JP2002363880A - HIGH QUALITY PAPER WITH 100% NON-WOOD PULP (BAGASSE PAPER-a) AND METHOD FOR PRODUCING THE SAME - Google Patents
HIGH QUALITY PAPER WITH 100% NON-WOOD PULP (BAGASSE PAPER-a) AND METHOD FOR PRODUCING THE SAMEInfo
- Publication number
- JP2002363880A JP2002363880A JP2001170575A JP2001170575A JP2002363880A JP 2002363880 A JP2002363880 A JP 2002363880A JP 2001170575 A JP2001170575 A JP 2001170575A JP 2001170575 A JP2001170575 A JP 2001170575A JP 2002363880 A JP2002363880 A JP 2002363880A
- Authority
- JP
- Japan
- Prior art keywords
- pulp
- paper
- bagasse
- producing
- wood
- 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
- 241000609240 Ambelania acida Species 0.000 title claims abstract description 37
- 239000010905 bagasse Substances 0.000 title claims abstract description 37
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 19
- 229920001131 Pulp (paper) Polymers 0.000 title claims abstract description 17
- 238000000034 method Methods 0.000 claims abstract description 34
- 240000000491 Corchorus aestuans Species 0.000 claims abstract description 17
- 235000011777 Corchorus aestuans Nutrition 0.000 claims abstract description 17
- 235000010862 Corchorus capsularis Nutrition 0.000 claims abstract description 17
- 239000010902 straw Substances 0.000 claims abstract description 13
- 229920000742 Cotton Polymers 0.000 claims abstract description 12
- 239000002994 raw material Substances 0.000 claims abstract description 9
- 239000002699 waste material Substances 0.000 claims abstract description 9
- 239000000945 filler Substances 0.000 claims abstract description 8
- 238000004513 sizing Methods 0.000 claims description 7
- 239000003795 chemical substances by application Substances 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 238000010009 beating Methods 0.000 abstract description 10
- 238000002156 mixing Methods 0.000 abstract description 10
- 239000000835 fiber Substances 0.000 abstract description 9
- 230000007423 decrease Effects 0.000 abstract description 7
- 239000002023 wood Substances 0.000 abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 3
- 239000000123 paper Substances 0.000 description 47
- 238000010411 cooking Methods 0.000 description 15
- 238000004537 pulping Methods 0.000 description 11
- 244000025254 Cannabis sativa Species 0.000 description 10
- 235000012766 Cannabis sativa ssp. sativa var. sativa Nutrition 0.000 description 10
- 235000012765 Cannabis sativa ssp. sativa var. spontanea Nutrition 0.000 description 10
- 235000009120 camo Nutrition 0.000 description 10
- 235000005607 chanvre indien Nutrition 0.000 description 10
- 239000011487 hemp Substances 0.000 description 10
- 238000004061 bleaching Methods 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 5
- 239000000428 dust Substances 0.000 description 5
- 239000003513 alkali Substances 0.000 description 4
- 238000007796 conventional method Methods 0.000 description 4
- 230000007935 neutral effect Effects 0.000 description 4
- -1 alkyl ketene dimer Chemical compound 0.000 description 3
- 230000006378 damage Effects 0.000 description 3
- 239000011122 softwood Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 238000013329 compounding Methods 0.000 description 2
- OSVXSBDYLRYLIG-UHFFFAOYSA-N dioxidochlorine(.) Chemical compound O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 description 2
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 235000010215 titanium dioxide Nutrition 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 239000004155 Chlorine dioxide Substances 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 244000068988 Glycine max Species 0.000 description 1
- 235000010469 Glycine max Nutrition 0.000 description 1
- 229920002488 Hemicellulose Polymers 0.000 description 1
- 240000000797 Hibiscus cannabinus Species 0.000 description 1
- 240000004153 Hibiscus sabdariffa Species 0.000 description 1
- 235000001018 Hibiscus sabdariffa Nutrition 0.000 description 1
- 240000006240 Linum usitatissimum Species 0.000 description 1
- 235000004431 Linum usitatissimum Nutrition 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 244000062793 Sorghum vulgare Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 244000098338 Triticum aestivum Species 0.000 description 1
- 240000001417 Vigna umbellata Species 0.000 description 1
- 235000011453 Vigna umbellata Nutrition 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- PYKYMHQGRFAEBM-UHFFFAOYSA-N anthraquinone Natural products CCC(=O)c1c(O)c2C(=O)C3C(C=CC=C3O)C(=O)c2cc1CC(=O)OC PYKYMHQGRFAEBM-UHFFFAOYSA-N 0.000 description 1
- 150000004056 anthraquinones Chemical class 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000000740 bleeding effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 239000002738 chelating agent Substances 0.000 description 1
- 235000019398 chlorine dioxide Nutrition 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 238000009499 grossing Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000002655 kraft paper Substances 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 150000002681 magnesium compounds Chemical class 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 239000000347 magnesium hydroxide Substances 0.000 description 1
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 1
- 235000019713 millet Nutrition 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000011087 paperboard Substances 0.000 description 1
- 239000003495 polar organic solvent Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052979 sodium sulfide Inorganic materials 0.000 description 1
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Landscapes
- Paper (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は非木材パルプのみの
配合になる上質紙とその製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to high quality paper containing only non-wood pulp and a method for producing the same.
