5%のバインダー溶液100部と、適量の1,2−ジメトキシエタン、適量の4−メトキシ−4−メチルペンタノン−2を加え、固形分濃度4.0%、1,2−ジメトキシエタン:4−メトキシ−4−メチルペンタノン−2=9:1の電荷発生層用分散液β1を作製した。
CuKα線によるX線回折においてブラッグ角(2θ±0.2)9.3°、10.6°、13.2°、15.1°、15.7°、16.1°、20.8°、23.3°、26.3°、27.1°に強い回折ピークを示すオキシチタニウムフタロシアニン10部を、1,2−ジメトキシエタン150部に加え、サンドグラインドミルにて粉砕分散処理を行い、顔料分散液を作製した。
この顔料分散液160部に、ポリビニルブチラール(電気化学工業(株)製、商品名デンカブチラール#6000C)5部を1,2−ジメトキシエタン95部に溶解した、固形分濃度5%のバインダー溶液100部と、適量の1,2−ジメトキシエタン、適量の4−メトキシ−4−メチルペンタノン−2を加え、固形分濃度4.0%、1,2−ジメトキシエタン:4−メトキシ−4−メチルペンタノン−2=9:1の電荷発生層用分散液β2を作製した。
電荷発生層用分散液β1と電荷発生層用分散液β2を8:2の割合で混合し、電荷発生層用分散液βを調製した。
【0067】
<感光体の作製>
実施例1
表面が鏡面仕上げされた外径30mm、長さ285mm、肉厚1.0mmのアルミニウム合金よりなるシリンダーの表面に、陽極酸化処理を行い、その後酢酸ニッケルを主成分とする封孔剤によって封孔処理を行うことにより、約6μmの陽極酸化被膜(アルマイト被膜)を形成した。このシリンダーを先に作製した電荷発生層用分散液αに浸漬塗布し、その乾燥後の重量が0.3g/m2(膜厚約0.3μm)となるように電荷発生層を形成した。
次に、この電荷発生層を形成したシリンダーを、下記構造式(2)に示す電荷輸送性化合物50部と、電荷輸送層用バインダー樹脂として製造例1で作製したポリカーボネート樹脂(粘度平均分子量約30,900、Mw/Mn=1.34、Mv/Mn′=1.15)100部、シリコーンオイル(信越化学社製、商品名KF96)0.05部をテトラヒドロフラン:1,4−ジオキサン=65:35の混合溶媒に溶解させた液に浸漬塗布することにより、乾燥後の膜厚20μmの電荷輸送層を設けた。このようにして得られた感光体ドラムをA1とする。
【0068】
【化2】
【0069】
実施例2
電荷輸送層用バインダー樹脂として製造例2で作製したポリカーボネート樹脂を用いたこと以外は実施例1と同様にして感光体A2を得た。このポリカーボネート樹脂は、Mv=42,200、Mw/Mn=1.32、Mv/Mn′=1.10である。
比較例1
電荷輸送層用バインダー樹脂として製造例6で作製したポリカーボネート樹脂を用いたこと以外は実施例1と同様にして感光体B1を得た。このポリカーボネート樹脂は、Mv=30,200、Mw/Mn=3.02、Mv/Mn′=1.45である。
比較例2
電荷輸送層用バインダー樹脂として製造例7で作製したポリカーボネート樹脂を用いたこと以外は実施例1と同様にして感光体B2を得た。このポリカーボネート樹脂は、Mv=45,900、Mw/Mn=3.55、Mv/Mn′=1.51である。
【0070】
実施例3
表面が鏡面仕上げされた外径30mm、長さ254mm、肉厚0.75mmのアルミニウム合金よりなるシリンダーを、先に調製した下引き層用分散液に浸漬塗布し、膜厚約1.3μmの下引き層を形成した。このシリンダーを先に作製した電荷発生層用分散液βに浸漬し、その乾燥後の重量が0.3g/m2(膜厚約0.3μm)となるように電荷発生層を形成した。
次に、この電荷発生層を形成したシリンダーを、前記構造式(2)に示す電荷輸送性化合物50部と、電荷輸送層用バインダー樹脂として製造例1で作製したポリカーボネート樹脂(粘度平均分子量約30,900、Mw/Mn=1.34、Mv/Mn′=1.15)100部、シリコーンオイル(信越化学社製、商品名KF96)0.05部をテトラヒドロフラン:1,4−ジオキサン=65:35の混合溶媒に溶解させた液に浸漬塗布することにより、乾燥後の膜厚25μmの電荷輸送層を設けた。このようにして得られた感光体ドラムをA3とする。
【0071】
実施例4
電荷輸送層用バインダー樹脂として製造例2で作製したポリカーボネート樹脂を用いたこと以外は実施例3と同様にして感光体A3を得た。このポリカーボネート樹脂は、Mv=42,200、Mw/Mn=1.32、Mv/Mn′=1.10である。
比較例3
電荷輸送層用バインダー樹脂として製造例6で作製したポリカーボネート樹脂を用いたこと以外は実施例3と同様にして感光体B3を得た。このポリカーボネート樹脂は、Mv=30,200、Mw/Mn=3.20、Mv/Mn′=1.45である。
比較例4
電荷輸送層用バインダー樹脂として製造例7で作製したポリカーボネート樹脂を用いたこと以外は実施例3と同様にして感光体B4を得た。このポリカーボネート樹脂は、Mv=45,900、Mw/Mn=3.55、Mv/Mn′=1.51である。
【0072】
実施例5
表面が鏡面仕上げされた外径30mm、長さ285mm、肉厚1.0mmのアルミニウム合金よりなるシリンダーの表面に、陽極酸化処理を行い、その後酢酸ニッケルを主成分とする封孔剤によって封孔処理を行うことにより、約6μmの陽極酸化被膜(アルマイト被膜)を形成した。このシリンダーを先に作製した電荷発生層用分散液αに浸漬塗布し、その乾燥後の重量が0.3g/m2(膜厚約0.3μm)となるように電荷発生層を形成した。
次に、この電荷発生層を形成したシリンダーを、前記構造式(2)に示す電荷輸送性化合物50部と、電荷輸送層用バインダー樹脂として製造例3で作製したポリカーボネート樹脂(粘度平均分子量約41,900、Mw/Mn=1.39、Mv/Mn′=1.04)100部、シリコーンオイル(信越化学社製、商品名KF96)0.05部をテトラヒドロフラン:トルエン=80:20の混合溶媒に溶解させた液に浸漬塗布することにより、乾燥後の膜厚20μmの電荷輸送層を設けた。このようにして得られた感光体ドラムをA5とする。
【0073】
実施例6
電荷輸送層用バインダー樹脂として製造例4で作製したポリカーボネート樹脂を用いたこと以外は実施例5と同様にして感光体A6を得た。このポリカーボネート樹脂は、Mv=52,900、Mw/Mn=1.38、Mv/Mn′=1.04である。
比較例5
電荷輸送層用バインダー樹脂として製造例8で作製したポリカーボネート樹脂を用いたこと以外は実施例5と同様にして感光体B5を得た。このポリカーボネート樹脂は、Mv=46,800、Mw/Mn=3.62、Mv/Mn′=1.52である。
比較例6
電荷輸送層用バインダー樹脂として製造例9で作製したポリカーボネート樹脂を用いたこと以外は実施例5と同様にして感光体B6を得た。このポリカーボネート樹脂は、Mv=56,900、Mw/Mn=3.89、Mv/Mn′=1.54である。
【0074】
実施例7
表面が鏡面仕上げされた外径30mm、長さ254mm、肉厚0.75mmのアルミニウム合金よりなるシリンダーを、先に調製した下引き層用分散液に浸漬塗布し、膜厚約1.3μmの下引き層を形成した。このシリンダーを先に作製した電荷発生層用分散液に浸漬し、その乾燥後の重量が0.3g/m2(膜厚約0.3μm)となるように電荷発生層を形成した。
次に、この電荷発生層を形成したシリンダーを、前記構造式(2)に示す電荷輸送性化合物50部と、電荷輸送層用バインダー樹脂として製造例3で作製したポリカーボネート樹脂(粘度平均分子量約41,900、Mw/Mn=1.39、Mv/Mn′=1.04)100部、シリコーンオイル(信越化学社製、商品名KF96)0.05部をテトラヒドロフラン:トルエン=80:20の混合溶媒に溶解させた液に浸漬塗布することにより、乾燥後の膜厚25μmの電荷輸送層を設けた。このようにして得られた感光体ドラムをA7とする。
【0075】
実施例8
電荷輸送層用バインダー樹脂として製造例4で作製したポリカーボネート樹脂を用いたこと以外は実施例7と同様にして感光体A8を得た。このポリカーボネート樹脂は、Mv=52,900、Mw/Mn=1.38、Mv/Mn′=1.04である。
比較例7
電荷輸送層用バインダー樹脂として製造例8で作製したポリカーボネート樹脂を用いたこと以外は実施例7と同様にして感光体B7を得た。このポリカーボネート樹脂は、Mv=46,800、Mw/Mn=3.62、Mv/Mn′=1.52である。
比較例8
電荷輸送層用バインダー樹脂として製造例9で作製したポリカーボネート樹脂を用いたこと以外は実施例7と同様にして感光体B8を得た。このポリカーボネート樹脂は、Mv=56,900、Mw/Mn=3.89、Mv/Mn′=1.54である。
【0076】
<感光体の評価>
[電気特性評価]
次にこれらA1からA8、B1からB8の感光体を、感光体特性試験機(三菱化学(株)製)に装着し、帯電、露光、電位測定、除電のサイクルによる電気特性評価試験を行った。初期表面電位は−700Vとし、露光はハロゲンランプの光を干渉フィルターで780nmの単色光としたものを用いて、表面電位が−700Vから−350Vに半減するのに要した露光量(半減露光量、E1/2)、4.7μJ/cm2(電荷発生層用分散液αを用いて作製した感光体の場合、露光から電位測定までの時間は約390ms)または1.2μJ/cm2(電荷発生層用分散液βを用いて作製した感光体の場合、露光から電位測定までの時間は約100ms)照射した時点の表面電位(VL)を測定した。また、除電光には660nmのLED光を用いて、除電光照射後の残留電位(Vr)を測定した。測定は温度25℃、湿度50%RHの環境下で行った。結果を表3に示す。
【0077】
【表3】
【0078】
表3で示される通り、実施例の感光体A1ないしA8は、比較例の感光体B1ないしB8と比べて同等若しくは良好な電機特性を有している。
[耐刷試験による膜減り測定]
次に感光体A1、A2、B1、B2、A5、A6、B5、B6を市販のカラーレーザープリンター(エプソン社製 LP3000C)に装着して常温常湿環境下においてモノクロ(黒)モードで24000枚のプリントを行った。
この際、プリントする前の感光層の膜厚、24000枚プリント後の膜厚を測定し、プリント10,000枚あたりの膜減り量を計算した。結果を表4に示す。
また、用いたバインダー樹脂のMvを横軸に10,000あたりの膜減り量を縦軸にとってプロットしたものを図1、図2に示す。
また、感光体A3、A4、B3、B4、A7、A8、B7、B8を市販のモノクロレーザープリンター(レックスマーク社製、Optra S2450、A4縦送りで24枚/分、DC印加のローラー帯電、ローラー転写)に装着して常温常湿下において30,000枚のプリントを行った。プリント前後の膜厚の差から10,000枚あたりの膜減り量を計算した。結果を表5に示す。
また、用いたバインダー樹脂のMvを横軸に10,000あたりの膜減り量を縦軸にとってプロットしたものを図3、図4に示す。
【0079】
【表4】
【0080】
【表5】
【0081】
【発明の効果】
本発明のポリカーボネートは従来使用されているポリカーボネートに比べ耐摩耗性に優れている為、耐熱性や高い表面硬度が要求される用途に適している。また、電子写真感光体において、本発明のポリカーボネートを用いることにより、優れた電気特性を示し、感光体表面の耐摩耗性を著しく向上させることができる。
【図面の簡単な説明】
【図1】粘度平均分子量と膜減り
【図2】粘度平均分子量と膜減り
【図3】粘度平均分子量と膜減り
【図4】粘度平均分子量と膜減り[0001]
BACKGROUND OF THE INVENTION
The present invention relates to electrophotographic photosensitive.To the bodyIn particular, narrow molecular weight distributionIRecarbonate treeFatThe present invention relates to an electrophotographic photoreceptor formed using a binder resin for a photosensitive layer.
[0002]
[Prior art]
In recent years, electrophotographic technology has been widely used and applied not only in the field of copying machines but also in the field of various printers because of its immediacy and high-quality images. Photoconductors, the core of electrophotographic technology, have been used as conventional photoconductive materials for inorganic photoconductors such as selenium, arsenic-selenium alloys, cadmium sulfide, and zinc oxide. A photoreceptor using an organic photoconductive material having advantages such as easy and easy manufacture is mainly used. However, organic photoreceptors have a shorter life than inorganic photoreceptors such as amorphous silicon, and further improvements are required.
[0003]
