Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0711113B2 - Recycled paper manufacturing method - Google Patents
[go: Go Back, main page]

JPH0711113B2 - Recycled paper manufacturing method - Google Patents

Recycled paper manufacturing method

Info

Publication number
JPH0711113B2
JPH0711113B2 JP13216886A JP13216886A JPH0711113B2 JP H0711113 B2 JPH0711113 B2 JP H0711113B2 JP 13216886 A JP13216886 A JP 13216886A JP 13216886 A JP13216886 A JP 13216886A JP H0711113 B2 JPH0711113 B2 JP H0711113B2
Authority
JP
Japan
Prior art keywords
paper
waste paper
oil
recycled paper
waste
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 - Lifetime
Application number
JP13216886A
Other languages
Japanese (ja)
Other versions
JPS62289689A (en
Inventor
一生 桜井
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.)
Nippon Steel Nisshin Co Ltd
Original Assignee
Nisshin Steel 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 Nisshin Steel Co Ltd filed Critical Nisshin Steel Co Ltd
Priority to JP13216886A priority Critical patent/JPH0711113B2/en
Publication of JPS62289689A publication Critical patent/JPS62289689A/en
Publication of JPH0711113B2 publication Critical patent/JPH0711113B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/64Paper recycling

Landscapes

  • Paper (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は主として鉱物油からなる圧延油の付着および含
有したステンレス鋼帯合紙の故紙を原材料にして、油分
の少ない再生紙を製造する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention is a method for producing recycled paper with low oil content by using a waste paper of stainless steel strip interleaving paper containing and adhering a rolling oil mainly composed of mineral oil as a raw material. Regarding

(従来技術) 金属帯を冷間圧延やスキンパスする際鉱物油を主成分と
する圧延油を使用して行うが、ステンレス鋼の冷延鋼帯
のごとく、表面疵が目立ち易いものの場合、コイルに巻
取るとき合紙を挿入して疵の発生を防止する。このため
コイルを巻戻して加工する場合、圧延油の付着および含
有した故紙が多量に発生する。しかし合紙は材質の良好
なものであるので、故紙になっても捨てず、従来より再
生紙製造の原材料に利用している。
(Prior Art) When cold-rolling or skin-passing a metal strip, a rolling oil containing mineral oil as a main component is used. However, when a surface flaw is easily noticeable, such as a cold-rolled steel strip of stainless steel, a coil is used. Insert interleaving paper when winding to prevent scratches. For this reason, when the coil is rewound and processed, a large amount of waste paper containing rolling oil and contained waste paper is generated. However, since the interleaving paper is a good material, even if it becomes a waste paper, it is not thrown away and has been used as a raw material for manufacturing recycled paper.

この故紙を原材料とする再生紙の製造方法の従来の一般
的な方法は故紙を巻物状もしくは圧縮塊状にして、底部
に剪断刃物を有する離解機に投入した後、工水もしくは
白水を故紙濃度が約5.5wt%になるように注入し、しか
る後に蒸気の直接吹き込み、剪断刃物の回転およびアル
カリ(例えばカセイソーダ)の添加を行って温度約60℃
で約90分攪拌することにより故紙を繊維状に離解させ、
故紙がかゆ状に離解したら脱水、水洗を繰返してアルカ
リ、圧延油を除去して抄紙する方法である。この方法で
故紙離解の際アルカリを添加するのは、故紙に付着した
鉱物油や植物油あるいは一般的な汚れなどの除去を促進
するためで、通常カセイソーダを故紙の約1wt%相当添
加している。
A conventional general method for producing recycled paper using this waste paper as a raw material is to make the waste paper into a roll or a compressed block, and put it in a disintegrator having a shearing blade at the bottom, and then add industrial water or white water to the waste paper concentration Inject it to about 5.5 wt%, then blow steam directly, rotate the shear blade and add alkali (for example, caustic soda) to obtain a temperature of about 60 ° C.
The waste paper is disintegrated into fibers by stirring for about 90 minutes.
When the waste paper is disintegrated into a porridge, dehydration and water washing are repeated to remove alkali and rolling oil, and papermaking is performed. The reason for adding an alkali during the disintegration of waste paper by this method is to accelerate the removal of mineral oil, vegetable oil or general dirt adhering to the waste paper, and caustic soda is usually added in an amount of about 1 wt% of the waste paper.