【0002】[0002]
【従来の技術】自然環境問題の解決の一つの手段とし
て、これまで大量に使われてきた紙が木材のパルプで作
られて来たのを反省し、非木材のパルプで紙を製造して
使っていこうと言う動きが高まってきた。そして、原料
として容易にかつ大量に集められるバガス(砂糖キビの
搾り粕)をパルプ化し、木材パルプの中に少量混抄し、
非木材紙として市場に売り出すことが大勢となってい
る。しかし、最近では非木材パルプ100%の上質紙が
供給されるなら、それをを使って見たいと言う人々も出
てきた。しかし、これまでバガスパルプ100%紙は弱
すぎて一般の用には向かないとされてきた。バガスは木
材に比べてリグニン含有量が小さく、セルロ−スとヘミ
セルロ−スの含有量が多いため、パルプ化も容易で、品
質の良いパルプが高収率で得られそうであるが、収率は
低く、諸強度は劣り、特に引き裂き強度が劣るなどの欠
点が指摘されてきた。そのため、通常は大量のバガスパ
ルプに強度に優れ繊維長の大きい針葉樹のKP(クラフ
トパルプ)をつなぎのパルプとして少量配合し、上質紙
等を抄造してきた もし、非木材100%の紙を生産す
るなら、少なくともバガスパルプの強度を思い切って向
上させる方法か、つなぎパルプも非木材パルプにし、そ
の大量供給を可能にする方法しか、選択できる方法はな
い。バガスパルプが、その原料の組成に比くらべて強度
が低いのは、バガス製糖の際に繊維が強い機械的破壊を
受けているうえに繊維が短く、蒸解時に薬液による高温
下での化学的損傷を受けているものと考えられる。特に
AP蒸解薬液(水酸化ナトリウム単独の水溶液)による
損傷は激しく、得られるパルプの強度は優れない。これ
らの欠点は、KP蒸解薬液(水酸化ナトリウムと硫化ナ
トリウムの混合液)やPA蒸解薬液(過酸化水素のアル
カリ溶液に安定剤等の蒸解助剤を添加)で蒸解して得ら
れるパルプが、引き裂き強度以外の諸強度が大きく向上
することでも理解できる。いずれにせよ、バガスパルプ
のみでは強度が足りない。叩解を進めれば裂断長や、比
破裂強度は幾分上がるが、濾水度は下がり、抄紙適性は
落ち、引き裂き強度は更に低下し、得られる紙は密度は
上がりパリパリになり、不透明度は著しく低下してして
針葉樹のKPを10〜20%配合して印用紙のような上
質紙や、板紙のような産業用紙を製造してきた。南では
木材も非木材も一般に繊維長は短く、麻以外に繊維の長
いものは求められないとされてきた。しかし、麻は資源
的に少なく、ロ−プやため極めて貴重で、安価なかも、
麻のような非木材の長繊維パルプを配合して、密度がほ
どほどに高く、強度もあるような紙を得るために叩解を
進めれば繊維が捩れ易く、繊維同志がくっついて、いわ
ゆるダマを作り洋紙の美観を損ね商品価値を著しく低下
させる。また、屑麻には植物の皮などの非繊維質の不純
物や塵が多く、従来の蒸解法ではパルプ化に際しても未
蒸解物の分別除去や除塵が容易でなく、屑麻を原料とし
たパルプを配合しても得られる紙は汚れ、商品価値が非
常に劣るので、このような印刷用紙等の上質紙の商業生
産についての成功例や、新たな企画は報告がなかった。2. Description of the Related Art As a means of solving the problem of the natural environment, we reflect on the fact that paper, which has been used in large quantities, is made of wood pulp, and manufacture paper with non-wood pulp. The movement to use it has been increasing. And bagasse (pulverized sugar millet), which is easily and massively collected as a raw material, is pulped and mixed into wood pulp in a small amount.
