JPH0229476A - Production of high-viscosity printing ink and dehydrator - Google Patents

Production of high-viscosity printing ink and dehydrator

Info

Publication number
JPH0229476A
JPH0229476A JP63179444A JP17944488A JPH0229476A JP H0229476 A JPH0229476 A JP H0229476A JP 63179444 A JP63179444 A JP 63179444A JP 17944488 A JP17944488 A JP 17944488A JP H0229476 A JPH0229476 A JP H0229476A
Authority
JP
Japan
Prior art keywords
heat
printing ink
mixture
wall
paste
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.)
Pending
Application number
JP63179444A
Other languages
Japanese (ja)
Inventor
Toru Kawada
徹 川田
Shunichi Oshida
俊一 押田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toyo Ink SC Holdings Co Ltd
Original Assignee
Toyo Ink Mfg Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Toyo Ink Mfg Co Ltd filed Critical Toyo Ink Mfg Co Ltd
Priority to JP63179444A priority Critical patent/JPH0229476A/en
Publication of JPH0229476A publication Critical patent/JPH0229476A/en
Pending legal-status Critical Current

Links

Landscapes

  • Inks, Pencil-Leads, Or Crayons (AREA)

Abstract

PURPOSE:To produce the title high-quality ink without causing any compositional unevenness, local solidification or film formation of the mixture by using a heat pipe in which induction heating is employed as a heat source as an external heating means in performing dehydration with a dehydrator after primary dehydration is performed by flushing. CONSTITUTION:A mixture of an aqueous pigment slurry or paste with a printing ink vehicle is dehydrated to about 5-10wt.% by the primary dehydration through flushing and is sent to a dehydrator, where it is agitated and transferred. During this time, the mixture is heated with a heat controller 15 while it is dehydrated by evacuation through an exhaust pipe. When a coil 17 is energized, the generated magnetic line of force causes the carbon steel 22 of the wall 2 comprising a ferromagnetic material to generate heat, and the generated heat is transferred to a heat pipe 16 to heat the working fluid sealed in it. The heated fluid liberates heat, condenses at the upper end and returns to the heat absorption part. By the heat generation of the wall 21 itself and the distribution of heat by the heat pipe 16, the temperature distribution of the wall 21 is uniformized, and the mixture in the inside space 3 can be uniformly heated.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は高粘度印刷インキの製造法及び水分除去装置に
関し、より詳しくはフラッシングによる一次脱水後、水
分を薄膜脱水装置で除去する際、外部加熱手段として誘
導加熱を熱源とするヒートバイブによることを特徴とす
る製造法及びそれに使用する水分除去装置に関する。
Detailed Description of the Invention [Industrial Application Field] The present invention relates to a method for producing high viscosity printing ink and a water removal device, and more specifically, after primary dehydration by flushing, when water is removed by a thin film dehydration device, external The present invention relates to a manufacturing method characterized in that a heat vibrator using induction heating as a heat source is used as a heating means, and a moisture removal device used therein.

[従来の技術] オフはット印刷インキなどの高粘度印刷インキは、顔料
とベヒクルとを混合し、三本ローラによって練肉する方
法と、顔料の水性スラリー若しくはペーストと印刷イン
キ用ベヒクルとを用いてフラッシングする方法とがある
。後者は透明性を要求され、かつ大量生産することので
きるプロセスインキの製造に適用されている。
[Prior art] High viscosity printing inks such as off-hat printing inks can be produced by mixing a pigment and a vehicle and kneading the mixture using three rollers, or by mixing an aqueous slurry or paste of pigment with a vehicle for printing ink. There is a method of flushing using The latter is applied to the production of process inks that require transparency and can be mass-produced.

