JPH03504621A - Manufacturing method of dry molded fibrous material - Google Patents
Manufacturing method of dry molded fibrous materialInfo
- Publication number
- JPH03504621A JPH03504621A JP50620889A JP50620889A JPH03504621A JP H03504621 A JPH03504621 A JP H03504621A JP 50620889 A JP50620889 A JP 50620889A JP 50620889 A JP50620889 A JP 50620889A JP H03504621 A JPH03504621 A JP H03504621A
- Authority
- JP
- Japan
- Prior art keywords
- binder
- manufacturing
- processing
- grade
- material web
- 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
Links
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F9/00—Complete machines for making continuous webs of paper
Landscapes
- Paper (AREA)
- Multicomponent Fibers (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】 乾式成形繊維材の製法 本発明は乾式成形繊維材ウェブの製法に係わる。[Detailed description of the invention] Manufacturing method of dry molded fibrous material The present invention relates to a method of making a dry formed fibrous web.
本発明の好ましい実施例としてセルロース繊維ウェブ即ち、いわゆる乾式成形紙 または乾式成形ティシュ−の製法を以下に説明するが、本発明の方法はその他の 種類の繊維ウェブの製造にも応用できることはいうまでもない。A preferred embodiment of the invention is a cellulosic fibrous web, i.e. a so-called dry-formed paper. A method for producing a dry-molded tissue will be described below, but the method of the present invention is applicable to other methods. Needless to say, it can also be applied to the production of various types of fibrous webs.
構造及び性質の異なるウェブを製造したい場合、材料が従来のようにワンステッ プで処理されてしまうと、品質間の切換えに幾つかの問題がある。規定のグレー ドを維持するためにはある程度の調整時間が必要であり、この調整時間にわたっ て製品としてのグレードから外れた、従って不合格品として除外せざるを得ない 製品が製造される。収益性を高め、単位量の合格品の生産に要するコストを抑え るためには個々のグレードごとに長時間稼動させねばならない。このことは設備 経費の大きい量産プラントにおいて余計なコストと能率損を招くことを意味する 。典型的な例として、引渡される製品としておそらくは10通りにも及ぶカラー のものを製造しなければならない紙ナプキンの場合が考えられる。クリーニング に費やされるグレード切換え時間は生産性の高い製紙設備の“生産性を低下させ る”だけでなく、コストと手間を増大させる。設備利用度を高くするには生産ル ーチンの作成等の手段によって慎重な生産プランを練らねばならない。しかし、 このような生産方式は個々のグレードに関するマーケット需要に対応する融通性 に乏しい。If you want to produce webs with different structures and properties, the materials can be There are some problems with switching between qualities once they are processed in a single file. Default gray A certain amount of adjustment time is required to maintain the Therefore, it has no choice but to be excluded as a rejected product. The product is manufactured. Increase profitability and reduce costs required to produce a unit quantity of acceptable products In order to achieve this goal, each grade must be operated for a long time. This is equipment This means extra costs and efficiency losses in expensive mass production plants. . As a typical example, the delivered product may have as many as 10 different colors. Consider the case of paper napkins, which require the production of cleaning The grade changeover time spent in This not only increases costs and labor, but also increases cost and effort. A careful production plan must be drawn up by means such as creating a new process. but, This production system provides flexibility to meet market demands for individual grades. Poor.