Since the electrophotographic photosensitive member is repeatedly used in an electrophotographic process, that is, a cycle of charging, exposure, development, transfer, cleaning, static elimination, and the like, it is deteriorated by various stresses during that time. Such deterioration includes, for example, strongly oxidative ozone and NOx generated from a corona charger normally used as a charger, which chemically damages the photosensitive layer, or a carrier (current) generated by image exposure is exposed to light. There are chemical and electrical degradations due to flowing in the layer, static elimination light, and decomposition of the photosensitive layer composition by external light. Further, there is mechanical deterioration such as abrasion of the surface of the photosensitive layer due to rubbing of a cleaning blade, a magnetic brush or the like, contact with a developer, paper, and the like, and film peeling. In particular, such damage on the surface of the photosensitive layer is likely to appear on the copy image, and directly impairs the image quality, which is a major factor that limits the life of the photoreceptor. In addition, if the photosensitive layer is highly worn, the film thickness becomes thin immediately and sufficient charging cannot be obtained, resulting in a short life. That is, in order to develop a long-life photoconductor, it is essential to increase the mechanical strength as well as the electrical and chemical durability.
[0004]
As a photoreceptor using an organic photoconductive material, a so-called dispersion type photoreceptor in which a photoconductive fine powder is dispersed in a binder resin, and a laminate type photoreceptor in which a charge generation layer and a charge transport layer are laminated are known. ing. In addition, in the laminated type photoreceptor, there are a forward laminated type photoreceptor in which the charge generation layer and the charge transport layer are laminated in this order on the conductive substrate, and a reverse laminated type photoreceptor in which the charge transport layer and the charge generation layer are laminated in this order. Are known. Multilayered photoreceptors can be obtained by combining highly efficient charge generating substances and charge transporting substances to obtain highly sensitive photoreceptors, a wide range of material selection, and highly safe photoreceptors. Has been developed and put into practical use as the mainstream of photoconductors because of its high productivity and relatively advantageous cost.
In general, in the case of a sequentially laminated type photoreceptor, it is the charge transport layer that is the outermost layer that is subjected to an electrical, chemical or mechanical load. The charge transport layer is usually composed of a binder resin and a charge transport material, and it is the binder resin that substantially determines the strength, but it does not have sufficient mechanical strength, and has a higher durability. The body is desired.
The binder resin for forming the charge transport layer of the photoreceptor includes vinyl polymers such as polymethyl methacrylate, polystyrene, and polyvinyl chloride, and copolymers thereof, polycarbonate, polyester, polysulfone, phenoxy, epoxy, silicone resin, etc. Thermoplastic resins and various thermosetting resins have been used. Among them, polycarbonate resins have relatively excellent performance, and various polycarbonate resins have been developed and put into practical use. (See
However, conventional organophotoreceptors using polycarbonates have insufficient mechanical strength, so they have disadvantages such as large wear and scratches, so that they have practically limited printing performance. The current situation remains.
[0005]
[Patent Document 1]
JP 50-98332 A
[Patent Document 2]
JP 59-71057 A
[Patent Document 3]
JP 59-184251
[Patent Document 4]
JP-A-5-21478
[0006]
[Problems to be solved by the invention]
The object of the present invention is to provide an electrophotographic photosensitive material that has excellent mechanical properties such as printing durability, abrasion resistance, and slipping property in repeated use, and also has excellent electrical characteristics.BodyIt is to provide.
[0007]
[Means for Solving the Problems]
Therefore, as a result of intensive studies on the improvement of the abrasion resistance of the surface of the electrophotographic photosensitive member, the present inventors have significantly improved the surface strength and durability by using a specific polycarbonate resin as a binder resin for the photosensitive layer. The inventors have found that an electrophotographic photoreceptor excellent in the above can be obtained, and have reached the present invention.
That is, the gist of the present invention is as follows.
An electrophotographic photosensitive member having at least a photosensitive layer on a conductive support.The binder resin of the photosensitive layer isBy reacting a carbonate-forming compound with a dihydroxy compound to form an oligomer and polymerizing the oligomer in the presence of a catalyst.manufacturedPolycarbonate resinBecauseThe catalyst used is a salt of a compound having a basicity of 7 or less as the pKa value of the hydrochloride, and is a polycarbonate resin. The weight average molecular weight (Mw) in terms of polystyrene measured by gel permeation chromatography in the polycarbonate resin The number average molecular weight calculated from the viscosity average molecular weight (Mv) calculated by the following formula (I) and the number of molecular ends, and the ratio (Mw / Mn) of the number average molecular weight (Mn) to 2.4 or less Polycarbonate resin whose ratio (Mv / Mn ′) to (Mn ′) is 1.4 or lessIsElectrophotographic photosensitivebody,
InExist.
[0008]
[Expression 2]
ηsp / C = [η] × (1 + 0.28ηsp) Formula (I)
[Η] = 1.23 × 10-Four× Mv0.83
(In the formula (I), ηsp is the specific viscosity of a polycarbonate resin methylene chloride solution measured at 20 ° C., and C is the concentration of the methylene chloride solution. As the methylene chloride solution, the concentration of the polycarbonate resin is 0.6 g / dl)
[0009]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described in detail. The polycarbonate resin in the present invention is produced by reacting a carbonate-forming compound and a dihydroxy compound. Typically, an aromatic compound (aromatic dihydroxy compound) having two phenolic hydroxyl groups represented by bisphenol A is reacted with phosgene to form an oligomer, and this oligomer is used in the absence of an end-capping agent. And polymerized in the presence of a catalyst such as pyridine hydrochloride or quinoline hydrochloride.