(発明が解決しようとする問題点) しかしながらこのような製造方法で鉱物油の付着量およ
び含有量が10wt%以上の故紙だけを原材料に用いて再生
紙を製造すると、再生紙には鉱物油が2〜3wt%残存し
てしまうものであった。このため抄紙の際や再生紙を使
用の際、次のような種々の問題があった。
(Problems to be Solved by the Invention) However, when recycled paper is manufactured by using only waste paper having a deposit and content of mineral oil of 10 wt% or more as a raw material by such a manufacturing method, the recycled paper will not contain mineral oil. 2 to 3 wt% remains. Therefore, there have been various problems as described below when making paper or using recycled paper.

1.抄紙上の問題 (1) 抄紙を継続していくと、抄紙機の網ロール部に
油分が濃縮蓄積されて、それが時折製品中に混入し、
「浮き種」と称する品質欠陥になる。
1. Problems in papermaking (1) When papermaking is continued, oil content is concentrated and accumulated on the net roll of the papermaking machine, and sometimes it is mixed in the product,
It becomes a quality defect called "floating seed".

(2) 抄紙後の乾燥工程で油分が蒸発し、空気中に油
粒子が放散浮遊するようになるため、作業者に不快感を
与えると同時に、周辺機器を汚染する。またこの乾燥工
程では油分の含有油やそれに起因する含水率の不均一性
により乾燥斑が生じ易くなり、製品も形状が損なわれた
り、シワが多くなり易い。この形状不良やシワの発生を
防止するには乾燥を過度にすればよいのであるが、乾燥
が過度になると乾燥海苔のごとく硬直化したものにな
り、湿度の高い時期に使用すると急激に水分を吸収して
シワが生じ、また急激に体積が変化して、含有不純物を
吐出する。さらに乾燥を過度に行うには多量の熱を必要
とするため、乾燥費が高くなり、好ましくない。
(2) In the drying step after paper making, the oil content evaporates, and the oil particles are dispersed and suspended in the air, which causes discomfort to the worker and contaminates peripheral equipment. Further, in this drying process, unevenness in the oil content and the resulting non-uniformity of the water content tend to cause dry spots, and the product is liable to lose its shape and wrinkles easily. To prevent this shape defect and the occurrence of wrinkles, it is sufficient to dry it excessively, but when it is excessively dried, it becomes stiff like dried seaweed, and when it is used in a high humidity period, it will drastically remove water. Wrinkles are generated by absorption, and the volume changes abruptly to discharge the contained impurities. Furthermore, since excessive drying requires a large amount of heat, the drying cost becomes high, which is not preferable.

2.再生紙の問題 (1) 板状の金属、ガラス、プラスチックなど直接重
ねて置くと表面にスリ疵、押疵、割れなどが発生しやす
い材質のものの場合、重ね合せの際合紙を挿入するが、
再生紙を合紙に使用すると、油分が材料の表面に転写し
てくもり、材料の商品価値を著しく低下させる。
2.Problems with recycled paper (1) Inserting interleaving paper at the time of stacking in the case of materials such as scratches, blemishes, and cracks that tend to occur on the surface when placed directly on top of each other, such as plate-shaped metal, glass, and plastic But
When recycled paper is used as an interleaving paper, oil is transferred to the surface of the material and becomes cloudy, which significantly reduces the commercial value of the material.

(2) 紙を構成する紙繊維同志が油分により滑りやす
くなり、紙力が低下する。このため例えば印刷用紙に使
用すると、印刷機のガイドロールにひっかかり作業性が
低下する。
(2) The paper fibers composing the paper become slippery due to the oil, and the paper strength is reduced. For this reason, when it is used for printing paper, for example, it is caught by the guide roll of the printing machine and the workability is reduced.