There is a great deal of marketing to the market as non-wood paper. However, recently, some people have requested to use 100% non-wood pulp high quality paper if it is supplied. However, up to now, 100% bagasse pulp paper has been considered too weak for general use. Bagasse has a lower lignin content and a higher content of cellulose and hemicellulose than wood, so that pulping is easy and high-quality pulp is likely to be obtained in high yield. However, drawbacks such as low strength, poor strength, and particularly poor tear strength have been pointed out. Therefore, a large amount of bagasse pulp is usually blended with a small amount of softwood KP (kraft pulp), which has high strength and a large fiber length, as a connecting pulp to make a high-quality paper. At least, there is no choice but to increase the strength of bagasse pulp drastically, or to make the connecting pulp non-wood pulp and to supply it in large quantities. Bagasse pulp has a lower strength compared to the composition of its raw materials because the fibers are subjected to strong mechanical destruction during bagasse making and the fibers are short, preventing chemical damage at high temperatures due to chemicals during cooking. It is thought that it has received. Particularly, the damage by the AP cooking chemical (aqueous solution of sodium hydroxide alone) is severe, and the strength of the obtained pulp is not excellent. These drawbacks are that pulp obtained by cooking with KP cooking liquor (a mixture of sodium hydroxide and sodium sulfide) or PA cooking liquor (adding a cooking aid such as a stabilizer to an alkaline solution of hydrogen peroxide) It can also be understood that various strengths other than the tear strength are greatly improved. In any case, bagasse pulp alone is not strong enough. As the beating process proceeds, the breaking length and specific burst strength increase somewhat, but the freeness decreases, the suitability for papermaking decreases, the tear strength further decreases, and the resulting paper increases in density and becomes crisp and opaque. Has significantly decreased, and high-quality paper such as printing paper and industrial paper such as paperboard have been manufactured by blending 10-20% of KP of softwood. In the south, both timber and non-timber have generally been short in fiber length, and it has been said that long fibers other than hemp are not required. However, hemp is scarce in resources, is very valuable because it is a rope,
Non-wood long fiber pulp such as hemp is blended, and if the beating is advanced to obtain paper with a moderately high density and strength, the fibers are easily twisted, and the fibers stick together. This impairs the aesthetics of sashimi paper and significantly lowers its commercial value. In addition, non-fibrous impurities and dust, such as plant skins, are large in waste hemp, and it is not easy to separate and remove undigested matter and dust removal during pulping by conventional cooking methods. However, there is no report on a successful example of commercial production of high-quality paper such as printing paper, or a new plan, since the paper obtained by blending is very dirty and has a very poor commercial value.
【0003】[0003]
【発明が解決しようとする課題】本発明は大量に生産可
能ではあるが、強度が低いバガスパルプを主原料とし、
強度と、風合いのよい100%非木材パルプによる上質
紙紙と、その製法を提供する。The present invention is based on bagasse pulp, which can be produced in large quantities but has low strength,
A high-quality paper made of 100% non-wood pulp with good strength and texture and a method for producing the same are provided.
【0004】[0004]
【課題を解決するための手段】本発明は製糖工場で大量
に副生するバガスを従来法、又は好ましくはPA法で、
皮等の夾雑物や塵が多く、蒸解が困難で、蒸解後も未蒸
解物や塵が多く分離除去困難で、大量に有りながら利用
されていなかったジュ−ト及びジュ−ト類似の麻類の屑
を用い、PA法でパルプ化して精選したものをつなぎパ
ルプとすることにより、非木材のつなぎパルプとしての
質と量の確保を可能とした。即ち、ジュ−ト、ケナフ及
びロ−ゼル麻等は亞麻やラミ−が高価な衣類等に使われ
るのと異なり、米、麦や、大豆、小豆等の雑穀や雑貨等
大量にあって、安価な物資の包装に大量に消費される麻
で、国連統計のみで年間約250万tも生産され消費さ
れている。麻及び麻袋の製造の際に多くの麻屑が発生す
るが、パルプにするには上記のように、従来法では容易
に精選パルプが得られないため、詰め物にされたり、廃
棄、焼却されてきた。しかして、下級紙や産業用紙の原
料パルプの製造に、一部のジュ−ト屑が使われているに
過ぎなかった。 本発明では、麻屑をPA法でパルプ化
して精選したものをつなぎパルプとして比較的大量に用
い、叩解を軽度に行い捩れを抑え、美観を損ねず強度が
ある100%非木材パルプからなる上質紙の製造を可能
とした。さらに、所望によりジュ−トパルプの他にわら
パルプ又は及びコットンパルプを加えて表面平滑性又は
及び風合いの優れた、100%非木材パルプからなる上
質紙とその製造方法を提供する。SUMMARY OF THE INVENTION According to the present invention, bagasse produced in large quantities in a sugar factory is produced by a conventional method or, preferably, a PA method.
