JP4092593B2 - 被乾燥物の乾燥方法及び装置 - Google Patents
被乾燥物の乾燥方法及び装置 Download PDFInfo
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- JP4092593B2 JP4092593B2 JP2007548255A JP2007548255A JP4092593B2 JP 4092593 B2 JP4092593 B2 JP 4092593B2 JP 2007548255 A JP2007548255 A JP 2007548255A JP 2007548255 A JP2007548255 A JP 2007548255A JP 4092593 B2 JP4092593 B2 JP 4092593B2
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- 238000011144 upstream manufacturing Methods 0.000 description 1
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Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
- F26B3/04—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour circulating over or surrounding the materials or objects to be dried
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B41—PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
- B41C—PROCESSES FOR THE MANUFACTURE OR REPRODUCTION OF PRINTING SURFACES
- B41C1/00—Forme preparation
- B41C1/10—Forme preparation for lithographic printing; Master sheets for transferring a lithographic image to the forme
- B41C1/1083—Mechanical aspects of off-press plate preparation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B41—PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
- B41N—PRINTING PLATES OR FOILS; MATERIALS FOR SURFACES USED IN PRINTING MACHINES FOR PRINTING, INKING, DAMPING, OR THE LIKE; PREPARING SUCH SURFACES FOR USE AND CONSERVING THEM
- B41N3/00—Preparing for use and conserving printing surfaces
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B13/00—Machines and apparatus for drying fabrics, fibres, yarns, or other materials in long lengths, with progressive movement
- F26B13/005—Seals, locks, e.g. gas barriers for web drying enclosures
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B13/00—Machines and apparatus for drying fabrics, fibres, yarns, or other materials in long lengths, with progressive movement
- F26B13/10—Arrangements for feeding, heating or supporting materials; Controlling movement, tension or position of materials
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/14—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects using gases or vapours other than air or steam, e.g. inert gases