(3) サイズ剤との反応が不均一になり易いため、印
刷インキの乗りが悪く、印刷不良が生じる。
(3) Since the reaction with the sizing agent is likely to be non-uniform, the printing ink does not ride well and printing defects occur.

(4) 鉱物油は一般に電気絶縁性が高いため、鉱物油
を含有する紙は帯電しやすく、例えば金属板の合紙に使
用した場合金属板と合紙が離れ難くなり、また金属帯を
コイル状に巻取る際に合紙を挿入したり、合紙をコイル
状に巻取ったりする場合に放電して、作業者に不快感を
与え、また設備の電気機器に障害を与えたりする。
(4) Since mineral oil generally has high electric insulation, paper containing mineral oil is easily charged with electricity. For example, when used as interleaving paper for metal plates, the metal plate and interleaving paper are difficult to separate, and the metal strip is coiled. When inserting the interleaving paper when winding the interleaving paper in the shape of a coil, or when winding the interleaving paper in the form of a coil, the electric discharge causes electric discomfort to the operator and also damages electric equipment of the facility.

以上のように従来の主として鉱物油の付着および含有の
故紙を原材料とする再生紙の製造方法には種々の問題が
あったので、本発明は上記問題を解決した再生紙の製造
方法を提供するものである。
As described above, since there are various problems in the conventional method for producing recycled paper mainly made from waste paper having mineral oil adhered and contained, the present invention provides a method for producing recycled paper that solves the above problems. It is a thing.

(問題点を解決するための手段) 本発明は離解機で故紙をアルカリ性水溶液で繊維状に離
解させる際鉱物油に対する脱油剤を添加して鉱物油を乳
化分散させて、鉱物油を繊維より分離し、これにより抄
紙上の問題を解決するとともに、油含有量の少ない再生
紙を製造できるようにしたものである。
(Means for Solving Problems) In the present invention, when the waste paper is disintegrated into fibers by an disintegrator with an alkaline aqueous solution, a deoiling agent for mineral oil is added to emulsify and disperse the mineral oil to separate the mineral oil from the fibers. In this way, it is possible to solve the papermaking problem and to manufacture recycled paper having a low oil content.

すなわち本発明は主として鉱物油からなる圧延油の付着
および含有したステンレス鋼帯合紙の故紙を脱油剤を添
加しアルカリ性水溶液で繊維状に離解させて脱油した
後、アルカリと脱油剤を除去して抄紙することを特徴と
する再生紙の製造方法を提供するものである。
That is, the present invention is mainly applied with a rolling oil consisting of mineral oil, and the waste paper of the stainless steel strip interleaving paper containing the oil is added with a deoiling agent to be disintegrated into fibers with an alkaline aqueous solution to deoil, and then the alkali and deoiling agent are removed. The present invention provides a method for producing recycled paper, which is characterized in that

本発明において、アルカリ性水溶液のアルカリ濃度は従
来法のように故紙に対して通常1wt%にするが、0.5〜2.
0wt%の範囲ならばよい。また脱油剤の種類はとくに限
定はなく、市販品でよいが、離解の際のアルカリ水溶液
を60〜90℃に、脱油剤と故紙との接触を10分以上にする
のが好ましい。さらに故紙の油含有率が高い場合には油
の付着および含有しない故紙やパルプを配合することも
可能である。
In the present invention, the alkali concentration of the alkaline aqueous solution is usually 1 wt% with respect to the waste paper as in the conventional method, but 0.5 to 2.
It should be in the range of 0 wt%. The type of the deoiling agent is not particularly limited and may be a commercially available product, but it is preferable that the alkaline aqueous solution at the time of disaggregation is kept at 60 to 90 ° C. and the contact between the deoiling agent and the waste paper is 10 minutes or more. Further, when the waste paper has a high oil content, it is possible to blend waste paper or pulp that does not contain oil and does not contain oil.