このフラッシング法は、−次脱水によって通常5〜10
%(単1)の水分含右呈となり、引き続き減圧下に加熱
しながら混合して最終的には1%以下、好ましくは0.
5%程度とする必要があり、このために処理に数時間も
の長時間を必要とし、製造の合理化が望まれている。こ
のため後記するような薄膜蒸発装置によって一次脱水後
のペーストを処理する工程が本発明者らによって試みら
れていた。
This flushing method usually requires 5 to 10
The water content becomes 1% (unit 1), and by subsequently mixing while heating under reduced pressure, the final content is 1% or less, preferably 0.5%.
It needs to be about 5%, which requires a long processing time of several hours, and rationalization of manufacturing is desired. For this reason, the present inventors have attempted a process of treating the paste after primary dehydration using a thin film evaporator as described later.

しかし、市販の薄膜蒸発装置は外部熱源として水蒸気に
よって外部ジャケラ1〜から加熱する方式しかないため
、部分加熱が生じやすく種々の欠点があった。
However, commercially available thin film evaporators have only a method of heating from the external jacket 1 by using water vapor as an external heat source, and therefore have various drawbacks in that partial heating tends to occur.

すなわち、−次脱水後のペーストを薄膜蒸発装置で処理
する場合は、ペーストの上部では水分が多く、下部では
少ないので上部と下部では理想的な加熱条件が責なって
おり、また、加熱が不均一になってペーストにローカル
ヒーティング(local heating )を生じ
るとペースト中の溶剤が局部的に揮発し、組成の不均一
の原因となり、更に局部的に固化して異物となったり、
局部的な被膜の発生の原因となる。
In other words, when the paste after secondary dehydration is processed using a thin film evaporator, the upper part of the paste has more water and the lower part has less water, so ideal heating conditions are responsible for the upper and lower parts. When the paste becomes uniform and local heating occurs in the paste, the solvent in the paste evaporates locally, causing non-uniformity of the composition, and further locally solidifying and becoming foreign matter.
Causes localized film formation.

このようなことから、薄膜蒸発装置の加熱装置としては
温度の制御幅が広く、かつ均一な加熱が可能であること
が望まれている。
For this reason, it is desired that a heating device for a thin film evaporator be capable of wide temperature control and uniform heating.

[発明が解決しようとする課題] しかるに前記従来の水蒸気を外部ジャケラ1−に導いて
加熱する方式では、加熱温度の微調整は困難であるし、
また、水蒸気であるため100℃以下での温度制御は不
可能であって、温度の制御幅が狭い範囲で使用せざるを
(qない。
[Problems to be Solved by the Invention] However, in the conventional method of introducing steam to the external jacket 1- for heating, fine adjustment of the heating temperature is difficult;
Furthermore, since it is water vapor, it is impossible to control the temperature below 100°C, so it has to be used within a narrow temperature control range.

本発明は上記の如き事情に鑑みてなされたものであって
、フラッシングによる一次脱水後に薄膜蒸発装置によっ
て二次脱水する上記製造法を改良し、制御節回が広く、
かつ微調整が可能であって、必要な加熱制御を実理する
ことができ、従って、プロセスインキの品質を向上させ
1qる高粘度印刷インキの製造法及び水分除去装置を提
供することを目的とするものである。
The present invention has been made in view of the above-mentioned circumstances, and improves the above-mentioned manufacturing method in which primary dehydration by flushing is followed by secondary dehydration using a thin film evaporator.
The purpose of the present invention is to provide a method for producing a high viscosity printing ink and a water removal device that can be finely adjusted and implement the necessary heating control, thereby improving the quality of the process ink. It is something to do.