Many jute and jute-like hemp which were not used in spite of large amounts of foreign substances such as skins and dust, which were difficult to digest, and which were difficult to separate and remove after cooking. By using the wastes and pulping by the PA method and selecting them carefully to obtain connecting pulp, it was possible to ensure the quality and quantity of non-wood connecting pulp. In other words, jute, kenaf, and roselle are different from flax and lami used for expensive clothing and the like, and are large in quantity, such as rice, wheat, soybeans, red beans, and other cereals and miscellaneous goods. Hemp is consumed in large quantities in the packaging of important materials, and is produced and consumed by the United Nations statistics alone at about 2.5 million tons per year. Many hemp dusts are produced during the production of hemp and hemp bags.However, as described above, pulp cannot be easily selected by the conventional method, so it is either filled or discarded or incinerated. Was. Thus, only a part of jute waste was used in the production of raw pulp for lower grade paper and industrial paper. In the present invention, a high-quality 100% non-wood pulp made of pulverized pulverized by the PA method and carefully selected and used as a connecting pulp is used in a relatively large amount as a connecting pulp. Made paper production possible. Furthermore, if desired, straw pulp or cotton pulp may be added in addition to jute pulp to provide a high-quality paper made of 100% non-wood pulp excellent in surface smoothness or texture and a method for producing the same.
【0005】[0005]
【発明実施の形態】主原料として用いるバガスパルプは
PA法パルプであることが望ましい。AP法、KP法及
びPA法のいずれの方法で得られたパルプでも100%
非木材紙の主原料として使用可能である。しかし、KP
法又はPA法で得られたバガスパルプはAP法で得られ
たものよりも強度が大きいので、つなぎパルプの添加量
は少なくてすむ。 またバガスをKP法でパルプ化する
よりも、PA法でパルプ化することは、未晒パルプがK
P法のパルプの半晒程度の白色度を有すること、漂白に
際し、無塩素化若しくは低塩素化が容易なので、地球環
境問題に取り組むうえで望ましい。DESCRIPTION OF THE PREFERRED EMBODIMENTS Bagasse pulp used as a main raw material is desirably PA pulp. 100% of pulp obtained by any of AP method, KP method and PA method
It can be used as a main raw material for non-wood paper. But KP
Since the bagasse pulp obtained by the method or the PA method has a higher strength than that obtained by the AP method, the amount of tethered pulp added is small. Further, pulping bagasse by the PA method rather than pulping bagasse by the KP method results in unbleached pulp having a K
It is desirable for tackling global environmental issues because it has a whiteness of about bleached pulp of the P method and is easily chlorinated or low chlorinated during bleaching.
【0006】PA法によるバガスのパルプ化は常法によ
って行う。そのパルプ化条件は幅広く取れるが、通常好
ましくは苛性アルカリと炭酸アルカリを、全アルカリと
してNa2 O換算で15〜30%、苛性化度65〜8
5%、過酸化水素をH2 O2として2〜5%、アントラ
キノン0.05〜0.2%、キレ−ト剤としてDTP
A、1−ヒドロキシアルキリデン−1,1−フォスフォ
ン酸等又はそれらの塩を0.2〜0.5%、水と任意に
混ざり合う極性有機溶媒としてNMP(ノルマルメチル
ピロリドン)等を0.05〜0.2%、マグネシウム化
合物として水酸化マグネシウム等をMgOとして0.0
5〜0.2%、を用いて蒸解薬液とする。液相蒸解も気
相蒸解も可能であるが、PA法における気相蒸解は煮え
むら無しに液比を1.5〜2.2L/kgと極めて小さ
く取れ、パルプの蒸解とパルプ廃液の濃縮のエネルギ−
を極端に削減出来るので、二酸化炭素による地球温暖化
防止のうえで好ましい。蒸解は最高温度110〜130
℃、同保持時間は30〜120分である。得られた未晒
パルプはカッパ−価3〜7と極めて低く、ハンタ−白色
度は45〜60%と極めて高く、漂白はPa薬液(アル
カリ性の過酸化水素溶液)又は酸素共存のPa薬液処理
で高い白色度の半晒パルプが得られる。二酸化塩素漂白
で省塩素漂白が、オゾン漂白により無塩素漂白が可能で
ともにハンタ−白色度80〜92%の高白色度の晒パル
プが得られる。The pulping of bagasse by the PA method is carried out by a conventional method. The pulping conditions can be widely varied, but usually, caustic alkali and alkali carbonate are preferably 15 to 30% in terms of Na 2 O as a total alkali, and the degree of causticization is 65 to 8
5%, 2 to 5% of hydrogen peroxide as H 2 O 2 , 0.05 to 0.2% of anthraquinone, DTP as a chelating agent
A, 0.2-0.5% of 1-hydroxyalkylidene-1,1-phosphonic acid or a salt thereof, and 0.05 of NMP (normal methylpyrrolidone) or the like as a polar organic solvent which is arbitrarily mixed with water. 0.20.2%, magnesium hydroxide or the like as a magnesium compound and 0.0 as MgO.