Here, the carbonate-forming compound is a compound capable of forming a carbonate bond [—O—CO—O—] in the polycarbonate main chain by a polymer forming reaction such as a condensation reaction or an exchange reaction. Specifically, phosgene And carbonic acid diester. Examples of the carbonic acid diester include dimethyl carbonate, diethyl carbonate, diphenyl carbonate, and ditolyl carbonate.
[0010]
Examples of the dihydroxy compound include an aliphatic dihydroxy compound and an aromatic dihydroxy compound. Examples of the aromatic dihydroxy compound include an aromatic compound having two phenolic hydroxyl groups.
Specific examples of preferred dihydroxy compounds used in the present invention include bisphenol A, hydroquinone, resorcin, dihydroxydiphenol, bis (hydroxyphenyl) alkane, bis (hydroxyphenyl) cycloalkane, bis (hydroxyphenyl) sulfide, Bis (hydroxyphenyl) ether, bis (hydroxyphenyl) ketone, bis (hydroxyphenyl) sulfone, bis (hydroxyphenyl) sulfoxide, bis (hydroxyphenyl) dialkylbenzene, and derivatives thereof having an alkyl or halogen substituent in the nucleus Is mentioned. Among these, 2,2-bis (4-hydroxyphenyl) propane, 2,2-bis (3,5-dimethyl-4-hydroxyphenyl) propane, 1,1-bis (4- Hydroxyphenyl) cyclohexane and 1,1-bis (4-hydroxyphenyl) -3,3,5-trimethylcyclohexane.
[0011]
A small amount of a branching agent having 3 or more functional groups can be used in combination with the dihydroxy compound. Such branching agents are known, for example 2,4-bis (4'-hydroxyphenyl-isopropyl) phenol, 2,6-bis (2'-hydroxy-5'-methylbenzyl) -4-methylphenol, 2- (4-hydroxyphenyl) -2- (2,4-dihydroxyphenyl) propane, 1,4-bis (4,4′-dihydroxytriphenylmethyl) benzene, 2,4-dihydroxybenzoic acid, trimesic acid, Cyanuric chloride, bis (4'-hydroxyphenyl) -2-oxo-2,3-dihydroxyindole, 3,3-bis (4-hydroxy-3-methylphenyl) -2-oxo-2,3-dihydroindole, etc. Is mentioned. Of these, those having three or more phenolic hydroxyl groups are preferred. The amount of branching agent used varies depending on the target degree of branching, but is usually used in an amount of 0.05 to 2 mol% with respect to the aromatic compound having two phenolic hydroxyl groups. Note that when a branching agent is used in combination, the viscosity average molecular weight (Mv) tends to increase.
[0012]
Next, a polycarbonate having a narrow molecular weight distribution used in the present invention is disclosed in, for example, JP-A-200200.2As described in JP-A-69168, the catalyst can be produced by using a hydrochloride having a pKa value of 7 or less, preferably 6 or less, more preferably 5.5 or less. That is, by using a catalyst having a weak basicity, the nucleophilic substitution reaction can be preferentially caused only from the other ionized terminal (phenylene-ONa terminal) without ionizing the terminal of the chloroformate molecule. Since the reaction mechanism is different from the conventional condensation polymerization at the time of producing a polycarbonate resin that proceeds only by a single reaction, a polycarbonate having a molecular weight distribution according to the Poisson distribution is obtained as a result.
[0013]
Furthermore, the production of the polycarbonate resin according to the present invention is preferably an interfacial polymerization reaction in which an aqueous phase and an organic phase are present as described later. In this interfacial polymerization reaction, the reaction proceeds by a nucleophilic substitution reaction from only the ionized end, and therefore, it is necessarily a sequential reaction that can only produce growth corresponding to the interfacial area per volume. When the molecular weight is large and the condensed species disappears, the chloroformate molecule terminal is hydrolyzed by NaOH in the aqueous phase, and the molecular weight elongation stops as the OH terminal. When the interfacial area per volume is small, as a side reaction, the chloroformate end, which is the molecular end of the growth reaction, undergoes a hydrolysis reaction with NaOH in the aqueous phase, resulting in growth to a molecular weight higher than that. The molecular weight is not obtained, that is, the molecular weight is controlled by the interfacial area. The background to the establishment of such a reaction is that the growth reaction proceeds at a much faster rate than the hydrolysis reaction.
[0014]
In the conventional condensation polymerization that occurs during the production of a general polycarbonate resin, there is no such imbalance in the reaction. In the conventional condensation polymerization, a catalyst having a high pKa value is used, and the chloroformate terminal is also activated in an ion-like manner by the catalyst having a high pKa value, and the reaction activity is almost the same as that of the ionized phenylene-ONa terminal. Is obtained at both molecular ends, and a condensate having a general molecular weight distribution according to Flory's most probable distribution can be obtained. .
[0015]
As a catalyst satisfying the above conditions, a salt of a nitrogen-containing heterocyclic compound is used. For example, a ring carbon atom such as pyridine, quinoline, isoquinoline, picoline, acridine, pyrazine, pyridazine, pyrimidine, 2,4,6-trimethyltriazine may be substituted with an alkyl group, an alkoxy group, a halogen atom, or the like. A salt of a compound having a saturated nitrogen-containing 6-membered ring is used. Further, salts of compounds having an unsaturated nitrogen-containing five-membered ring such as phenothiazine, 2-methylimidazole, benzimidazole, benzotriazole, benzothiazole and the like are also used. Of these nitrogen-containing heterocyclic compounds, pyridine, quinoline, picoline, imidazoles, pyrazoles, triazoles, and the like are preferably used. These catalysts are used so that it may become 0.01-1 mol% normally with respect to the aromatic compound which has two phenolic hydroxyl groups of a raw material. Preferably it is used so that it may become 0.05-0.5 mol%, especially 0.05-0.15 mol%. These nitrogen-containing heterocyclic compounds are used in the salt form such as hydrochloride, sulfate, nitrate, hydrobromide, etc., but in the reaction system, they are in a dissociation equilibrium state between the free base form and the salt form. It is thought that there is.
[0016]
These catalysts may be present in the reaction system from the beginning of the reaction between the aromatic compound having two phenolic hydroxyl groups and phosgene, or may be added to the reaction system after this reaction. However, if the addition of the catalyst is delayed, it becomes difficult to control the molecular weight of the polycarbonate resin to be produced. Accordingly, the catalyst is preferably added to the reaction system from the beginning of the reaction with phosgene until the molecular weight starts to increase, and in terms of viscosity average molecular weight (Mv), Mv reaches 2000 to 3000.
[0017]
On the other hand, as a condensation catalyst, you may use together the well-known thing used for the two-phase interfacial polymerization method. Usually, trialkylamine, N-ethylpyrrolidone, N-ethylpiperidine, N-ethylmorpholine, N-isopropylpiperidine, or N-isopropylmorpholine is used. Of these, triethylamine or N-ethylpiperidine is preferably used. The condensation catalyst is preferably supplied to the reaction system after phosgene is supplied. In the reaction, an aqueous solution prepared by dissolving an aromatic compound having two phenolic hydroxyl groups and caustic soda in water and an inert organic solvent are mixed to prepare an emulsion, and phosgene is supplied thereto. React to produce oligomers. The molar ratio of the aromatic compound having two phenolic hydroxyl groups and caustic soda in the aqueous solution is usually 1: 1.8 to 3.5, preferably 1: 2.0 to 3.2. A small amount of a reducing agent such as hydrosulfite is preferably added to the aqueous solution. The ratio of the organic phase to the aqueous phase is preferably 0.2 to 1.0 (volume ratio). As the inert organic solvent, a phosgene that is a raw material, an oligomer generated by the reaction, and a polycarbonate resin are dissolved under reaction conditions, but those that do not dissolve in water are used. The amount used may be an amount capable of dissolving the produced oligomer, but is usually used so that the concentration of the produced oligomer solution is 10 to 40% by weight.
[0018]
Typical inert organic solvents include aliphatic hydrocarbons such as hexane and n-heptane, methylene chloride, chloroform, carbon tetrachloride, dichloroethane, trichloroethane, tetrachloroethane, dichloropropane and 1,2-dichloroethylene. Chlorinated aliphatic hydrocarbons, aromatic hydrocarbons such as benzene, toluene and xylene, chlorinated aromatic hydrocarbons such as chlorobenzene, o-dichlorobenzene and chlorotoluene, and other substituted aromatic carbons such as nitrobenzene and acetophenone Examples include hydrogen. Of these, chlorinated hydrocarbons such as methylene chloride or chlorobenzene are preferably used. These inert organic solvents can be used alone or as a mixture with other solvents. The oligomer formation reaction is performed at 80 ° C. or lower, preferably 70 ° C. or lower. If the reaction temperature is too high, side reactions will increase and the phosgene intensity will deteriorate. Conversely, a low reaction temperature is advantageous in terms of reaction control, but the reaction is a large exothermic reaction. Therefore, the lower the temperature of the reaction system, the higher the cost for maintaining this temperature. Therefore, considering these points, the reaction is usually carried out at 10 to 65 ° C.
[0019]
The oligomer produced as described above is then polymerized to give a polycarbonate resin. Usually, the reaction mixture obtained in the above oligomer production step is separated into an aqueous phase and an organic phase in which the oligomer is dissolved, and is necessary so that the oligomer concentration in this organic phase is 5 to 30% by weight. Depending on the addition of inert organic solvent. Next, an aqueous solution of caustic soda is newly added to the oligomer solution, and the aforementioned catalyst is further added to cause interfacial polymerization. In this case, the ratio of the aqueous phase to the organic phase is preferably 0.2 to 2.0 (volume ratio). The temperature of the interfacial polymerization reaction varies depending on the organic solvent used, but in the case of methylene chloride, it is usually carried out at 10 to 35 ° C.