[課題を解決するための手段] この目的に対応して、この発明の高粘度印刷インキのy
 B法は、顔料の水性スラリー若しくはペーストと印刷
インキ用ベヒクルとを用いてフラッシングし、−次脱水
したペーストを、縦型円筒、この円筒の中心にある回転
軸、この回転軸に取りつけられた攪拌移送手段、減圧手
段および外部加熱手段を備えてなる水分除去装置によっ
て残存水分を除去する工程を含む高粘度印刷インキの製
造法において、前記水分除去装置の外部加熱手段の少な
くとも1つとして、誘導加熱を熱源とするヒートパイプ
によることを特徴としている。
[Means for Solving the Problem] Corresponding to this purpose, the high viscosity printing ink of the present invention
Method B involves flushing with an aqueous slurry or paste of pigment and a vehicle for printing ink, and then transferring the dehydrated paste to a vertical cylinder, a rotating shaft in the center of the cylinder, and a stirring shaft attached to the rotating shaft. A method for producing a high viscosity printing ink comprising a step of removing residual moisture by a moisture removal device comprising a transfer means, a pressure reduction means, and an external heating means, wherein at least one of the external heating means of the moisture removal device includes induction heating. It is characterized by using a heat pipe as a heat source.

また、この発明の高粘度印刷インキの水分除去装置は、
縦型円筒の胴部と、複数の円筒状部分が軸方向に連結し
て形成されかつ内部に攪拌移送手段を設置可能な縦型円
筒の胴部を有し、前記円筒状部分の外側に誘導コイルが
配設され、前記円筒状部分の壁部は前記誘導コイルによ
り発生した磁界により発熱する強磁性材料を含み、前記
壁部にヒートパイプが配設されていることを特徴として
いる。
In addition, the high viscosity printing ink moisture removal device of this invention includes:
It has a vertical cylindrical body and a plurality of cylindrical parts connected in the axial direction, and has a vertical cylindrical body in which an agitation transfer means can be installed, and is guided to the outside of the cylindrical part. A coil is disposed, the wall of the cylindrical portion includes a ferromagnetic material that generates heat due to the magnetic field generated by the induction coil, and a heat pipe is disposed on the wall.

[作用] 顔料の水性スラリー若しくはペース1〜と印刷インキ用
ベヒクルとの混合物はフラッシングによる一次脱水によ
って水分が5〜10%(重量)に調整された後、水分除
去装置に送り込まれ、ここで攪拌移送される。この間、
混合物には、胴部壁の誘導発熱とヒートパイプによる伝
熱によって所望の加熱が与えられつつ真空脱水される。
[Function] The mixture of the pigment aqueous slurry or paste 1~ and the printing ink vehicle is first dehydrated by flushing to adjust the water content to 5 to 10% (by weight), and then sent to a water removal device where it is stirred. be transported. During this time,
The mixture is vacuum dehydrated while being given the desired heating by induction heat generation in the body wall and heat transfer by the heat pipe.

[実施例1 第1図から第3図にはこの発明の高粘度印刷インキの製
造法において使用する水分除去装置が示されている。水
分除去装置1は縦型円筒状の胴部2を有する。胴部2は
円筒状の内部空間3を有する。内部空間3は上端の蒸気
部4、中央部の攪拌移送部5及び下端の排出部6とから
なっている。
[Example 1] Figures 1 to 3 show a water removal device used in the method for producing high viscosity printing ink of the present invention. The moisture removal device 1 has a body 2 having a vertical cylindrical shape. The body 2 has a cylindrical internal space 3. The internal space 3 consists of a steam section 4 at the upper end, an agitation transfer section 5 at the center, and a discharge section 6 at the lower end.

蒸気部4には供給管7が接続し、排出部6に排出管8が
接続している。また、蒸気部4には排気管11が接続し
ている。内部空間3内には蓋9を口過して軸方向に回転
軸12が挿通されており、この回転軸12には攪拌移送
部5内において攪拌移送ブレード13が取付けられてい
る。
A supply pipe 7 is connected to the steam section 4, and a discharge pipe 8 is connected to the discharge section 6. Further, an exhaust pipe 11 is connected to the steam section 4. A rotating shaft 12 is inserted into the internal space 3 in the axial direction through the lid 9, and a stirring transfer blade 13 is attached to the rotating shaft 12 in the stirring transfer section 5.