本発明の目的の1つは乾式成形材料に関連して上述した公知の製法に伴なう不都 合を解消する製法を達成することにある。One of the objects of the present invention is to solve the disadvantages associated with the above-mentioned known manufacturing methods in connection with dry molding materials. The objective is to develop a manufacturing method that eliminates the problem of
本発明は製造工程を互いに分離された少なくとも2つのステップに分けることで 上記問題を経済的かつ合理的に解決する。ステップ1では凝集状態にある取扱い 易いウェブを得るのに必要な標準的成分を除いて色材や化学添加物を含まない素 材を形成する。次のステップ、即ち、ステップ2ではこの素材を所要の仕上がり グレードまで加工する。このようにして極めてすぐれた融通性と生産コスト軽減 が達成される。ステップ1では白色素材を扱うだけでよく、乾燥させねばならな い結合剤溶液が比較的少量であるから設備の加工速度を高め、稼動時間を長くす ることができ、マスターリールは白色素材だけで構成されるから貯蔵が簡単であ り、ムダの総量も少ないという幾つもの利点が達成される。ステップ2でも、カ ラー選択が自由であり。添加物塗布が容易であり、エンボスパターンを採用すれ ばバリエーションが一段と豊富になり、要求される個々の品質ごとに稼動時間を 短く設定することで経済性が高まるという利点が得られる。ステップ2に使用さ れる設備は必ずしも高生産性製紙設備と直結させて設ける必要はなく、近接の工 場または外部の加工業者の工場に設置すればよい。換言すれば、ステップ2及び 場合によってはそれ以後のステップはステップ1よりも簡単安価な設備で行うこ とができ、これによって高価な高生産性製紙設備の利用度を高めることができる 。The present invention is characterized by dividing the manufacturing process into at least two steps separated from each other. To solve the above problems economically and rationally. In step 1, handling in agglomerated state Materials free of colorants and chemical additives other than the standard ingredients necessary to obtain a smooth web. form material. The next step, step 2, is to process this material to the desired finish. Process to grade. In this way, maximum flexibility and reduced production costs are achieved. is achieved. In step 1, you only need to work with the white material, which must be dried. The relatively small amount of binder solution increases equipment processing speeds and increases uptime. The master reel is made of only white material, making it easy to store. A number of advantages are achieved, including less total waste. In step 2, You are free to choose. Additives can be easily applied and an embossed pattern is used. This means that there will be a wider variety of variations, and the operating time can be adjusted to suit each quality required. Setting it short has the advantage of increasing economic efficiency. used for step 2 It is not necessary to install the equipment directly connected to the high-productivity paper manufacturing equipment; It can be installed at the factory or at the factory of an outside processor. In other words, step 2 and In some cases, subsequent steps can be performed with simpler and cheaper equipment than step 1. This increases the utilization of expensive, high-productivity papermaking equipment. .
好ましい実施例に従って本発明をさらに詳細に説明する。The present invention will be explained in more detail according to preferred embodiments.
ステップ1において、繊維をウェブに成形し、これを圧縮し、結合剤を塗布し、 仕上がりグレードの20〜90%、好ましくは60〜80%に相当する加工度ま で乾燥させ、いわゆるマスターリールに巻取る。半加工素材を巻取ったこのマス ターリールは高い設備利用度で形成することができる。なぜなら、ウェブごとの 材料組成及び処理の基本的な種類が少なく、均一な性質及び高い品質を与えるこ とができるからである。マスターリールは以後のステップにおける処理に備えて 緩衝在庫を計ることができる。In step 1, the fibers are formed into a web, which is compressed and a binder is applied; A degree of processing equivalent to 20 to 90%, preferably 60 to 80% of the finished grade. It is then dried on a so-called master reel. This mass is rolled up from semi-processed material. Tarir can be formed with high capacity utilization. Because each web The basic variety of material composition and processing is small, giving uniform properties and high quality. This is because it can be done. The master reel is prepared for processing in subsequent steps. Buffer stock can be measured.
結合剤の種類及び品質はステップ2においてウェブの両面にそれぞれ特殊な性質 を持たせることができるようにステップ1においてウェブの面ごとに別々に選択 すればよい。The type and quality of the binder is determined in step 2 by determining the special properties of each side of the web. In step 1, select each side of the web separately so that do it.
ステップ2において、カラー、吸収性、耐炎性、エンボシングなど、(湿潤強さ 、無毛羽性などのような)基本的“強さ特性”を除く規定の性質を含む最終引渡 しグレードまでウェブを加工する。In step 2, color, absorbency, flame resistance, embossing, etc. (wet strength) final delivery, including specified properties other than basic “strength characteristics” (such as hair-free properties, etc.) The web is processed to a fine grade.