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/005—Treatment of dryer exhaust gases
- F26B25/006—Separating volatiles, e.g. recovering solvents from dryer exhaust gases
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Drying Of Solid Materials (AREA)
Description
固形分量(%)=固形分/(揮発分+固形分)×100
である。固形分及び(揮発分+固形分)は、重量測定により求めることができる。
〔支持体〕
本発明において、被乾燥物は連続的に走行する帯状支持体に限定されることはなく、帯状以外の金属、樹脂、紙、布等も含まれる。
〔低沸点溶媒〕
本実施形態に使用される低沸点溶媒としては、沸点が30℃以上130℃以下のものが好ましい。このような低沸点溶媒としては、以下のものが挙げられるが、本発明はこれらに限定されるものではない。括弧内に沸点を記載する。
〔高沸点溶媒〕
本実施形態に使用される高沸点溶媒は、沸点が150℃以上のものが好ましい。このような高沸点溶媒のとして、以下のものが挙げられるが、本発明はこれらに限定されるものではない。括弧内に沸点を記載する。
〔塗布液〕
本発明において、塗布液に使用する溶媒は、特に限定されず、水や各種溶剤等が挙げられる。
(ノボラック樹脂)
本実施形態における画像形成層には、構造単位としてフェノール、或いは置換フェノール類を含むノボラック型フェノール樹脂(ノボラック樹脂)を含有したものを用いることができる。ノボラック樹脂は、未露光部において強い水素結合性を生起し、露光部において一部の水素結合が容易に解除されるといった点から感光層に必須のアルカリ可溶性樹脂である。このノボラック樹脂は、分子内に構造単位としてフェノール類を含むものであれば特に制限はない。
また、アルデヒド類の例としては、ホルムアルデヒド、アセトアルデヒド、アクロレイン、クロトンアルデヒド等の脂肪族及び芳香族アルデヒドが挙げられる。好ましくは、ホルムアルデヒド又はアセトアルデヒドである。
画像形成層には、赤外線吸収色素が添加される。赤外線吸収色素を添加することにより、画像形成層は赤外線レーザ感応性となる。ここで用いられる赤外線吸収剤としては、波長750nmから1,400nmに吸収極大を有し、この波長の光を吸収し熟を発生する染料であれば特に制限はなく、赤外線吸収性染料として知られる種々の染料を用いることができる。
(現像抑制剤)
画像形成層には、そのインヒビション(溶解抑制能)を高める目的で、現像抑制剤を含有させることが好ましい。
上記一般式(1)中、Rlは、多価アルコール残基又は多価フェノール残基を表し、R2は水素原子、置換基を有していても良い炭素原子数1〜25のアルキル基、アルケニル基、アルキ二ル基、アルキロイル基、アリール基又はアリーロイル基を表す。R3は置換基を有しても良いアルキレン残基を表し、mは平均で10以上、nは1〜4の整数を表す。
(その他の添加剤)
画像形成層を形成するにあたっては、上記の必須成分の他、さらに必要に応じて、種々の添加剤を添加することができる。
画像形成層には、感度を向上させる目的で、酸無水物類、フェノール類、有機酸類を添加してもよい。
画像形成層には、塗布性を良化するため、また、現像条件に対する処理の安定性を広げるため、特開昭62−251740号公報や特開平3−208514号公報に記載されているような非イオン界面活性剤、特開昭59−121044号公報、特開平4−13149号公報に記載されているような両性界面活性剤、EP950517公報に記載されているようなシロキサン系化合物、特開昭62−170950号公報、特開平11−288093号公報、特願2001−247351に記載されているようなフッ素含有のモノマー共重合体を添加することができる。
画像形成層には、露光による加熱後直ちに可視像を得るための焼き出し剤や、画像着色剤としての染料や顔料を加えることができる。
画像形成層には、塗膜の柔軟性等を付与するために可塑剤を添加しても良い。例えば、ブテルフタニル、ポリエチレングリコール、クエン酸トリブチル、フタル酸ジエチル、フタル酸ジブチル、フタル酸ジヘキシル、フタル酸ジオクチル、リン酸トリクレジル、リン酸トリブチル、リン酸トリオクチル、オレイン酸テトラヒドロフルフリル、アクリル酸又はメタクリル酸のオリゴマー及びポリマー等が用いられる。これらの可塑剤の添加量は、画像形成層の全固形分に対し、1質量%〜20質量%が好ましく、2質量%〜5質量%がより好ましい。