胴部2は複数の円in状部分くこの実施例の場合は4個
の円筒状部分2a、2b、2c、及び2d)が軸方向に
連結して形成されている。円筒状部分2aは蒸気部4に
対応し、円筒状部分2b、2cは攪拌移送部5に対応し
、円筒状部分2dはJjl出部6に対応する。円筒状部
分2aには前記の供給管7及び排気管11が接続し、円
筒状部分2dには排出管8が接続する。特に重要なこと
として、円筒状部分2b、2Gには加熱制御装置14b
114cが取付けられている。排出部6にも同様の加熱
制御装置14dを取付【プてもよい。
The body portion 2 is formed by connecting a plurality of circular in-shaped portions (in the case of this embodiment, four cylindrical portions 2a, 2b, 2c, and 2d) in the axial direction. The cylindrical portion 2 a corresponds to the steam section 4 , the cylindrical portions 2 b and 2 c correspond to the stirring transfer section 5 , and the cylindrical section 2 d corresponds to the JJI outlet section 6 . The aforementioned supply pipe 7 and exhaust pipe 11 are connected to the cylindrical portion 2a, and the exhaust pipe 8 is connected to the cylindrical portion 2d. Particularly important is that the cylindrical portions 2b, 2G have a heating control device 14b.
114c is installed. A similar heating control device 14d may also be attached to the discharge section 6.

加熱制御装置14b〜1/1dは互いにほぼ同様の構成
であるので、以下には円筒状部分2bに設けられている
加熱制御装置14bについて説明する。
Since the heating control devices 14b to 1/1d have substantially the same configuration, the heating control device 14b provided in the cylindrical portion 2b will be described below.

加熱制御装置14bは誘導加熱装置15と複数のヒート
パイプ16を備えている。誘導加熱装置15はコイル1
7及び鉄心18を有する。この誘導加熱装置15自体は
公知であって、市販のものを使用することができる。
The heating control device 14b includes an induction heating device 15 and a plurality of heat pipes 16. The induction heating device 15 has a coil 1
7 and an iron core 18. This induction heating device 15 itself is publicly known, and a commercially available device can be used.

円筒状部分2bの壁部21が誘導加熱装置15の加熱の
対象であり、従って、壁部21は強磁性体で構成する必
要がある。このために、壁部21は炭素tA22を両側
からステンレス123.24で被覆したクラツド鋼を使
用して構成する。壁部21の外側をコイル17が取巻き
、その外側に鉄心18が位置する。
The wall 21 of the cylindrical portion 2b is the object of heating by the induction heating device 15, and therefore the wall 21 must be made of ferromagnetic material. For this purpose, the wall portion 21 is constructed using clad steel with carbon tA22 coated on both sides with stainless steel 123.24. A coil 17 surrounds the outside of the wall portion 21, and an iron core 18 is located outside the coil 17.

一方、ヒートパイプ16は所定のピッチで壁部21内に
埋め込まれている。
On the other hand, the heat pipes 16 are embedded within the wall portion 21 at a predetermined pitch.

円筒状部分2c、2dについての加熱制御装置1/Ic
、14dも同様である。
Heating control device 1/Ic for cylindrical portions 2c and 2d
, 14d are also the same.

この発明の高粘度印刷インキの製造法は以上説明した水
分除去装置1を使用して次のようにしてなされる。
The method for producing high viscosity printing ink of the present invention is carried out as follows using the moisture removal device 1 described above.

プロセスインキの成分となる水性スラリー若しくはベー
ストと印刷インキ用ベヒクルとの混合体は、フラッシン
グ法における一次脱水によって5〜10%(fiffl
)の水分含有量に脱水され、この状態で供給管7から胴
部2の内部空間3内に供給され、攪拌移送部5において
攪拌移送ブレード13によって攪拌されつつ、排出部6
に移送される。
A mixture of an aqueous slurry or base, which is a component of a process ink, and a printing ink vehicle is prepared by primary dehydration in a flashing method to produce a 5-10% (fiffl)
), and in this state is supplied from the supply pipe 7 into the internal space 3 of the body 2, and is stirred by the agitation transfer blade 13 in the agitation transfer section 5, and then transferred to the discharge section 6.
will be transferred to.