ステップ2においてさらに結合剤が追加塗布され、この結合剤には、所要の性質 を与えるためのその他の成分が混入される。特に着色については、本発明のツー ステップ製法は従来の製法では達成が困難であった成果を可能にする。使用され る結合剤中の色素が全面に均等に配分され、繊維を充分な深さまでカバーするか ら、満足な色感が得られ、しかも、必要なら両面において同様の効果を得ること ができる。ステップ2における結合剤は例えば液体(溶液、分散系、懸濁液)、 ペース、泡状物など種々の形で塗布することができ、塗布方法としては、グラビ ア印刷、フレキソ印刷、スクリーン印刷、ローラ−塗布またはスプレィなど種々 の方法を利用することができる。In step 2, additional binder is applied, which has the desired properties. Other ingredients are mixed in to give the In particular, regarding coloring, the tool of the present invention Step manufacturing enables results that are difficult to achieve with traditional manufacturing methods. used Is the pigment in the binder distributed evenly over the entire surface and covers the fibers to a sufficient depth? A satisfactory color impression can be obtained, and if necessary, the same effect can be obtained on both sides. Can be done. The binder in step 2 is, for example, a liquid (solution, dispersion, suspension), It can be applied in various forms such as paste or foam. Various printing methods such as flexo printing, screen printing, roller coating or spray printing, etc. method can be used.
国際調査報告international search report
Claims (1)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE8802010-2 | 1988-05-30 | ||
SE8802010A SE461228B (en) | 1988-05-30 | 1988-05-30 | PROCEDURES FOR THE PREPARATION OF DRY FORMATED FIBER MATERIAL |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03504621A true JPH03504621A (en) | 1991-10-09 |
Family
ID=20372462
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP50620889A Pending JPH03504621A (en) | 1988-05-30 | 1989-05-25 | Manufacturing method of dry molded fibrous material |
Country Status (9)
Country | Link |
---|---|
EP (1) | EP0427734A1 (en) |
JP (1) | JPH03504621A (en) |
AU (1) | AU3763089A (en) |
DK (1) | DK281290D0 (en) |
ES (1) | ES2015681A6 (en) |
FI (1) | FI905897A0 (en) |
NO (1) | NO905123D0 (en) |
SE (1) | SE461228B (en) |
WO (1) | WO1989012139A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6136422A (en) | 1996-04-05 | 2000-10-24 | Eatern Pulp & Paper Corporation | Spray bonded multi-ply tissue |
-
1988
- 1988-05-30 SE SE8802010A patent/SE461228B/en not_active IP Right Cessation
-
1989
- 1989-05-25 JP JP50620889A patent/JPH03504621A/en active Pending
- 1989-05-25 WO PCT/SE1989/000295 patent/WO1989012139A1/en not_active Application Discontinuation
- 1989-05-25 AU AU37630/89A patent/AU3763089A/en not_active Abandoned
- 1989-05-25 EP EP19890906849 patent/EP0427734A1/en not_active Withdrawn
- 1989-05-30 ES ES8901844A patent/ES2015681A6/en not_active Expired - Fee Related
-
1990
- 1990-11-27 NO NO1990905123A patent/NO905123D0/en unknown
- 1990-11-27 DK DK281290A patent/DK281290D0/en not_active Application Discontinuation
- 1990-11-29 FI FI905897A patent/FI905897A0/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
AU3763089A (en) | 1990-01-05 |
ES2015681A6 (en) | 1990-09-01 |
DK281290A (en) | 1990-11-27 |
FI905897A0 (en) | 1990-11-29 |
WO1989012139A1 (en) | 1989-12-14 |
DK281290D0 (en) | 1990-11-27 |
NO905123L (en) | 1990-11-27 |
NO905123D0 (en) | 1990-11-27 |
SE8802010L (en) | 1989-12-01 |
SE461228B (en) | 1990-01-22 |
SE8802010D0 (en) | 1988-05-30 |
EP0427734A1 (en) | 1991-05-22 |
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