次に実施例により本発明を説明する。Next, the present invention will be described with reference to examples.

(実施例) 第1図は本発明の製造工程を示すもので、離解機1は鉄
製の有底円筒状のもので、上部に開口部2を、また内部
側面に邪魔板3を、さらに底部に水平回転する剪断刃物
4と蒸気吹込み口5を有している。この離解機1にまず
コンベア6で油の付着した故紙7を投入し、次に白水
(工水)を投入して、故紙7の濃度が約5.5wt%になる
ようにした。この状態で剪断刃物4を回転させて、故紙
7を離解させながら、カセイソーダを故紙7に対して1w
t%、また脱油剤を油の付着しない故紙換算で表1のよ
うに投入した後、温度80℃で40分間剪断刃物4を回転し
て離解、脱油し、故紙をかゆ状にした。その後剪断刃物
4を停止させて、かゆ状物をポンプ8で抄紙用原料貯槽
9に送り、そこに一旦貯蔵した後、ポンプ10で分粒機11
に送って濾過し、完全に離解したもののみを1対の網状
ロールの第1圧縮濾過洗浄機12に送った。ここで圧縮し
て一部脱水することにより脱アルカリ、脱油して含水率
約75wt%にした後、白水(工水)をかけながら原料希釈
装置13に送り、白水(工水)を加えて再びかゆ状にし
た。その後このかゆ状物を前記第1圧縮濾過洗浄機12と
同構造の第2圧縮濾過洗浄機14にポンプ15で送り、再び
脱水して、含水率約75wt%にした後、白水(工水)をか
けながら濾過洗浄機16に送り、最終洗浄と濾過を行い、
以後常法に従って抄紙し、再生紙を製造した。
(Embodiment) FIG. 1 shows a manufacturing process of the present invention. The disintegrator 1 is an iron bottomed cylinder, and has an opening 2 at the top, a baffle plate 3 at the inner side surface, and a bottom. It has a shearing blade 4 that horizontally rotates and a steam inlet 5. To the disintegrator 1, the waste paper 7 with oil attached thereto was first charged by the conveyor 6, and then white water (engineering water) was added so that the concentration of the waste paper 7 became about 5.5 wt%. In this state, rotate the shearing blade 4 to disintegrate the waste paper 7 and remove the caustic soda from the waste paper 1 w
After adding t% and a degreasing agent as shown in Table 1 in terms of waste paper without oil adhesion, the shear blade 4 was rotated at a temperature of 80 ° C. for 40 minutes for disaggregation and deoiling to make the waste paper a porridge. After that, the shearing blade 4 is stopped, and the porridge-like material is sent by the pump 8 to the raw material storage tank 9 for papermaking, where it is once stored, and then the pump 10 is used for the sizing machine 11.
To the first compression filter washer 12 having a pair of mesh rolls. Here, after compressing and partially dehydrating, it is dealkalized and deoiled to a water content of about 75 wt%, then sent to the raw material diluting device 13 while sprinkling white water (working water), and adding white water (working water). I made itchy again. After that, the porridge was sent to the second compression filtration washing machine 14 having the same structure as the first compression filtration washing machine 12 by the pump 15 and was dehydrated again to have a water content of about 75 wt%, and then white water (engineering water). While sending it to the filter washing machine 16, performs the final washing and filtration,
After that, paper was made according to a conventional method to produce recycled paper.

表1に原材料(故紙)中の油含有率、使用した脱油剤の
種類および再生紙の油含有率の関係を示す。
Table 1 shows the relationship between the oil content in the raw material (waste paper), the type of the deoiling agent used, and the oil content in the recycled paper.

表1より脱油剤の種類を選択して脱油すれば再生紙の油
含有率を従来よりかなり低くすることができる。
By selecting the type of deoiling agent from Table 1 and deoiling, the oil content of recycled paper can be made considerably lower than before.