5 to 0.2% is used as the cooking liquid. Both liquid-phase cooking and gas-phase cooking are possible, but the gas-phase cooking in the PA method can obtain a very small liquid ratio of 1.5 to 2.2 L / kg without uneven boiling. Energy
Can be extremely reduced, which is preferable in preventing global warming due to carbon dioxide. Cooking is at a maximum temperature of 110 to 130
° C and the holding time is 30 to 120 minutes. The resulting unbleached pulp has an extremely low kappa value of 3 to 7, a very high Hunter whiteness of 45 to 60%, and bleaching by treatment with a Pa chemical (alkali hydrogen peroxide solution) or a Pa chemical with oxygen. A semi-bleached pulp with high whiteness is obtained. Chlorine dioxide bleaching enables chlorine-saving bleaching, and ozone bleaching enables chlorine-free bleaching. Both bleached pulp with a Hunter brightness of 80 to 92% is obtained.
【0007】ジュ−トは通常の品質以上の物は織物、ロ
−プ等の用途があるので、多用途で使いたくともり、資
源的に大量に集めがたい。また、木材チップに比べれば
遙に高価で、パルプ原料として使うには特殊高級紙の原
料パルプの製造しか考えられなかった。従来、ジュ−ト
屑のパルプは塵が多く上質紙の原料として用いられなか
った。本発明では、ジュ−ト類似の麻類の屑を集め、P
A法でパルプ化することによって皮等の夾雑物まで蒸解
し、分離除去困難な未蒸解物や塵を無くして精選漂白
し、針葉樹の晒KPの代わりに使える強度を持ったパル
プにし、上質紙(バガス紙−a)の製造に使えるつなぎ
パルプを調製する。 そのPA法によるパルプ化の最適
条件は上述のバガスの蒸解温度よりやや高い120〜1
40℃であるが、あとの蒸解条件及び漂白条件は略同等
である。Since a jute having a quality higher than ordinary quality is used for fabrics, ropes and the like, it is desired to use it for many purposes and it is difficult to collect a large amount of resources. In addition, it is much more expensive than wood chips, and the only way to use it as a raw material for pulp was to produce raw pulp for specialty high-grade paper. Conventionally, jute waste pulp has a large amount of dust and has not been used as a raw material for high quality paper. In the present invention, jute-like hemp debris is collected and P
Pulping by method A digests foreign substances such as skins, removes undigested materials and dust that are difficult to separate and remove, and carefully selects and bleaches it to give pulp with strength that can be used in place of bleached KP of softwood. Prepare a tie pulp that can be used for the production of (bagasse paper-a). The optimum conditions for pulping by the PA method are 120 to 1 which are slightly higher than the above-described bagasse cooking temperature.
The temperature is 40 ° C., but the digestion conditions and the bleaching conditions are substantially the same.