[0020]
After completion of the polymerization, the organic phase is washed with an aqueous caustic soda solution until the content of the chloroformate group of the polycarbonate resin is 0.1 μeq / g or less, then washed with an aqueous acid solution to neutralize the alkali and remove the catalyst. Further, the electrolyte is completely removed by washing with water. Finally, the organic solvent is removed from the organic phase by evaporation to obtain a polycarbonate resin. This polycarbonate resin has a very narrow molecular weight distribution in the state as produced by the interfacial polycondensation reaction, that is, without performing a treatment for adjusting the molecular weight distribution such as fractional precipitation or extraction and removal of low molecular weight components.
[0021]
The polycarbonate resin obtained by the above method allows the reaction to occur without using a terminal blocking agent at any stage of the oligomer formation reaction and the polymerization reaction from the oligomer to the polycarbonate resin. is there. If a polycarbonate resin whose molecular terminal is sealed with a long-chain alkyl group is desired, the polycarbonate resin obtained above is reacted with a long-chain alcohol, a long-chain carboxylic acid or a reactive derivative thereof. A polycarbonate resin whose ends are sealed to a desired degree can be obtained.
[0022]
The polycarbonate resin in the present invention can be produced by the above method, and the ratio (Mw / Mn) of polystyrene-equivalent weight average molecular weight (Mw) to number average molecular weight (Mn) measured by gel permeation chromatography is 2. The ratio (Mv / Mn ′) of the viscosity average molecular weight (Mv) calculated by the following formula (I) and the number average molecular weight (Mn ′) calculated from the number of molecular ends is 1.4 or less. It is as follows.
[0023]
[Equation 3]
ηsp / C = [η] × (1 + 0.28ηsp) Formula (I)
[Η] = 1.23 × 10-Four× Mv0.83
(In the formula, ηsp is the specific viscosity measured at 20 ° C. for a methylene chloride solution of polycarbonate resin, and C is the concentration of this methylene chloride solution. The methylene chloride solution has a polycarbonate resin concentration of 0.6 g / dl. Is used)
[0024]
A preferable polycarbonate resin in the present invention has Mw / Mn of 2.4 or less, particularly 2.0 or less. Mv / Mn ′ is preferably 1.3 or less, particularly preferably 1.2 or less. Mw / Mn and Mv / Mn ′ are both indices indicating the width of the molecular weight distribution, and a small value means that the molecular weight distribution is narrow. There have been proposals for the production of polycarbonate resins having a narrow molecular weight distribution, but the products obtained by these conventional production methods have a value far exceeding 2 from Mw / Mn calculated from the glass transition point. Since the value is close to 3, the polycarbonate resin used in the present invention is different from this and has a remarkably narrow molecular weight distribution.
[0025]
Mv is preferably 5,000 to 200,000, more preferably 10,000 to 150,000, and most preferably 20,000 to 100,000. If Mv is less than 5,000, the strength is insufficient and impractical, and if it exceeds 200,000, it is difficult to apply an appropriate film thickness.
[0026]
<Conductive support>
The electrophotographic photoreceptor of the present invention is constituted by forming a photosensitive layer on a conductive support. As the conductive support on which the photosensitive layer is formed, any of those used in known electrophotographic photoreceptors can be used. Specifically, for example, drums, sheets made of metal materials such as aluminum, stainless steel, copper, nickel, zinc, indium, gold, and silver, laminates of these metal foils, deposits, or aluminum, copper, palladium on the surface Insulating supports such as polyester film provided with a conductive layer such as tin oxide, indium oxide, and conductive polymer, paper, and glass. Furthermore, a plastic film, a plastic drum, paper, a paper tube, and the like obtained by applying a conductive material such as metal powder, carbon black, copper iodide, and a polymer electrolyte together with an appropriate binder to conduct a conductive treatment may be used. Further, a plastic sheet or drum containing a conductive material such as metal powder, carbon black, or carbon fiber and becoming conductive can be used. Moreover, the plastic film and belt which carried out the electroconductive process with electroconductive metal oxides, such as a tin oxide and an indium oxide, are mentioned. Thus, the surface of the conductive support can be subjected to various treatments, for example, surface oxidation treatment or chemical treatment within a range that does not affect the image quality. The shape can be any shape such as a drum, a sheet, a belt, a seamless belt, and the like.
[0027]
<Blocking layer>
A known blocking layer that is usually used may be provided between the conductive support and the photosensitive layer. Examples of the blocking layer include an anodized aluminum film, an inorganic layer such as aluminum oxide and aluminum hydroxide, an organic layer such as polyvinyl alcohol, casein, polyvinyl pyrrolidone, polyacrylic acid, celluloses, gelatin, starch, polyurethane, polyimide and polyamide. Layers are used. When the organic layer is used as a blocking layer, a metal oxide such as titania, alumina, silica, and zirconium oxide or a metal fine powder such as copper, silver, and aluminum may be dispersed.
[0028]
Although the film thickness of these blocking layers can be set suitably, it is 0.05-20 micrometers normally, Preferably it is the range of 0.1-10 micrometers.
<Configuration of photosensitive layer>
As the photosensitive layer, any of a so-called laminated type photosensitive layer and a dispersion type photosensitive layer can be used. However, in order to comprehensively consider the mechanical properties, electrical characteristics, manufacturing stability, etc. A laminate type photoreceptor is preferred.
[0029]
<Charge generating material>
Examples of the charge generation material contained in the photosensitive layer include oxide semiconductors such as titanium oxide, silicon materials such as amorphous silicon, other inorganic photoconductive substances, phthalocyanines, azo dyes, quinacridones, polycyclic quinones, pyrylium salts, Various organic pigments and dyes such as perylene, indigo, thioindigo, anthanthrone, pyrantrone, and cyanine can be used. Among them, perylene, metal-free phthalocyanine, copper, indium chloride, gallium, silicon, tin, titanium, zinc, vanadium and other metals, or oxides, chlorides, hydroxide coordinated phthalocyanines, or monoazo, Azo pigments such as bisazo, trisazo and polyazos are desirable.
Further, two or more kinds of charge generating materials may be mixed and used for the purpose of improving the chargeability at the first rotation, reducing light fatigue, and adjusting sensitivity.
[0030]
<Charge transport material>
In the present invention, charge transport materials used in the photosensitive layer include diphenoquinone derivatives, aromatic nitro compounds such as 2,4,7-trinitrofluorenone, carbazole derivatives, indole derivatives, imidazole derivatives, oxazole derivatives, pyrazole derivatives, oxalates. Heterocyclic compounds such as diazole derivatives, pyrazoline derivatives, thiadiazole derivatives, aniline derivatives, hydrazone compounds, aromatic amine derivatives, stilbene derivatives, butadiene derivatives, enamine compounds, a combination of these compounds, or from these compounds And a polymer having such a group in the main chain or side chain. In addition, you may use the said charge transport material in mixture of 2 or more types.
[0031]
<Dispersion type photosensitive layer>
When the electrophotographic photosensitive member of the present invention has a dispersion type photosensitive layer, the charge generating material is dispersed or dissolved in the layer containing the polycarbonate resin of the present invention together with the charge transporting material.
At this time, the particle size of the charge generating material needs to be sufficiently small, and is preferably 1 μm or less, more preferably 0.5 μm or less.
The amount of the charge generating material dispersed or dissolved in the photosensitive layer is, for example, in the range of 0.5 to 50% by weight. However, if the amount is too small, sufficient sensitivity cannot be obtained. And is preferably used in the range of 1 to 20% by weight.
Furthermore, the photosensitive layer may contain various additives such as an antioxidant, an electron-withdrawing compound, a leveling agent, a lubricant, an ultraviolet absorber, and a sensitizer as necessary.
In addition, various additives for improving the mechanical strength and durability of the coating film can also be used. Examples of such additives include known plasticizers, various stabilizers, fluidity imparting agents, and crosslinking agents.
The resulting coating solution is coated on a conductive support and dried to form a photosensitive layer. Usually, the coating solution is used in a thickness of several μm to several tens of μm, preferably 10 to 45 μm, more preferably 20 to 35 μm.
[0032]
<Laminated photosensitive layer>
i) Charge generation layer
When the electrophotographic photoreceptor of the present invention has a laminated photosensitive layer, the charge generating material is used alone or in combination with a binder resin to form the charge generating layer.
Disperse and dissolve the charge generating material in an appropriate dispersion medium using a ball mill, ultrasonic disperser, paint shaker, attritor, sand grinder, etc., and add a binder resin as necessary to adjust the coating solution. The coating solution is dried by a coating method such as dipping method, spray method, bar coater method, blade method, roll coater method, wire bar coating method, knife coater coating method.
[0033]
Examples of the binder resin include polyester resin, polyvinyl acetate, polyester, polycarbonate, polyvinyl acetoacetal, polyvinyl propional, polyvinyl butyral, phenoxy resin, epoxy resin, urethane resin, cellulose ester, cellulose ether, styrene, vinyl acetate, vinyl chloride, Examples thereof include polymers and copolymers of vinyl compounds such as acrylic acid esters, methacrylic acid esters, vinyl alcohol, and ethyl vinyl ether, polyamides, and silicon resins. In this case, the charge generation material is usually 5 to 500 parts by weight, preferably 20 to 300 parts by weight, based on 100 parts by weight of the binder resin. The film thickness of the charge generation layer is usually 0.01-5 μm, preferably 0.05-2 μm, more preferably 0.15-0.8 μm. In addition, the charge generation layer may contain various additives such as a leveling agent, an antioxidant, and a sensitizer for improving the coating property as necessary.