また第2図は故紙7を離解させる際脱油剤として表1の
脱油剤Cを使用した場合の故紙7と脱油剤との接触時間
を示すものであるが、再生紙の油含有率を従来の2%以
下にするには接触時間を10分間以上にする必要がある。
FIG. 2 shows the contact time between the waste paper 7 and the degreasing agent when the deoiling agent C shown in Table 1 was used as the degreasing agent when the waste paper 7 was disintegrated. In order to reduce it to 2% or less, the contact time must be 10 minutes or more.

さらに第3図は上記離解の際の温度と脱油剤Cの添加量
との関係を示したものであるが、再生紙の油含有率を従
来の2%以下にするには温度を60〜90℃にする必要があ
る。
Further, FIG. 3 shows the relationship between the temperature at the time of disaggregation and the addition amount of the deoiling agent C. In order to reduce the oil content of recycled paper to 2% or less of the conventional temperature, the temperature should be 60 to 90%. Must be ℃.

(効果) 以上のごとく本発明の製造方法によれば、再生紙の油含
有率を従来より低くすることができるので、従来問題に
なっていた抄紙上の問題や再生紙の問題はなくなる。
(Effects) According to the production method of the present invention as described above, the oil content of recycled paper can be made lower than before, so that the problems of papermaking and recycled paper, which have hitherto been problems, are eliminated.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明による製造工程であり、第2図は故紙を
離解させる際実施例において使用した脱油剤Cと故紙と
の接触時間を示すグラフであり、第3図は脱油剤Cの添
加量と離解の際の温度との関係を示すグラフである。 1……離解機、2……開口部、3……邪魔板、4……剪
断刃物、5……蒸気吹込み口、6……コンベア、7……
故紙、8……ポンプ、9……抄紙用原料貯槽、10……ポ
ンプ、11……分粒機、12……第1圧縮濾過洗浄機、13…
…原料希釈装置、14……第2圧縮濾過洗浄機、15……ポ
ンプ、16……濾過洗浄機、
FIG. 1 is a manufacturing process according to the present invention, FIG. 2 is a graph showing the contact time between the deoiling agent C used in the examples and the waste paper when disintegrating the waste paper, and FIG. 3 is the addition of the deoiling agent C. It is a graph which shows the relationship between the amount and the temperature at the time of disaggregation. 1 ... disintegrator, 2 ... opening, 3 ... baffle plate, 4 ... shear blade, 5 ... steam inlet, 6 ... conveyor, 7 ...
Waste paper, 8 ... Pump, 9 ... Paper making material storage tank, 10 ... Pump, 11 ... Granulator, 12 ... First compression filtration washing machine, 13 ...
… Raw material diluter, 14 …… 2nd compression filtration washing machine, 15 …… Pump, 16 …… Filtration washing machine,