この間、被処理混合物である混合物は加熱制御装置15
に加熱され、かつ排気管11からの排気によって脱水さ
れる。
During this time, the mixture to be treated is heated by the heating control device 15.
and is dehydrated by exhaust air from the exhaust pipe 11.

加熱制御装置15の動作は次の通りである。The operation of the heating control device 15 is as follows.

コイル7を発振器(図示せず)を使用して励磁すると、
コイル17から発生した磁力線は強磁性材料からなる壁
部21の炭素鋼22を通って磁気回路を構成し、炭素鋼
22が発熱する。この炭素鋼22の発熱はヒートパイプ
16に伝えられる。
When the coil 7 is excited using an oscillator (not shown),
The magnetic lines of force generated from the coil 17 pass through the carbon steel 22 of the wall portion 21 made of ferromagnetic material to form a magnetic circuit, and the carbon steel 22 generates heat. This heat generated by the carbon steel 22 is transmitted to the heat pipe 16.

ζ−ドパイブ16では、吸熱部が炭素鋼22で加熱され
、内部に封入した作動液が熱せられて蒸発し、冷却部で
ある上端に向って流れ、上端部で潜熱を放出して凝縮し
、作動液が吸熱部に戻る。こうして、壁部21自体の発
熱と、これに加えて、ヒートパイプ16による熱の分配
により、壁部21の温度分布は均一化され、内部空間3
内の混合物に対する加熱は均、−に行われる。
In the ζ-dopibe 16, the heat absorbing part is heated by the carbon steel 22, and the working fluid sealed inside is heated and evaporated, flows toward the upper end which is the cooling part, releases latent heat at the upper end, and condenses. The working fluid returns to the heat absorption section. In this way, the temperature distribution of the wall part 21 is made uniform due to the heat generated by the wall part 21 itself and the heat distribution by the heat pipe 16, and in addition to this, the temperature distribution of the wall part 21 is made uniform, and the internal space 3
The mixture within is heated evenly.

一方、このような加熱制御装置をもつ円筒状部分2b、
2c、2dは軸方向に積み重ねられており、この場合に
、それぞれの円筒状部分2b。
On the other hand, a cylindrical portion 2b having such a heating control device,
2c, 2d are axially stacked, in this case the respective cylindrical part 2b.

2c、2dにおける加熱制御装置14b、14c。Heating control devices 14b, 14c in 2c, 2d.

14dは独立に温度制御可能であるから、内部空間3の
軸方向においては、任愈の温度分布を形成することがで
きる。またそれぞれの加熱制御装置における発熱量は発
振器の出力を調整することによって変更でき、微調整も
可能である。
14d can be independently temperature controlled, so that an arbitrary temperature distribution can be formed in the axial direction of the internal space 3. Further, the amount of heat generated in each heating control device can be changed by adjusting the output of the oscillator, and fine adjustment is also possible.

攪拌移送部5における脱水が終了して排出部6に達した
混合物は排出管8から排出される。
The mixture that has been dehydrated in the agitation transfer section 5 and has reached the discharge section 6 is discharged from the discharge pipe 8.

[発明の効果1 この発明の高粘度印刷インキの製造法及び水分除去装置
では、胴部の周囲に蒸気ジャケットを設ける必要がない
ので装置の構成を簡単にすることができる。しかもM 
Q加熱を利用するために発振器の出力をダイAフルで調
整するだけで広範囲の温度制御が可能となり、かつ微調
整も可能どなる。
[Advantageous Effects of the Invention 1] In the high viscosity printing ink manufacturing method and water removal device of the present invention, there is no need to provide a steam jacket around the body, so the structure of the device can be simplified. Moreover, M
In order to utilize Q heating, a wide range of temperature control is possible by simply adjusting the output of the oscillator with the die A full, and fine adjustment is also possible.