When the charge generating material is used alone, the coating solution may be prepared and applied without adding a binder to the dispersion, or may be formed by a method such as vapor deposition or sputtering.
[0034]
ii) Charge transport layer
When the electrophotographic photoreceptor of the present invention has a function-separated type photosensitive layer, the charge transport material is mixed with a binder resin containing the polycarbonate resin of the present invention to form a charge transport layer.
The ratio of the charge transport material and the binder resin is usually 10 to 200 parts by weight, preferably 30 to 150 parts by weight, based on 100 parts by weight of the binder resin.
The thickness of the charge transport layer is usually 10 to 50 μm, preferably 13 to 35 μm.
Furthermore, the charge transport layer may contain various additives such as an antioxidant, an electron-withdrawing compound, a leveling agent, a lubricant, an ultraviolet absorber, a sensitizer, and other charge transport materials as necessary. .
In addition, various additives for improving the mechanical strength and durability of the coating film can be used. Examples of such additives include known plasticizers, various stabilizers, fluidity imparting agents, and crosslinking agents.
[0035]
<Coating solution for forming photosensitive layer>
Solvents and dispersion media used when applying the above layers include butylamine, diethylamine, ethylenediamine, isopropanolamine, triethanolamine, triethylenediamine, N, N-dimethylformamide, acetone, methyl ethyl ketone, cyclohexanone, benzene, toluene, Xylene, chloroform, 1,2-dichloroethane, 1,2-dichloropropane, 1,1,2-trichloroethane, 1,1,1-trichloroethane, trichloroethylene, tetrachloroethane, dichloromethane, tetrahydrofuran, dioxane, methyl Examples include alcohol, ethyl alcohol, isopropyl alcohol, ethyl acetate, butyl acetate, dimethyl sulfoxide, and methyl cellosolve.
These solvents may be used alone or in combination of two or more.
[0036]
<Photosensitive layer forming method>
Examples of the photosensitive layer coating method include a spray coating method, a spiral coating method, a ring coating method, and a dip coating method.
Spray coating methods include air spray, airless spray, electrostatic air spray, electrostatic airless spray, rotary atomizing electrostatic spray, hot spray, and hot airless spray. Considering the degree of conversion, adhesion efficiency, etc., in the rotary atomizing electrostatic spray, the conveying method disclosed in the republished Japanese Patent Publication No. 1-805198, that is, the cylindrical workpiece is rotated while the axial direction is spaced. By continuously transporting the electrophotographic photosensitive member, an electrophotographic photosensitive member excellent in film thickness uniformity can be obtained with a comprehensively high adhesion efficiency.
[0037]
Examples of the spiral coating method include a method using a liquid injection coating machine or a curtain coating machine disclosed in Japanese Patent Laid-Open No. 52-119651, and paint from a minute opening disclosed in Japanese Patent Laid-Open No. 1-2231966. There are a method of continuously flying in a streak shape, a method using a multi-nozzle body disclosed in JP-A-3-193161, and the like.
As an example of the dip coating method, the following coating formation procedure of the charge transport layer may be mentioned.
Using a charge transport material, binder resin, solvent, etc., the total solid concentration is 15% or more, more preferably 40% or less, and the viscosity is usually 50 centipoise or more and 700 centipoise or less, preferably 100 centipoise or more and 500 centipoise. The following coating liquid for forming the charge transport layer is prepared.
After the coating film is formed, the coating film is dried, and the drying temperature and time are adjusted so that necessary and sufficient drying is performed. A drying temperature is 100-250 degreeC normally, Preferably it is 110-170 degreeC, More preferably, it is the range of 115-140 degreeC. As a drying method, a hot air dryer, a steam dryer, an infrared dryer, a far infrared dryer, or the like can be used.
The electrophotographic photoreceptor of the present invention thus obtained maintains excellent printing durability and slipperiness over a long period of time, and is suitable for electrophotographic fields such as copying machines, printers, fax machines, and plate-making machines.
[0038]
【Example】
EXAMPLES Hereinafter, although an Example demonstrates this invention still in detail, this invention is not limited to a following example, unless the summary is exceeded. “Parts” used in Examples and Comparative Examples indicates “parts by weight” unless otherwise specified.
<Preparation of binder resin>
The evaluation method in the production example is as follows.
(1) Measurement of gel permeation chromatography
Equipment: Tosoh Corporation product, HLC-8020
Columns: Four columns (diameter: 7.8 mmφ, length: 300 mm) packed with TSK 5000HLX, 4000HLX, 3000HLX, and 2000HLX (all manufactured by Tosoh Corporation) were used as fillers.
Detector: Refractometer
Eluent: Tetrahydrofuran
Calibration curve: Standard polystyrene (molecular weight; 761 (Mw / Mn ≦ 1.14), 2000 (Mw / Mn ≦ 1.20), 4000 (Mw / Mn ≦ 1.06), 9000 (Mw) manufactured by Chemco Corporation /Mn≦1.04), 17500 (Mw / Mn ≦ 1.03), 50000 (Mw / Mn ≦ 1.03), 233000 (Mw / Mn ≦ 1.05), 600000 (Mw / Mn ≦ 1.05) ) And 900,000 (Mw / Mn ≦ 1.05).
Operation: Mw and Mn were determined in terms of polystyrene from the chart obtained by detecting the difference in refractive index, and Mw / Mn was calculated. The baseline at this time was calculated by connecting the point where the base before the rising of the high molecular weight was faithfully extended as it was and the point where it returned to the original baseline on the low molecular weight side while the device was completely stable. In addition, it was confirmed that the above-mentioned standard polystyrene was measured and all were within the standard.
[0039]
(2) Measurement of number average molecular weight (Mn ′)
The ends of the polycarbonate resin produced without using the end-capping agent and the remaining ends not terminated with the terminator are all OH groups. The terminal OH group was colored with titanium tetrachloride under the acidity of acetic acid, and the terminal group was quantified by measuring the absorbance at a wavelength of 480 nm. The number average molecular weight (Mn ′) was calculated by the following formula (II).
Mn ′ = 106/ (Number of terminal groups (μeq / g) × 1/2) Formula (II)
[0040]
Further, when a terminal blocking agent is used in the polymerization, it is calculated from the number of terminal OH groups obtained by the above measurement and the amount of the sealing agent added, assuming that the terminal blocking agent is all bonded to the terminal. The total with the number of terminal groups on the end was taken as the number of terminal groups. In addition, the polycarbonate resin polymerized in the presence of the end-capping agent was subjected to alkali hydrolysis in a preliminary experiment, and the amount of the end-capping agent bonded was quantified, and all the used end-capping agents were bonded to the molecular ends. I have confirmed that.
[0041]
(3) Measurement of viscosity average molecular weight (Mv)
It calculated | required based on following formula (I).
[0042]
[Expression 4]
ηsp / C = [η] × (1 + 0.28ηsp) Formula (I)
[Η] = 1.23 × 10-Four× Mv0.83
In the formula, ηsp is the specific viscosity measured at 20 ° C. for a methylene chloride solution of polycarbonate resin, and C is the concentration of this methylene chloride solution. As the methylene chloride solution, a polycarbonate resin having a concentration of 0.6 g / dl was used.
[0043]
[Production Example 1]
An aqueous solution in which 2,2-bis (4-hydroxyphenyl) propane (hereinafter referred to as “bisphenol A”) is dissolved at 35 ° C. and then cooled to 25 ° C. in a caustic soda aqueous solution in which hydrosulfite is dissolved; The cooled methylene chloride is continuously supplied to a stainless steel pipe having an inner diameter of 6 mm and mixed, and the mixed solution is supplied to a homomixer (product of Tokushu Kaika Co., Ltd., TK homomic line flow LF-500 type). And emulsified to prepare an emulsion. The supply amount to the pipe is 16.31 kg / Hr of bisphenol A, 5.93 kg / Hr of caustic soda, 101.1 kg / Hr of water, 0.018 kg / Hr of hydrosulfite, and 68.0 kg / Hr of methylene chloride. The produced emulsion was allowed to flow through a pipe reactor having an inner diameter of 6 mm into a PTFE (polytetrafluoroethylene) pipe reactor having an inner diameter of 6 mm and a length of 34 m. Liquefied phosgene, cooled to 0 ° C. at the same time, was supplied to the pipe reactor at 7.5 kg / Hr for reaction to produce oligomers. The flow rate of the pipe reactor is 1.7 m / sec. As phosgene, phosgene cooled to −5 ° C. was passed through SV = 3 into a cylindrical container having a diameter of 55 mm and a height of 500 mm filled with the following activated carbon (trade name: Taihei Chemical Co., Ltd., trade name: Yokokor S). The purified product was used.
[0044]
Various physical properties of activated carbon cocool S (product of Taihei Chemicals)
True density: 2.1 g / ml
Porosity: 40%
Specific surface area: 1200m2/ G
Pore volume: 0.86 ml / g
[0045]
In the pipe reactor, the temperature rose to 60 ° C, but was 35 ° C at the outlet due to external cooling. The reaction mixture was allowed to stand and separate into an aqueous phase and an oil phase. 30 kg was fractionated from the obtained oil phase, and charged into a reaction vessel with an internal volume of 200 liters with a Faudler blade.