【0008】わらパルプとコットンパルプを配合するこ
とにより、100%非木材パルプで印刷適性及び風合い
が更に好ましい良質の印刷用紙とその製造方法を提供し
うるに至った。特にわらパルプの配合は印刷適性の向上
に寄与し、コットンパルプの配合は高級感のある風合を
持った印刷用紙筆記用紙等の上質紙の供給に寄与する。
このいずれも添加量が少ないので、従来法によるパルプ
でもよいが、PA法によるパルプであることは品質向上
のうえからさらに望ましい。PA法による蒸解条件は、
わらパルプにあってはバガスのパルプ化条件が適用で
き、コットンパルプにあってはジュ−トのパルプ化条件
が適用できる[0008] By blending straw pulp and cotton pulp, it has become possible to provide a high-quality printing paper which is 100% non-wood pulp and which has more favorable printability and texture, and a method for producing the same. In particular, the blending of straw pulp contributes to the improvement of printability, and the blending of cotton pulp contributes to the supply of high quality paper such as printing paper and writing paper having a luxurious feel.
Both of them have a small amount of addition, so that pulp by the conventional method may be used, but pulp by the PA method is more preferable from the viewpoint of quality improvement. Cooking conditions by the PA method are as follows:
Bagasse pulping conditions can be applied to straw pulp, and jute pulping conditions can be applied to cotton pulp.
【0009】抄紙は安く大量供給が可能なバガスパルプ
を70〜95%、好ましくは85〜90%(残りはジュ
−ト屑のパルプ又は及びコットンパルプとわらパル
プ)、と出来るだけ高い率で配合できるので、出来得れ
ば強度の大きいバガスパルプを用いるようにすること
が、つなぎパルプの使用量を減らすことを可能とする。
叩解は全てのパルプを混合して同時に行うよりも、それ
ぞれ別個に叩解する方が、つなぎパルプの配合率が低く
し、強度の大きいバガス紙を得るのに好ましい。混合し
てパルプを叩解するときは、バガスは強い叩解を行って
も強度があまり上がらずに濾水度が下がるなどの、抄紙
工程のトラブルを起こしやすくする。いずれの叩解で
も、CSFが350〜650mL、好ましくはCSFが
450〜550mLに止めるのが望ましい。屑ジュ−ト
は未利用資源として比較的豊富で、PA法で得られるパ
ルプは強度の叩解をして強度を上げるよりも捩れの起き
るのを抑えて、CSF400〜600mL、好ましくは
CSF450〜550mLに工程を管理することが望ま
しい。[0009] The papermaking can be mixed with bagasse pulp, which can be supplied in large quantities at a low cost, at a rate as high as possible with 70 to 95%, preferably 85 to 90% (the remainder is jute pulp or cotton pulp and straw pulp). Therefore, if possible, the use of bagasse pulp having a high strength makes it possible to reduce the amount of tethered pulp used.
It is preferable to beat each separately, rather than mixing all the pulp at the same time, in order to obtain a bagasse paper having a low blending ratio of the connecting pulp and a high strength. When beaten by mixing pulp, bagasse tends to cause troubles in the paper making process, such as a decrease in freeness without a significant increase in strength even after strong beating. In any beating, it is desirable to keep the CSF at 350-650 mL, preferably at 450-550 mL. The waste jute is relatively abundant as an unused resource, and the pulp obtained by the PA method suppresses the occurrence of twisting rather than beating the strength and increases the strength to 400 to 600 mL of CSF, preferably 450 to 550 mL of CSF. It is desirable to control the process.
【0010】わらパルプは紙の表面平滑性を良くし印刷
適性の向上に寄与するが、叩解を軽度に抑えることは抄
紙工程において水切れの低下を防げるのでCSF400
〜600mL好ましくはCSF450〜550mLに工
程を管理することが望ましい。[0010] Straw pulp improves the surface smoothness of the paper and contributes to the improvement of printability. However, suppressing beating to a small extent can prevent a decrease in drainage in the papermaking process, so that CSF400 is used.
It is desirable to manage the process to ~ 600 mL, preferably CSF 450-550 mL.
【0011】コットンパルプは印刷用バガス紙の風合い
の向上に寄与し、高級感を出すのによいが、叩解を進め
ないと紙の表面を極度に損ねることがあるのでCSF1
50〜500mL、好ましくはCSF200〜300m
Lに工程を管理することが望ましい。[0011] Cotton pulp contributes to the improvement of the texture of bagasse paper for printing and is good for giving a high-grade feel. However, if the beating is not advanced, the surface of the paper may be extremely damaged.
50-500 mL, preferably CSF200-300 m
It is desirable to control the process to L.
【0012】つなぎパルプとして屑ジュ−トから得られ
たパルプの配合率は5〜30%、好ましくは10〜20
%である。補助原料として用いるわらパルプは配合率は
3〜15%で、コットンパルプの配合率は5〜10%で
ある。The blending ratio of pulp obtained from waste jute as a connecting pulp is 5 to 30%, preferably 10 to 20%.