更に、胴部の軸方向で加熱制御装置を分割して独立に制
御することが可能どなり、これによって軸方向に所望の
温度分布を形成することができる。
Furthermore, it becomes possible to divide the heating control device in the axial direction of the body and control it independently, thereby making it possible to form a desired temperature distribution in the axial direction.

このことから、混合物を理想的な温度分布で処理するこ
とができ、混合物の組成の不均一や局部的な固化や被膜
発生によるインキの品質低下を防ぐことができる。
Therefore, the mixture can be treated with ideal temperature distribution, and deterioration in ink quality due to uneven composition of the mixture, local solidification, or film formation can be prevented.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はこの発明の一実施例に係わる水分除去装置の正
面説明図、第2図は加熱制御装置の縦断面説明図、及び
第3図は第2図における■−■部所面説明図である。 2・・・胴部 2a、2b、2c、2d−・・円筒状部分3・・・内部
空間 4・・・蒸気部 5・・・攪拌移送部 6・・・排出部 7・・・供給管 8・・・排出管 11・・・排気管 12・・・回転軸 13・・・攪拌移送ブレード 14b、14c、14d・・・加熱制御装置15・・・
誘導加熱装置 16・・・ヒートバイブ 17・・・コイル 18・・・鉄心 21・・・壁部 22・・・炭素鋼 23.24・・・ステンレス鋼 1・・・水分除去装罫
FIG. 1 is an explanatory front view of a moisture removal device according to an embodiment of the present invention, FIG. 2 is an explanatory longitudinal cross-sectional view of a heating control device, and FIG. 3 is an explanatory view of the section ■-■ in FIG. 2. It is. 2...Body portions 2a, 2b, 2c, 2d--Cylindrical portion 3...Inner space 4...Steam section 5...Agitation transfer section 6...Discharge section 7...Supply pipe 8... Discharge pipe 11... Exhaust pipe 12... Rotating shaft 13... Stirring transfer blades 14b, 14c, 14d... Heating control device 15...
Induction heating device 16...Heat vibrator 17...Coil 18...Iron core 21...Wall portion 22...Carbon steel 23.24...Stainless steel 1...Moisture removal rule

Claims (2)

【特許請求の範囲】[Claims] (1)顔料の水性スラリー若しくはペーストと印刷イン
キ用ベヒクルとを用いてフラッシングし、一次脱水した
ペーストを、縦型円筒、この円筒の中心にある回転軸、
この回転軸に取りつけられた攪拌移送手段、減圧手段お
よび外部加熱手段を備えてなる水分除去装置によって残
存水分を除去する工程を含む高粘度印刷インキの製造法
において、前記水分除去装置の外部加熱手段の少なくと
も1つとして、誘導加熱を熱源とするヒートパイプによ
ることを特徴とする高粘度印刷インキの製造法。
(1) The paste, which has been flushed with an aqueous slurry or paste of pigment and a vehicle for printing ink and has been primarily dehydrated, is placed in a vertical cylinder, with a rotating shaft in the center of the cylinder;
In the method for producing high viscosity printing ink, the method includes the step of removing residual moisture by a moisture removal device that is equipped with an agitation transfer device, a pressure reduction device, and an external heating device, which are attached to the rotating shaft, and an external heating device of the moisture removal device. A method for producing a high viscosity printing ink, characterized in that at least one of the above uses a heat pipe using induction heating as a heat source.
(2)縦型円筒の胴部と、複数の円筒状部分が軸方向に
連結して形成されかつ内部に撹拌移送手段を設置可能な
縦型円筒の胴部を有し、前記円筒状部分の外側に誘導コ
イルが配設され、前記円筒状部分の壁部は前記誘導コイ
ルにより発生した磁界により発熱する強磁性材料を含み
、前記壁部にヒートパイプが配設されていることを特徴
とする高粘度印刷インキの水分除去装置
(2) It has a vertical cylindrical body and a plurality of cylindrical parts connected in the axial direction, and has a vertical cylindrical body in which an agitation and transfer means can be installed; An induction coil is disposed on the outside, a wall of the cylindrical portion includes a ferromagnetic material that generates heat due to the magnetic field generated by the induction coil, and a heat pipe is disposed on the wall. High viscosity printing ink moisture removal equipment
JP63179444A 1988-07-19 1988-07-19 Production of high-viscosity printing ink and dehydrator Pending JPH0229476A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63179444A JPH0229476A (en) 1988-07-19 1988-07-19 Production of high-viscosity printing ink and dehydrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63179444A JPH0229476A (en) 1988-07-19 1988-07-19 Production of high-viscosity printing ink and dehydrator