Next, 16 kg of methylene chloride and 32 kg of water were added thereto, and after cooling to 3 ° C. with stirring in a nitrogen atmosphere, pyridine hydrochloride as a catalyst was added at a ratio of 0.02 mol% with respect to bisphenol A, and 25% 4.15 kg of an aqueous caustic soda solution was added and a polymerization reaction was carried out for 60 minutes with stirring at 400 rpm, thereby producing a polycarbonate resin. At this time, the internal temperature of the polymerization rose to 11 ° C.
[0046]
To this reaction mixture, 3.04 mol% of benzoyl chloride as an end terminator with respect to bisphenol A and caustic soda equivalent to the terminator were added and stirred for 60 minutes while maintaining the same temperature. To the reaction mixture, 35 kg of methylene chloride and 10 kg of water were added, stirred for 20 minutes at room temperature, and allowed to stand to separate the aqueous phase and the organic phase. To the organic phase, 28 kg of 0.1N hydrochloric acid was added and stirred for 15 minutes, and then allowed to stand to separate the aqueous phase and the organic phase. As a result of repeating the washing operation of adding 28 kg of pure water to this organic phase and stirring for 15 minutes and then allowing it to stand to separate into an aqueous phase and an oil phase, chlorine ions were no longer detected in the aqueous phase. The washing operation was stopped. From the organic phase, methylene chloride was removed by evaporation with a kneader, and the resulting powder was dried to obtain a polycarbonate resin. Table 1 shows polymerization conditions and physical properties of the obtained polycarbonate resin.
[0047]
[Production Example 2]
In Production Example 1, the stirring rotation speed during the polymerization reaction was changed to 420, and the amount of caustic soda added at the same time as the end terminator and the end terminator was changed to 2.45 mol% with respect to bisphenol A. In the same manner as in Example 1, polycarbonate resin was produced. Table 1 shows the physical properties of the obtained polycarbonate resin.
[0048]
[Production Example 3]
An aqueous solution in which 1,1-bis (4-hydroxyphenyl) cyclohexane (hereinafter referred to as “bisphenol Z”) is dissolved at 35 ° C. and then cooled to 25 ° C. in a caustic soda aqueous solution in which hydrosulfite is dissolved; The cooled methylene chloride is continuously supplied to a stainless steel pipe having an inner diameter of 6 mm and mixed, and the mixed solution is supplied to a homomixer (product of Tokushu Kaika Co., Ltd., TK homomic line flow LF-500 type). And emulsified to prepare an emulsion. The feed rates to the pipe are bisphenol Z 8.63 kg / Hr, caustic soda 3.86 kg / Hr, water 110.9 kg / Hr, hydrosulfite 0.018 kg / Hr, and methylene chloride 68.0 kg / Hr. The produced emulsion was passed through a pipe having an inner diameter of 6 mm and a PTFE pipe reactor having an inner diameter of 6 mm and a length of 34 m. Liquefied phosgene, cooled to 0 ° C. at the same time, was supplied to the pipe reactor at 3.4 kg / Hr for reaction to produce oligomers. The flow rate of the pipe reactor is 1.7 m / sec. The phosgene was purified by passing phosgene cooled to −5 ° C. at SV = 3 into a cylindrical container having a diameter of 55 mm and a height of 500 mm filled with the activated carbon (Yaikol S manufactured by Taihei Chemical Co., Ltd.). A thing was used.
[0049]
In the pipe reactor, the temperature rose to 60 ° C, but was 35 ° C at the outlet due to external cooling. The reaction mixture was allowed to stand and separate into an aqueous phase and an oil phase. 33 kg of the obtained oil phase was fractionated and charged into a reaction vessel with an internal volume of 200 liters equipped with a Faudler blade.
Next, 4.8 kg of methylene chloride and 33 kg of water were added thereto, and after cooling to 3 ° C. with stirring in a nitrogen atmosphere, pyridine hydrochloride was added as a catalyst in a proportion of 0.20 mol% with respect to bisphenol A. 5.41 kg of 25% aqueous sodium hydroxide solution was added and a polymerization reaction was carried out for 60 minutes with stirring at 420 rpm and a polycarbonate resin was produced. At this time, the internal temperature of the polymerization rose to 11 ° C.
[0050]
To this reaction mixture, 35 kg of methylene chloride and 10 kg of water were added, stirred for 20 minutes at room temperature, and allowed to stand to separate the aqueous phase and the organic phase. To the organic phase, 28 kg of 0.1N hydrochloric acid was added and stirred for 15 minutes, and then allowed to stand to separate the aqueous phase and the organic phase. As a result of repeating the washing operation of adding 28 kg of pure water to this organic phase and stirring for 15 minutes and then allowing it to stand to separate into an aqueous phase and an oil phase, chlorine ions were no longer detected in the aqueous phase. The washing operation was stopped. From the organic phase, methylene chloride was removed by evaporation with a kneader, and the resulting powder was dried to obtain a polycarbonate resin. Table 1 shows polymerization conditions and physical properties of the obtained polycarbonate resin.
[0051]
[Production Example 4]
In Production Example 3, a polycarbonate resin was produced in the same manner as in Production Example 3, except that the number of stirring rotations during the polymerization reaction was changed to 430 rpm. Table 1 shows the physical properties of the obtained polycarbonate resin.
[0052]
[Production Example 5]
2,2-bis (3-methyl-4-hydroxyphenyl) propane (hereinafter referred to as “bisphenol C”) and 1,1-bis (4-hydroxyphenyl)-are added to an aqueous caustic soda solution in which hydrosulfite is dissolved. An aqueous solution in which 1-phenylethane (hereinafter referred to as “bisphenol P”) is dissolved at 35 ° C. and then cooled to 25 ° C. and methylene chloride cooled to 5 ° C. are continuously added to a stainless steel pipe having an inner diameter of 6 mm. The mixture was supplied and mixed, and the mixture was emulsified by passing through a homomixer (product of Tokushu Kika Co., Ltd., TK homomic line flow LF-500 type) to prepare an emulsion. The feed rates to the pipe were bisphenol C 8.11 kg / Hr, bisphenol P 8.20 kg / Hr, caustic soda 5.28 kg / Hr, water 101.8 kg / Hr, hydrosulfite 0.018 kg / Hr, and methylene chloride 68. 0 kg / Hr. The produced emulsion was passed through a pipe having an inner diameter of 6 mm and a PTFE pipe reactor having an inner diameter of 6 mm and a length of 34 m. Liquefied phosgene, cooled to 0 ° C. at the same time, was supplied to the pipe reactor at 6.3 kg / Hr for reaction to produce oligomers. The flow rate of the pipe reactor is 1.7 m / sec. The phosgene was purified by passing phosgene cooled to −5 ° C. at SV = 3 into a cylindrical container having a diameter of 55 mm and a height of 500 mm filled with the activated carbon (Yaikol S manufactured by Taihei Chemical Co., Ltd.). Things were used.
[0053]
In the pipe reactor, the temperature rose to 60 ° C, but was 35 ° C at the outlet due to external cooling. The reaction mixture was allowed to stand and separate into an aqueous phase and an oil phase. From the obtained oil phase, 32 kg was collected and charged into a reaction vessel with a fouler blade having an internal volume of 200 liters.
Next, 11.5 kg of methylene chloride and 30 kg of water were added thereto, and after cooling to 3 ° C. with stirring in a nitrogen atmosphere, pyridine hydrochloride was added as a catalyst at a ratio of 0.02 mol% with respect to bisphenol A. 4.65 kg of 25% caustic soda aqueous solution was added and a polymerization reaction was carried out for 60 minutes while stirring at a stirring speed of 390 rpm to produce a polycarbonate resin. At this time, the internal temperature of the polymerization rose to 10 ° C.
[0054]
To this reaction mixture, 35 kg of methylene chloride and 10 kg of water were added, stirred for 20 minutes at room temperature, and allowed to stand to separate the aqueous phase and the organic phase. To the organic phase, 28 kg of 0.1N hydrochloric acid was added and stirred for 15 minutes, and then allowed to stand to separate the aqueous phase and the organic phase. As a result of repeating the washing operation of adding 28 kg of pure water to this organic phase and stirring for 15 minutes and then allowing it to stand to separate into an aqueous phase and an oil phase, chlorine ions were no longer detected in the aqueous phase. The washing operation was stopped. The methylene chloride was removed by evaporation from the organic phase with a kneader, and the resulting powder was dried to obtain a polycarbonate resin. Table 1 shows polymerization conditions and physical properties of the obtained polycarbonate resin.
[0055]
[Production Example 6]
Manufactured in Production Example 2 except that para-t-butylphenol was used at 2.4 mol% with respect to bisphenol A as a terminal terminator and triethylamine was used at 1.15 mol% with respect to bisphenol A as a catalyst during the polymerization reaction. A polycarbonate resin was produced in exactly the same manner as in Example 2. Table 2 shows the polymerization conditions and the physical properties of the obtained polycarbonate resin.
[0056]
[Production Example 7]
In Production Example 2, production was performed except that para-t-butylphenol was used at 1.6 mol% with respect to bisphenol A as a terminal terminator and triethylamine was used at 1.15 mol% with respect to bisphenol A as a catalyst during the polymerization reaction. A polycarbonate resin was produced in exactly the same manner as in Example 2. Table 2 shows the polymerization conditions and the physical properties of the obtained polycarbonate resin.