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】主として鉱物油からなる圧延油の付着およ
び含有したステンレス鋼帯合紙の故紙を脱油剤を添加し
アルカリ性水溶液で繊維状に離解させて脱油した後、ア
ルカリと脱油剤を除去して抄紙することを特徴とする再
生紙の製造方法。
Claims: 1. A rolling oil consisting mainly of mineral oil and a waste paper of stainless steel strip interleaving paper containing the oil are added with a deoiling agent and disintegrated into fibrous form with an alkaline aqueous solution for deoiling, and then the alkali and the deoiling agent are removed. A method for producing recycled paper, which comprises:
【請求項2】アルカリ水溶液のアルカリ濃度を故紙に対
してカセイソーダを0.5〜2.0wt%添加したものにするこ
とを特徴とする特許請求の範囲第1項に記載の再生紙の
製造方法。
2. The method for producing recycled paper according to claim 1, wherein the alkaline concentration of the alkaline aqueous solution is 0.5 to 2.0 wt% of caustic soda added to the waste paper.
【請求項3】離解機に故紙を入れた後アルカリ水溶液と
脱油剤とを投入して故紙を離解および脱油することを特
徴とする特許請求の範囲第1項に記載の再生紙の製造方
法。
3. The method for producing recycled paper according to claim 1, wherein the waste paper is disintegrated and deoiled by introducing an alkaline aqueous solution and a deoiling agent after putting the waste paper in the disintegrator. .
【請求項4】故紙に鉱物油の付着および含有しない故紙
もしくはパルプを配合することを特徴とする特許請求の
範囲第1項に記載の再生紙の製造方法。
4. The method for producing recycled paper according to claim 1, wherein the waste paper is mixed with a waste paper or pulp that does not contain or contain mineral oil.
【請求項5】脱油処理した再生紙の含油分を2%以下に
することを特徴とする特許請求の範囲第1〜4項のいず
れかに記載の再生紙の製造方法。
5. The method for producing recycled paper according to any one of claims 1 to 4, wherein the oil content of the deoiled recycled paper is 2% or less.
JP13216886A 1986-06-07 1986-06-07 Recycled paper manufacturing method Expired - Lifetime JPH0711113B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13216886A JPH0711113B2 (en) 1986-06-07 1986-06-07 Recycled paper manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13216886A JPH0711113B2 (en) 1986-06-07 1986-06-07 Recycled paper manufacturing method

Publications (2)

Publication Number Publication Date
JPS62289689A JPS62289689A (en) 1987-12-16
JPH0711113B2 true JPH0711113B2 (en) 1995-02-08

Family

ID=15074954

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13216886A Expired - Lifetime JPH0711113B2 (en) 1986-06-07 1986-06-07 Recycled paper manufacturing method

Country Status (1)

Country Link
JP (1) JPH0711113B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117966514B (en) * 2024-02-22 2025-09-19 宁波思特雷斯金属防护材料有限公司 Backing paper and preparation method and application thereof

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4929881A (en) * 1972-07-13 1974-03-16
JPS4937721A (en) * 1972-08-15 1974-04-08
JPS5932231B2 (en) * 1976-08-30 1984-08-07 日立金属株式会社 Ingot extraction device
JPS59262A (en) * 1982-06-02 1984-01-05 Fujitsu Ltd Controlling system in case of abnormal congestion of time division switchboard

Also Published As

Publication number Publication date
JPS62289689A (en) 1987-12-16

Similar Documents

Publication Publication Date Title
US6051108A (en) Method of removing and preventing the buildup of contaminants in papermaking processes
US3822178A (en) Process for repulping waxed paper using a water soluble nonionic emulsifier
CA2815457C (en) Method for making fire retardant materials and related products
US6364999B1 (en) Process for producing a wood pulp having reduced pitch content and process and reduced VOC-emissions
JPH026681A (en) How to make paper or cardboard from recycled fibers
JP2022515368A (en) Fiber separation
CN106256952A (en) Utilize the method that corrugating medium's paper mill sludge and slurry produce environmental friendly regenerated bobbin body paper
US2054301A (en) Production of pulverulent cellulose
US2360779A (en) Method of screening and washing paper pulp
EP0666369A2 (en) Felt conditioner
JPH0711113B2 (en) Recycled paper manufacturing method
JPH0351389A (en) Pitch controlling agent and method for controlling pitch
JPH0457795B2 (en)
RU2768635C1 (en) Method for obtaining flaxseed pulp
US1933227A (en) Recovery of pulp from waste paper
US1991823A (en) Reclaiming pulp from waste paper
EP3751052A1 (en) Method for manufacturing paper and/or cardboard from nutshell flour
US2675745A (en) Protection of dispersed asbestos
CN1985048A (en) Process for sheeting raw cotton linters
CN110714349A (en) Production process of high-strength corrugated base paper
US2041294A (en) Method of making paper
CN112593453A (en) Method for manufacturing liquid crystal substrate protection paper
US20090032206A1 (en) Processes used in the manufacture of paper products
US975387A (en) Method of treating bagasse.
DE602890C (en) Process for the production of particularly absorbent, paper-like material from cellulose