Publications (1)

Publication Number Publication Date
JPH0229476A true JPH0229476A (en) 1990-01-31

Family

ID=16065968

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63179444A Pending JPH0229476A (en) 1988-07-19 1988-07-19 Production of high-viscosity printing ink and dehydrator

Country Status (1)

Country Link
JP (1) JPH0229476A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002040606A3 (en) * 2000-11-17 2002-12-19 Buehler Ag Method and device for producing printing inks
WO2004096482A1 (en) * 2003-05-02 2004-11-11 Kba-Giori S.A. Machine and process for cutting openings in a substrate

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002040606A3 (en) * 2000-11-17 2002-12-19 Buehler Ag Method and device for producing printing inks
WO2004096482A1 (en) * 2003-05-02 2004-11-11 Kba-Giori S.A. Machine and process for cutting openings in a substrate

Similar Documents

Publication Publication Date Title
JPH0229476A (en) Production of high-viscosity printing ink and dehydrator
JPH02222498A (en) Method for continuously drying paste raw material for high-density detergent
EP0864535B1 (en) Process and apparatus for evaporation of saline solutions
JPH11324324A (en) Method and device for mixing carbon dioxide with concrete
US2677504A (en) Method of mixing, vacuum drying, and pulverizing an ortho-cellutone dye
AU631063B2 (en) Digestion method and installation with preheating of lignocellulose materials in solid phase
EP0122289B1 (en) Process for improving the solubility of a difficultly soluble gelling agent
US4187616A (en) Method for cooling aged board material
US3527447A (en) Process for the preparation of calcined gypsum
CN210385830U (en) Reation kettle is used in thiamine ester production
JPS5686757A (en) High speed flushing device in flexo graphic press
US1728495A (en) Cement-grinding mill
JP2003509219A (en) Pretreatment method of casting sand for casting and apparatus therefor
JPS6443337A (en) Continuous medium-type dispersing and stirring machine
JPH04320658A (en) Preparation of soybean milk coagulation
JPH01139174A (en) Coating of coating material and its ageing method
CN210906181U (en) Unsaturated polyester resin is reation kettle for equipment
JP2005127555A (en) Microwave drying device
JPS58141332A (en) Uniform cooling method for tubular body
CN211198623U (en) Energy-conserving heating device of nanometer calcium carbonate boiled thick liquid surface treatment
JPH08252505A (en) Preparation of slurry of separation agent for annealing of electrical steel sheet and its applicator
JP2002080249A (en) Hydrated lime and method of producing the same
JP2000015296A (en) Vacuum evaporation type dehydrator in which sludge is charged directly into vacuum can body, heat-treated, and dehydrated by vacuum evaporation
JP3359049B2 (en) Apparatus for manufacturing porous pipe whose surface is selectively plasma-treated, and porous pipe manufactured by this manufacturing apparatus
JP2002361298A (en) Method for treating brewer's sludge and pretreatment apparatus used therein