[0057]
[Production Example 8]
Production Example 3 except that para-t-butylphenol was used at 1.8 mol% with respect to bisphenol Z as a terminal terminator, and triethylamine was used at 1.15 mol% with respect to bisphenol Z as a catalyst during the polymerization reaction. A polycarbonate resin was produced in exactly the same manner as in Example 3. Table 2 shows the polymerization conditions and the physical properties of the obtained polycarbonate resin.
[0058]
[Production Example 9]
Production Example 3 except that para-t-butylphenol was used at 1.6 mol% with respect to bisphenol Z as a terminal terminator and triethylamine was used at 1.15 mol% with respect to bisphenol Z as a catalyst during the polymerization reaction. A polycarbonate resin was produced in exactly the same manner as in Example 3. Table 2 shows the polymerization conditions and the physical properties of the obtained polycarbonate resin.
[0059]
[Production Example 10]
Manufactured in Production Example 5 except that para-t-butylphenol was used at 1.7 mol% with respect to bisphenol Z as a terminal terminator and triethylamine was used at 1.15 mol% with respect to bisphenol Z as a catalyst during the polymerization reaction. A polycarbonate resin was produced in exactly the same manner as in Example 5. Table 2 shows the polymerization conditions and the physical properties of the obtained polycarbonate resin.
[0060]
[Table 1]
[0061]
[Table 2]
[0062]
<Preparation of dispersion for charge generation layer>
<Preparation of dispersion for undercoat layer>
Titania treated with 3% by weight of methyldimethoxysilane on titanium oxide (Ishihara Sangyo Co., Ltd .: trade name: TTO55N (average primary particle size: about 40 nm)) in a mixed solvent of methanol / n-propanol = 7/3 by a ball mill. The titanium oxide slurry is mixed with a copolymerized polyamide solution of the following structural formula (1), further subjected to ultrasonic dispersion treatment, and the solvent composition is methanol / n-propanol = 7/3. A dispersion having a solid content concentration of 16% by weight with titanium / polyamide = 3/1 was prepared to prepare an undercoat layer dispersion.
[0063]
[Chemical 1]
[0064]
Black angle (2θ ± 0.2) 9.3 °, 10.6 °, 13.2 °, 15.1 °, 15.7 °, 16.1 °, 20.8 ° in X-ray diffraction by CuKα ray 10 parts of oxytitanium phthalocyanine showing a strong diffraction peak at 23.3 °, 26.3 ° and 27.1 ° are added to 150 parts of 1,2-dimethoxyethane, and pulverized and dispersed in a sand grind mill. A pigment dispersion was prepared.
[0065]
5 parts of polyvinyl butyral (trade name Denkabutyral # 6000C, manufactured by Denki Kagaku Kogyo Co., Ltd.) was dissolved in 95 parts of 1,2-dimethoxyethane to prepare a
5 parts of a phenoxy resin (trade name PKHH, manufactured by Union Carbide) was dissolved in 95 parts of 1,2-dimethoxyethane to prepare a
To 160 parts of the pigment dispersion prepared earlier, 50 parts of
[0066]
10 parts of oxytitanium phthalocyanine, which shows the maximum diffraction peak at a Bragg angle (2θ ± 0.2) of 27.3 ° in X-ray diffraction using CuKα rays, is added to 150 parts of 1,2-dimethoxyethane and pulverized in a sand grind mill. Dispersion treatment was performed to prepare a pigment dispersion.
A binder solution 100 having a solid content concentration of 5% was prepared by dissolving 5 parts of polyvinyl butyral (trade name Denkabutyral # 6000C, manufactured by Denki Kagaku Kogyo Co., Ltd.) in 95 parts of 1,2-dimethoxyethane in 160 parts of this pigment dispersion. Part, an appropriate amount of 1,2-dimethoxyethane and an appropriate amount of 4-methoxy-4-methylpentanone-2, and a solid content concentration of 4.0%, 1,2-dimethoxyethane: 4-methoxy-4-methyl A dispersion β1 for charge generation layer of pentanone-2 = 9: 1 was prepared.
Bragg angles (2θ ± 0.2) 9.3 °, 10.6 °, 13.2 °, 15.1 °, 15.7 °, 16.1 °, 20.8 ° in X-ray diffraction by CuKα ray 10 parts of oxytitanium phthalocyanine showing a strong diffraction peak at 23.3 °, 26.3 ° and 27.1 ° are added to 150 parts of 1,2-dimethoxyethane, and pulverized and dispersed in a sand grind mill. A pigment dispersion was prepared.
A binder solution 100 having a solid content concentration of 5% was prepared by dissolving 5 parts of polyvinyl butyral (trade name Denkabutyral # 6000C, manufactured by Denki Kagaku Kogyo Co., Ltd.) in 95 parts of 1,2-dimethoxyethane in 160 parts of this pigment dispersion. Part, an appropriate amount of 1,2-dimethoxyethane and an appropriate amount of 4-methoxy-4-methylpentanone-2, and a solid content concentration of 4.0%, 1,2-dimethoxyethane: 4-methoxy-4-methyl A dispersion β2 for charge generation layer of pentanone-2 = 9: 1 was prepared.
Charge generation layer dispersion β1 and charge generation layer dispersion β2 were mixed at a ratio of 8: 2 to prepare charge generation layer dispersion β.
[0067]
<Production of photoconductor>
Example 1
The surface of a cylinder made of an aluminum alloy with an outer diameter of 30 mm, a length of 285 mm, and a wall thickness of 1.0 mm is mirror-finished, and then anodized, and then sealed with a sealant mainly composed of nickel acetate. As a result, an anodic oxide coating (alumite coating) of about 6 μm was formed. This cylinder was dip-coated in the charge generation layer dispersion α prepared earlier, and the weight after drying was 0.3 g / m.2The charge generation layer was formed so as to have a film thickness of about 0.3 μm.
Next, the cylinder in which this charge generation layer was formed was prepared by using 50 parts of the charge transporting compound represented by the following structural formula (2) and the polycarbonate resin (viscosity average molecular weight of about 30) produced in Production Example 1 as a binder resin for the charge transport layer. , 900, Mw / Mn = 1.34, Mv / Mn ′ = 1.15) 100 parts, silicone oil (trade name KF96, manufactured by Shin-Etsu Chemical Co., Ltd.) 0.05 parts tetrahydrofuran: 1,4-dioxane = 65: A charge transport layer having a thickness of 20 μm after drying was provided by dip coating in a solution dissolved in 35 mixed solvent. The photoreceptor drum thus obtained is designated as A1.
[0068]
[Chemical formula 2]
[0069]
Example 2
A photoconductor A2 was obtained in the same manner as in Example 1 except that the polycarbonate resin prepared in Production Example 2 was used as the binder resin for the charge transport layer. This polycarbonate resin has Mv = 42,200, Mw / Mn = 1.32, and Mv / Mn ′ = 1.10.
Comparative Example 1
A photoreceptor B1 was obtained in the same manner as in Example 1 except that the polycarbonate resin prepared in Production Example 6 was used as the binder resin for the charge transport layer. This polycarbonate resin has Mv = 30,200, Mw / Mn = 3.02, Mv / Mn ′ = 1.45.
Comparative Example 2
A photoconductor B2 was obtained in the same manner as in Example 1 except that the polycarbonate resin prepared in Production Example 7 was used as the binder resin for the charge transport layer. This polycarbonate resin has Mv = 45,900, Mw / Mn = 3.55, and Mv / Mn ′ = 1.51.
[0070]
Example 3
A cylinder made of an aluminum alloy with an outer diameter of 30 mm, a length of 254 mm, and a wall thickness of 0.75 mm, which has a mirror-finished surface, is dip-coated in the previously prepared dispersion for the undercoat layer, and the film thickness is about 1.3 μm below. A pulling layer was formed. The cylinder was immersed in the charge generation layer dispersion β prepared earlier, and the weight after drying was 0.3 g / m.2The charge generation layer was formed so as to have a film thickness of about 0.3 μm.
Next, the cylinder on which this charge generation layer was formed was prepared by using 50 parts of the charge transporting compound represented by the structural formula (2) and the polycarbonate resin (viscosity average molecular weight of about 30) produced in Production Example 1 as a binder resin for the charge transport layer. , 900, Mw / Mn = 1.34, Mv / Mn ′ = 1.15) 100 parts, silicone oil (trade name KF96, manufactured by Shin-Etsu Chemical Co., Ltd.) 0.05 parts tetrahydrofuran: 1,4-dioxane = 65: A charge transport layer having a thickness of 25 μm after drying was provided by dip coating in a solution dissolved in 35 mixed solvent. The photoreceptor drum thus obtained is designated as A3.
[0071]
Example 4
A photoconductor A3 was obtained in the same manner as in Example 3 except that the polycarbonate resin prepared in Production Example 2 was used as the binder resin for the charge transport layer. This polycarbonate resin has Mv = 42,200, Mw / Mn = 1.32, and Mv / Mn ′ = 1.10.
Comparative Example 3
A photoconductor B3 was obtained in the same manner as in Example 3 except that the polycarbonate resin prepared in Production Example 6 was used as the binder resin for the charge transport layer. This polycarbonate resin has Mv = 30,200, Mw / Mn = 3.20, and Mv / Mn ′ = 1.45.