%. Straw pulp used as an auxiliary raw material has a compounding ratio of 3 to 15%, and cotton pulp has a compounding ratio of 5 to 10%.
【0013】抄紙助剤としてサイズ剤及び填料等を通常
添加する。サイズ剤は紙に適度の耐水性を持たせ、にじ
み止めを行うもので、従来の代表的なロジンサイズは、
紙を酸性にしてサイズを行うので、文書の長期保存を可
能とする上で、中性サイズが好ましい。中性サイズ剤と
してはアルキルケテンダイマ−、等通常使われているも
のの内から選べるし、CMCやにかわサイズ等の表面サ
イズを行うことも出来る。填料は紙の不透明度を上げる
ために有効で、特に使用パルプにペントサンが多く含ま
れるバガス稲わら等のパルプは叩解することにより紙の
密度が上がりパリパリするとともに不透明度が下がり裏
抜けが激しくなるが、本発明によればジュ−トパルプに
よって無理な叩解を進めないので、填料の添加の必要性
は少なくなる。もし加えるならば填料としてチャイナク
レイ、タルク、チタンホワイト等を5〜40%、好まし
くは10〜25%加える。A sizing agent, a filler and the like are usually added as a papermaking aid. The sizing agent gives the paper moderate water resistance and prevents bleeding.
Since the paper is acidified for sizing, a neutral size is preferable for enabling long-term storage of the document. The neutral sizing agent can be selected from commonly used ones such as alkyl ketene dimer and the like, and a surface size such as CMC or glue size can also be used. Filler is effective to increase the opacity of paper, especially pulp such as bagasse rice straw, which contains a lot of pentosan in the pulp used, is beaten to increase the density of the paper and increase the crispness, decrease the opacity and increase the strikethrough However, according to the present invention, the necessity of beating with the jute pulp does not proceed, so that the necessity of adding a filler is reduced. If added, add 5-40%, preferably 10-25% of China clay, talc, titanium white, etc. as filler.
【0014】抄紙は薄物の少量生産には円網、短網等の
ヤンキ−マシン、中、重量の多層紙のうち、大量生産に
は円網抄紙機が、通常の紙の大量生産には長網又はツイ
ンワイヤ−マシンによるのが好ましい。キャレンダ−又
はス−パ−キャテンダ−による処理は紙の表面を更に平
滑にするのに効果がある。Papermaking is performed by a yankee machine such as a circular net or a short net for small-scale production of thin materials. Among medium- and heavy-weight multilayer papers, a circular-mesh papermaking machine is used for mass production, and a long-sized paper is used for mass production of ordinary paper. Preference is given to mesh or twin-wire machines. Treatment with a calender or a super-cattender is effective in further smoothing the surface of the paper.
【0015】[0015]
【発明の効果】バガスパルプ主体で比較的少ない副原料
パルプを南の未利用資源から得て、良質の100%非木材パ
ルプの印刷用紙と、その製造が可能となった。According to the present invention, a relatively small amount of auxiliary pulp mainly composed of bagasse pulp can be obtained from unused resources in the south, and high-quality 100% non-wood pulp printing paper can be manufactured.
【0016】[0016]
【実施例】次に本発明を実施例により更に説明するが、
本発明はこの実施例によって限定されるものではない。Next, the present invention will be further described with reference to Examples.
The present invention is not limited by this embodiment.
【0017】実施例1 バガスのAP法による晒パルプ82%に屑ジュ−トのP
A法の晒パルプ18%を用いた。バガスパルプはCSF
530mLまで叩解し、これにジュ−トパルプをCSF
480mLまで叩解し、両者を合わせアルキルケテンダ
イマ−0.3%を加えて中性サイズを施し、填料として
チャイナクレイ7%を加えて、長網マシンによって米坪量
55g/m2のバガス紙を得、さらにス−パ−カレンダ
−にかけて印刷用上質紙を得た。EXAMPLE 1 82% bleached pulp of bagasse by the AP method of bagasse was treated with P
18% bleached pulp from Method A was used. Bagasse pulp is CSF
Beat to 530 mL and add jute pulp to CSF
Was beaten to 480 mL, subjected to neutral sizing by adding -0.3% alkyl ketene dimer combined both added 7% China clay as a filler, bagasse paper basis weight amount 55 g / m 2 by Fourdrinier machine The resulting paper was further subjected to a super calendar to obtain high quality paper for printing.