画像形成層には、キズに対する抵抗性を付与する目的で、表面の静摩擦係数を低下させる化合物を添加することもできる。具体的には、米国特許第6,117,913号明細書、特願2001−261627号、特願2002−032904号、特願2002−165584号の各明細書に記載されているような、長鎖アルキルカルボン酸のエステルを有する化合物などを挙げることができる。WAX剤の添加量としては、画像形成層全体に対して、0.1質量%〜10質量%が好ましく、0.5質量%〜5質量%がより好ましい。
〔マット層〕
上記のようにして設けられた画像形成層の表面には、真空焼き枠を用いた密着露光の際の真空引きの時間を短縮し、かつ、焼きボケを防止するため、マット層が設けられてもよい。具体的には、マット層を設ける方法、固体粉末を熱蒸着させる方法等が挙げられる。
〔バックコート層〕
上述したようにして得られる平版印刷版原版には、重ねても画像形成層が傷付かないように、裏面(画像形成層が設けられない側の面)に、有機高分子化合物からなる被覆層(以下「バックコート層」ともいう。)を必要に応じて設けてもよい。バックコート層の主成分としては、ガラス転移点が20℃以上の、飽和共重合ポリエステル樹脂、フェノキシ樹脂、ポリビニルアセタール樹脂および塩化ビニリデン共重合樹脂からなる群から選ばれる少なくとも1種の樹脂を用いるのが好ましい。
[実施例1−1〜1−2、比較例1−1]
まず、図6の表1に示す各条件にて、熱風乾燥部32において熱風乾燥した後、蒸気雰囲気乾燥部30において蒸気乾燥した。この熱風乾燥部32から蒸気雰囲気乾燥部30への切り替えは、塗布膜が固化した直後(乾燥点)とした。この乾燥点直後における塗布膜中の残存γ-ブチロラクトン量は、100mg/m2であった。また、ウエブ12の温度は、熱風乾燥部32における熱風乾燥温度及び乾燥時間を変えることで設定温度に調整した。また、図2の乾燥装置20の出口(熱風乾燥部34の出口)におけるウエブ12の最高到達温度を測定した。
(蒸気雰囲気乾燥部30における乾燥条件)
・アルミニウムウエブの搬送速度 :20m/分
・チャンバ38における蒸気雰囲気での乾燥時間:1.5秒
・低沸点溶媒蒸気の温度 :110℃(実施例1−2)、140℃(実施例1−1)
・低沸点溶媒蒸気の風量 :25m3/h
・高沸点溶媒:γ−ブチロラクトン
・低沸点溶媒:水(実施例1−1)、MEK(メチルエチルケトン、実施例1−2)
(残留高沸点溶媒量の測定方法)
アルミニウムウエブ上に塗布した塗布膜サンプルを、アルミニウムウエブごと30mm×10mmに切り出し、バイヤル瓶に入れて密閉した。このバイヤル瓶を専用の装置に投入して、180℃で5分間加熱した後、装置内に装備されているシリンジでバイヤル瓶中の気体の一部を取り出し、ガスクロマトグラフィで分析した。得られたクロマトグラムのピーク面積とあらかじめ用意しておいた検量線とから塗布膜中に残留していた溶媒の濃度を算出した。
[実施例2−1〜2−6、比較例2−1〜2−6]
図7の表2に示す各条件にて、熱風乾燥部32において熱風乾燥した後、蒸気雰囲気乾燥部30において蒸気乾燥した。この熱風乾燥部32から蒸気雰囲気乾燥部30への切り替えは、塗布膜が固化した直後(乾燥点)とした。この乾燥点直後における塗布膜中の残存γ-ブチロラクトン量は、100mg/m2であった。また、ウエブ12の温度は、熱風乾燥部32における熱風乾燥温度及び乾燥時間を変えることで設定温度に調整した。なお、ウエブ12としては、上記実施例1−1と同様のものを使用した。
(蒸気雰囲気乾燥部30における乾燥条件)
・アルミニウムウエブの搬送速度 :20m/分
・チャンバ38における蒸気雰囲気での乾燥時間:1.5秒
・低沸点溶媒を含む加熱エアの温度 :140℃
・低沸点溶媒蒸気を含む加熱エアの風量 :25m3/h
・高沸点溶媒:γ−ブチロラクトン
・低沸点溶媒:水
残留高沸点溶媒量の測定方法は、上記実施例1と同様の方法で行った。この結果を、図7の表2にまとめた。
Claims (14)
- 第1の溶媒を含む被乾燥物を搬送させながら乾燥する被乾燥物の乾燥方法であって、
前記被乾燥物を乾燥点まで乾燥する第1の乾燥工程と、
前記第1の乾燥工程の後段の乾燥チャンバ内において、前記第1の溶媒よりも沸点の低い第2の溶媒の蒸気雰囲気を形成すると共に、前記乾燥チャンバの入口における前記被乾燥物の品温が前記蒸気雰囲気の温度に対して所定の温度差を有して低くなるようにして乾燥させる第2の乾燥工程と、
を備えたことを特徴とする被乾燥物の乾燥方法。 - 前記温度差は5〜100℃の範囲であることを特徴とする請求項1の被乾燥物の乾燥方法。
- 前記第2の溶媒の蒸気量をC[g/m3]、前記被乾燥物の品温をT[℃]、T[℃]での前記第2の溶媒の飽和蒸気圧をPT[Pa]、前記第2の溶媒の分子量をM、気体定数をR(8.31Pa・m3/(mol・K))とすると、
0.25≦CR(273.15+T)/(PT×M)<1.0
を満たすことを特徴とする請求項1又は2の被乾燥物の乾燥方法。 - 前記第2の溶媒の蒸気雰囲気の温度と前記被乾燥物の品温とを検出する温度検出ステップと、