Comparative Example 4
A photoconductor B4 was obtained in the same manner as in Example 3 except that the polycarbonate resin prepared in Production Example 7 was used as the binder resin for the charge transport layer. This polycarbonate resin has Mv = 45,900, Mw / Mn = 3.55, and Mv / Mn ′ = 1.51.
[0072]
Example 5
The surface of a cylinder made of an aluminum alloy with an outer diameter of 30 mm, a length of 285 mm, and a wall thickness of 1.0 mm is mirror-finished, and then anodized, and then sealed with a sealant mainly composed of nickel acetate. As a result, an anodic oxide coating (alumite coating) of about 6 μm was formed. This cylinder was dip-coated in the charge generation layer dispersion α prepared earlier, and the weight after drying was 0.3 g / m.2The charge generation layer was formed so as to have a film thickness of about 0.3 μm.
Next, 50 parts of the charge transporting compound represented by the structural formula (2) and the polycarbonate resin prepared in Production Example 3 as a binder resin for the charge transport layer (viscosity average molecular weight of about 41) were formed on the cylinder on which the charge generation layer was formed. , 900, Mw / Mn = 1.39, Mv / Mn ′ = 1.04), 100 parts of silicone oil (trade name KF96, manufactured by Shin-Etsu Chemical Co., Ltd.), 0.05 parts, mixed solvent of tetrahydrofuran: toluene = 80: 20 A charge transport layer having a thickness of 20 μm after drying was provided by dip coating in the solution dissolved in the solution. The photoreceptor drum thus obtained is designated as A5.
[0073]
Example 6
A photoreceptor A6 was obtained in the same manner as in Example 5 except that the polycarbonate resin prepared in Production Example 4 was used as the binder resin for the charge transport layer. This polycarbonate resin has Mv = 52,900, Mw / Mn = 1.38, and Mv / Mn ′ = 1.04.
Comparative Example 5
A photoconductor B5 was obtained in the same manner as in Example 5 except that the polycarbonate resin prepared in Production Example 8 was used as the binder resin for the charge transport layer. This polycarbonate resin has Mv = 46,800, Mw / Mn = 3.62, Mv / Mn ′ = 1.52.
Comparative Example 6
A photoconductor B6 was obtained in the same manner as in Example 5 except that the polycarbonate resin prepared in Production Example 9 was used as the binder resin for the charge transport layer. This polycarbonate resin has Mv = 56,900, Mw / Mn = 3.89, and Mv / Mn ′ = 1.54.
[0074]
Example 7
A cylinder made of an aluminum alloy with an outer diameter of 30 mm, a length of 254 mm, and a wall thickness of 0.75 mm, which has a mirror-finished surface, is dip-coated in the previously prepared dispersion for the undercoat layer, and the film thickness is about 1.3 μm below. A pulling layer was formed. This cylinder is immersed in the previously prepared dispersion for charge generation layer, and the weight after drying is 0.3 g / m.2The charge generation layer was formed so as to have a film thickness of about 0.3 μm.
Next, 50 parts of the charge transporting compound represented by the structural formula (2) and the polycarbonate resin prepared in Production Example 3 as a binder resin for the charge transport layer (viscosity average molecular weight of about 41) were formed on the cylinder on which the charge generation layer was formed. , 900, Mw / Mn = 1.39, Mv / Mn ′ = 1.04), 100 parts of silicone oil (trade name KF96, manufactured by Shin-Etsu Chemical Co., Ltd.), 0.05 parts, mixed solvent of tetrahydrofuran: toluene = 80: 20 A charge transport layer having a thickness of 25 μm after drying was provided by dip-coating in the solution dissolved in the solution. The photoreceptor drum thus obtained is designated as A7.
[0075]
Example 8
A photoconductor A8 was obtained in the same manner as in Example 7 except that the polycarbonate resin prepared in Production Example 4 was used as the binder resin for the charge transport layer. This polycarbonate resin has Mv = 52,900, Mw / Mn = 1.38, and Mv / Mn ′ = 1.04.
Comparative Example 7
A photoconductor B7 was obtained in the same manner as in Example 7 except that the polycarbonate resin prepared in Production Example 8 was used as the binder resin for the charge transport layer. This polycarbonate resin has Mv = 46,800, Mw / Mn = 3.62, Mv / Mn ′ = 1.52.
Comparative Example 8
A photoconductor B8 was obtained in the same manner as in Example 7 except that the polycarbonate resin prepared in Production Example 9 was used as the binder resin for the charge transport layer. This polycarbonate resin has Mv = 56,900, Mw / Mn = 3.89, and Mv / Mn ′ = 1.54.
[0076]
<Evaluation of photoreceptor>
[Electrical characteristics evaluation]
Next, the photoconductors A1 to A8 and B1 to B8 were mounted on a photoconductor characteristic tester (manufactured by Mitsubishi Chemical Corporation), and an electric characteristic evaluation test was performed by a cycle of charging, exposure, potential measurement, and static elimination. . The initial surface potential was -700V, and the exposure was carried out using a halogen lamp with a monochromatic light of 780 nm using an interference filter, and the exposure amount required to halve the surface potential from -700V to -350V (half exposure amount) , E1 / 2), 4.7 μJ / cm2(In the case of a photoreceptor produced using the dispersion α for charge generation layer, the time from exposure to potential measurement is about 390 ms) or 1.2 μJ / cm2(In the case of a photoreceptor produced using the dispersion β for charge generation layer, the time from exposure to potential measurement is about 100 ms) The surface potential (VL) at the time of irradiation was measured. Moreover, the residual electric potential (Vr) after neutralization light irradiation was measured using 660 nm LED light for static elimination light. The measurement was performed in an environment of temperature 25 ° C. and humidity 50% RH. The results are shown in Table 3.
[0077]
[Table 3]
[0078]
As shown in Table 3, the photoconductors A1 to A8 of the example have the same or better electrical characteristics than the photoconductors B1 to B8 of the comparative example.
[Measurement of film reduction by printing test]
Next, the photoconductors A1, A2, B1, B2, A5, A6, B5, and B6 are mounted on a commercially available color laser printer (LP3000C manufactured by Epson Corporation), and 24,000 sheets in monochrome (black) mode in a normal temperature and humidity environment. Printed out.
At this time, the film thickness of the photosensitive layer before printing and the film thickness after printing 24,000 sheets were measured, and the amount of film reduction per 10,000 printed sheets was calculated. The results are shown in Table 4.
Further, FIG. 1 and FIG. 2 are plots in which the Mv of the binder resin used is plotted on the horizontal axis and the amount of film loss per 10,000 is plotted on the vertical axis.
In addition, the photoconductors A3, A4, B3, B4, A7, A8, B7, and B8 are commercially available monochrome laser printers (manufactured by Lexmark, Optra S2450, 24 sheets per minute with A4 vertical feed, DC charging roller charging, rollers 30,000 sheets were printed at room temperature and humidity. The amount of film reduction per 10,000 sheets was calculated from the difference in film thickness before and after printing. The results are shown in Table 5.
Further, FIG. 3 and FIG. 4 show plots in which the Mv of the binder resin used is plotted on the horizontal axis and the amount of film loss per 10,000 is plotted on the vertical axis.
[0079]
[Table 4]
[0080]
[Table 5]
[0081]
【The invention's effect】
Since the polycarbonate of the present invention is superior in abrasion resistance compared to conventionally used polycarbonate, it is suitable for applications requiring heat resistance and high surface hardness. Further, by using the polycarbonate of the present invention in an electrophotographic photoreceptor, excellent electrical characteristics can be exhibited, and the abrasion resistance of the photoreceptor surface can be remarkably improved.
[Brief description of the drawings]
FIG. 1 Viscosity average molecular weight and film loss
Fig. 2 Viscosity average molecular weight and film loss
Fig. 3 Viscosity average molecular weight and film loss
[Figure 4] Viscosity average molecular weight and film loss
Claims (3)
カーボネート形成化合物とジヒドロキシ化合物とを反応させてオリゴマーを生成させ、このオリゴマーを触媒の存在下に重合させることにより製造されたポリカーボネート樹脂であって、
該触媒として塩酸塩のpKa値として7以下の塩基性度を有する化合物の塩を用い、
該ポリカーボネート樹脂におけるゲルパーミエーションクマトグラフィーにより測定したポリスチレン換算の重量平均分子量(Mw)と数平均分子量(Mn)との比(Mw/Mn)が2.4以下であり、
かつ下記式(I)で算出される粘度平均分子量(Mv)と分子末端数から算出される数平均分子量(Mn′)との比(Mv/Mn′)が1.4以下であるポリカーボネート樹脂であることを特徴とする電子写真感光体。
A polycarbonate resin produced by reacting a carbonate-forming compound and a dihydroxy compound to produce an oligomer, and polymerizing the oligomer in the presence of a catalyst ,
A salt of a compound having a basicity of 7 or less as the pKa value of hydrochloride is used as the catalyst,
The ratio (Mw / Mn) of polystyrene-equivalent weight average molecular weight (Mw) and number average molecular weight (Mn) measured by gel permeation chromatography in the polycarbonate resin is 2.4 or less,
And a polycarbonate resin having a ratio (Mv / Mn ′) of 1.4 or less of the viscosity average molecular weight (Mv) calculated by the following formula (I) and the number average molecular weight (Mn ′) calculated from the number of molecular terminals. an electrophotographic photosensitive member, characterized in that.
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