【0018】実施例2 バガスのPA法による晒パルプ80%に屑ジュ−トのP
A法の晒パルプ10%、わらのPA法による晒パルプ3
%、コットンリンタ−パルプ7%とを用いた。バガスパ
ルプはCSF500mLまで叩解し、これにジュ−トパ
ルプをCSF400mLまで叩解し、わらパルプはCS
F500mLまで叩解し、コトンリンタ−パルプはCS
F150mLまで叩解し、叩解後4 者合わせアルキルケ
テンダイマ−0.3%を加えて中性サイズを施し、填料
としてチタンホワイト7%を加えて、短網マシンによって
米坪量45g/m2のバガス紙を得、さらにカレンダ−
にかけて印刷用上質紙を得た。EXAMPLE 2 Pulverized jute P was added to 80% bleached pulp by the bagasse PA method.
10% bleached pulp of Method A, bleached pulp of straw PA method 3
% And cotton linter-pulp 7%. Bagasse pulp is beaten to CSF 500 mL, and jute pulp is beaten to CSF 400 mL, and straw pulp is CS
F. Beat to 500 mL, cotton linter-pulp is CS
It was beaten to F150mL, subjected to neutral sizing by adding 4's alignment alkyl ketene dimer -0.3% after beating, the addition of 7% titanium white as a filler, bagasse US basis weight 45 g / m 2 by Tan'ami machine Paper, calendar
To obtain high quality paper for printing.
Claims (4)
主成分とし、補原料としてジュ−ト屑PA法のパルプ、
及び所望により抄紙助剤を用いることを特徴とする非木
材パルプ100%の上質紙(バガス紙−a)とその製造
方法。1. A pulp made of bagasse (sugar milled pulp) as a main component, and a pulp obtained by a jute waste PA method as an auxiliary material.
And 100% non-wood pulp high-quality paper (bagasse paper-a) characterized by using a papermaking aid as required, and a method for producing the same.
法のパルプの他にわらパルプ又は及びコットンパルプを
用いる請求項1の上質紙とその製造方法。2. A jute waste PA as an auxiliary raw material pulp.
The high-quality paper according to claim 1, wherein straw pulp or cotton pulp is used in addition to the pulp of the method.
パルプがPA法パルプである請求項1及び2の上質紙と
その製造方法。3. Straw pulp or cotton linter
3. A high quality paper and a method for producing the high quality paper, wherein the pulp is PA pulp.
請求項1、2、及び、3の上質紙とその製造方法。4. The high quality paper according to claim 1, wherein a sizing agent and a filler are used as a papermaking auxiliary, and a method for producing the high quality paper.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001170575A JP2002363880A (en) | 2001-06-06 | 2001-06-06 | HIGH QUALITY PAPER WITH 100% NON-WOOD PULP (BAGASSE PAPER-a) AND METHOD FOR PRODUCING THE SAME |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001170575A JP2002363880A (en) | 2001-06-06 | 2001-06-06 | HIGH QUALITY PAPER WITH 100% NON-WOOD PULP (BAGASSE PAPER-a) AND METHOD FOR PRODUCING THE SAME |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2002363880A true JP2002363880A (en) | 2002-12-18 |
Family
ID=19012472
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001170575A Pending JP2002363880A (en) | 2001-06-06 | 2001-06-06 | HIGH QUALITY PAPER WITH 100% NON-WOOD PULP (BAGASSE PAPER-a) AND METHOD FOR PRODUCING THE SAME |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2002363880A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20180029764A1 (en) * | 2016-07-26 | 2018-02-01 | Footprint International, LLC. | Methods and Apparatus For Manufacturing Fiber-Based Meat Containers |
| CN108086057A (en) * | 2017-12-08 | 2018-05-29 | 马鞍山虹润彩印有限责任公司 | It is a kind of using dogstail as the preparation method of the wrapping paper of raw material |
-
2001
- 2001-06-06 JP JP2001170575A patent/JP2002363880A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20180029764A1 (en) * | 2016-07-26 | 2018-02-01 | Footprint International, LLC. | Methods and Apparatus For Manufacturing Fiber-Based Meat Containers |
| US10428467B2 (en) * | 2016-07-26 | 2019-10-01 | Footprint International, LLC | Methods and apparatus for manufacturing fiber-based meat containers |
| CN108086057A (en) * | 2017-12-08 | 2018-05-29 | 马鞍山虹润彩印有限责任公司 | It is a kind of using dogstail as the preparation method of the wrapping paper of raw material |
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