前記温度検出ステップで得られた検出結果に基づいて、前記被乾燥物の品温が前記蒸気雰囲気の温度に対して所定の温度差を有して低くなるように前記被乾燥物の品温及び/又は前記第2の溶媒の蒸気雰囲気の温度を制御する温度制御ステップと、
を備えたことを特徴とする請求項1〜3の何れか1の被乾燥物の乾燥方法。 - 前記第2の溶媒の蒸気雰囲気を形成する乾燥チャンバ内における前記第2の溶媒の蒸気量を検出する蒸気量検出ステップと、
前記蒸気量検出ステップで得られた検出結果に基づいて、前記乾燥チャンバ内の前記第2の溶媒の蒸気量が所定の範囲になるように、前記乾燥チャンバ内に供給する前記第2の溶媒の蒸気量を制御する蒸気量制御ステップと、
を備えたことを特徴とする請求項1〜4の何れか1の被乾燥物の乾燥方法。 - 請求項1〜5の何れか1の被乾燥物の乾燥方法を適用したことを特徴とする平版印刷版原版の製造方法。
- 第1の溶媒を含む被乾燥物を搬送させながら乾燥する被乾燥物の乾燥装置であって、
前記被乾燥物を乾燥点まで乾燥する第1の乾燥部と、
前記第1の乾燥部の後段に設けられた乾燥チャンバ内において、前記第1の溶媒よりも沸点の低い第2の溶媒の蒸気雰囲気を形成すると共に、前記乾燥チャンバの入口における前記被乾燥物の品温が前記蒸気雰囲気の温度に対して所定の温度差を有して低くなるようにして乾燥させる第2の乾燥部と、
を備えたことを特徴とする被乾燥物の乾燥装置。 - 前記第2の乾燥部は、
前記第1の溶媒よりも沸点の低い第2の溶媒の蒸気を生成し、前記乾燥チャンバ内に前記第2の溶媒の蒸気雰囲気を形成するための溶媒蒸気生成手段と、
前記乾燥チャンバ内の被乾燥物を加熱する加熱手段と、
前記乾燥チャンバ入口における前記第2の溶媒の蒸気雰囲気の温度と前記被乾燥物の品温を検出するための温度検出手段と、
該温度検出手段の検出結果に基づいて、前記乾燥チャンバ入口における前記被乾燥物の品温が前記蒸気雰囲気の温度に対して所定の温度差を有して低くなるように、前記加熱手段を制御する制御手段と、
を備えたことを特徴とする請求項7の被乾燥物の乾燥装置。 - 前記乾燥チャンバの前段に、前記被乾燥物を冷却する冷却手段を備え、
前記温度検出手段の検出結果に基づいて、前記乾燥チャンバ入口における前記被乾燥物の品温が前記蒸気雰囲気の温度に対して所定の温度差を有して低くなるように、前記制御手段が前記冷却手段を制御することを特徴とする請求項8の被乾燥物の乾燥装置。 - 前記乾燥チャンバ内の前記第2の溶媒の蒸気量を検出する蒸気量検出手段と、
前記蒸気量検出手段の検出結果に基づいて、前記乾燥チャンバ内における前記第2の溶媒の蒸気量が所定の範囲になるように、前記乾燥チャンバ内に供給する前記第2の溶媒の蒸気量を制御する蒸気量制御手段と、
を備えたことを特徴とする請求項8又は9の被乾燥物の乾燥装置。 - 前記乾燥チャンバ入口及び出口にエアカーテンを形成するためのエアカーテン形成手段を備えたことを特徴とする請求項8〜10の何れか1の被乾燥物の乾燥装置。
- 前記溶媒蒸気生成手段に供給する前記第2の溶媒を貯留するための溶媒貯留槽と、
前記乾燥チャンバ内から排気した蒸気雰囲気から前記第2の溶媒を分離するための分離手段と、
該分離手段で分離した第2の溶媒を前記溶媒貯留槽に戻すための循環配管と、
を備えたことを特徴とする請求項8〜11の何れか1の被乾燥物の乾燥装置。 - 前記第2の乾燥部の後段には、前記被乾燥物を熱風乾燥する第3の乾燥部が設けられたことを特徴とする請求項7〜12の何れか1の被乾燥物の乾燥装置。
- 請求項7〜13の何れか1の被乾燥物の乾燥装置を備えたことを特徴とする平版印刷版原版の製造装置。
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US (1) | US8196312B2 (ja) |
EP (1) | EP1967803B1 (ja) |
JP (1) | JP4092593B2 (ja) |
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KR101309055B1 (ko) | 2013-09-16 |
JPWO2007136005A1 (ja) | 2009-10-01 |
KR20090009771A (ko) | 2009-01-23 |
CN101360965B (zh) | 2010-12-22 |
WO2007136005A1 (ja) | 2007-11-29 |
CN101360965A (zh) | 2009-02-04 |
EP1967803A4 (en) | 2014-05-07 |
EP1967803A1 (en) | 2008-09-10 |
US20100058609A1 (en) | 2010-03-11 |
US8196312B2 (en) | 2012-06-12 |
EP1967803B1 (en) | 2016-09-28 |
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