JP2000170090A - Japanese paper-like bagasse paper as paper form for unconventional name card, letter paper or the like, and production of the same - Google Patents
Japanese paper-like bagasse paper as paper form for unconventional name card, letter paper or the like, and production of the sameInfo
- Publication number
- JP2000170090A JP2000170090A JP10358403A JP35840398A JP2000170090A JP 2000170090 A JP2000170090 A JP 2000170090A JP 10358403 A JP10358403 A JP 10358403A JP 35840398 A JP35840398 A JP 35840398A JP 2000170090 A JP2000170090 A JP 2000170090A
- Authority
- JP
- Japan
- Prior art keywords
- pulp
- paper
- bagasse
- millet
- strength
- 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 27
- 239000010905 bagasse Substances 0.000 title claims abstract description 27
- 238000004519 manufacturing process Methods 0.000 title abstract description 7
- 238000010411 cooking Methods 0.000 claims abstract description 22
- 239000000835 fiber Substances 0.000 claims abstract description 21
- 229920001131 Pulp (paper) Polymers 0.000 claims abstract description 11
- 238000005520 cutting process Methods 0.000 claims abstract description 5
- 238000000034 method Methods 0.000 claims description 35
- 244000062793 Sorghum vulgare Species 0.000 claims description 18
- 235000019713 millet Nutrition 0.000 claims description 18
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 16
- 239000002994 raw material Substances 0.000 claims description 16
- 239000007788 liquid Substances 0.000 claims description 10
- 239000003513 alkali Substances 0.000 claims description 9
- 244000138286 Sorghum saccharatum Species 0.000 claims description 7
- 235000011684 Sorghum saccharatum Nutrition 0.000 claims description 7
- 240000000111 Saccharum officinarum Species 0.000 claims description 6
- 235000007201 Saccharum officinarum Nutrition 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 150000004056 anthraquinones Chemical class 0.000 claims description 5
- 239000002738 chelating agent Substances 0.000 claims description 5
- 239000000126 substance Substances 0.000 claims description 5
- 238000010009 beating Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 239000003495 polar organic solvent Substances 0.000 claims description 4
- 239000012670 alkaline solution Substances 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 150000002681 magnesium compounds Chemical class 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 239000002699 waste material Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 abstract description 3
- 241000283690 Bos taurus Species 0.000 abstract 3
- 240000008114 Panicum miliaceum Species 0.000 abstract 2
- 235000007199 Panicum miliaceum Nutrition 0.000 abstract 2
- 239000004615 ingredient Substances 0.000 abstract 2
- 239000002075 main ingredient Substances 0.000 abstract 2
- 239000002023 wood Substances 0.000 abstract 2
- 239000000123 paper Substances 0.000 description 41
- 239000000243 solution Substances 0.000 description 7
- 238000007796 conventional method Methods 0.000 description 6
- 230000029087 digestion Effects 0.000 description 6
- 238000005406 washing Methods 0.000 description 5
- 230000006378 damage Effects 0.000 description 4
- 239000012071 phase Substances 0.000 description 4
- 241000209134 Arundinaria Species 0.000 description 3
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 3
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 3
- 238000004061 bleaching Methods 0.000 description 3
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- -1 magnesium compound Magnesium oxide Chemical class 0.000 description 3
- 244000025254 Cannabis sativa Species 0.000 description 2
- 235000012766 Cannabis sativa ssp. sativa var. sativa Nutrition 0.000 description 2
- 235000012765 Cannabis sativa ssp. sativa var. spontanea Nutrition 0.000 description 2
- 240000000907 Musa textilis Species 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- 235000009120 camo Nutrition 0.000 description 2
- 239000003518 caustics Substances 0.000 description 2
- 235000005607 chanvre indien Nutrition 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- OSVXSBDYLRYLIG-UHFFFAOYSA-N dioxidochlorine(.) Chemical compound O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 description 2
- 239000001963 growth medium Substances 0.000 description 2
- 239000011487 hemp Substances 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- 239000000395 magnesium oxide Substances 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 238000004537 pulping Methods 0.000 description 2
- 238000004513 sizing Methods 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- HSKPJQYAHCKJQC-UHFFFAOYSA-N 1-ethylanthracene-9,10-dione Chemical compound O=C1C2=CC=CC=C2C(=O)C2=C1C=CC=C2CC HSKPJQYAHCKJQC-UHFFFAOYSA-N 0.000 description 1
- 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
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- QPCDCPDFJACHGM-UHFFFAOYSA-N N,N-bis{2-[bis(carboxymethyl)amino]ethyl}glycine Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(=O)O)CCN(CC(O)=O)CC(O)=O QPCDCPDFJACHGM-UHFFFAOYSA-N 0.000 description 1
- 229910004742 Na2 O Inorganic materials 0.000 description 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N Na2O Inorganic materials [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 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
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000002419 base digestion Methods 0.000 description 1
- 108010051210 beta-Fructofuranosidase Proteins 0.000 description 1
- 230000009172 bursting Effects 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 235000019398 chlorine dioxide Nutrition 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000011033 desalting Methods 0.000 description 1
- XQRLCLUYWUNEEH-UHFFFAOYSA-N diphosphonic acid Chemical compound OP(=O)OP(O)=O XQRLCLUYWUNEEH-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003623 enhancer Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 229960004903 invert sugar Drugs 0.000 description 1
- 235000011073 invertase Nutrition 0.000 description 1
- 239000001573 invertase Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 239000002609 medium Substances 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 235000013379 molasses Nutrition 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 235000020374 simple syrup Nutrition 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- MWNQXXOSWHCCOZ-UHFFFAOYSA-L sodium;oxido carbonate Chemical compound [Na+].[O-]OC([O-])=O MWNQXXOSWHCCOZ-UHFFFAOYSA-L 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000002351 wastewater Substances 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、木材パルプを全く
用いずに非木材パルプのみを用いた、個性的な和紙風の
名刺用紙及び便箋用紙等のバガス紙及びその製造法に関
わる。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a unique Japanese paper-like bagasse paper such as business card paper and stationery paper using only non-wood pulp without using any wood pulp, and a method for producing the same.
【0002】[0002]
【従来の技術】こうぞ、みつまた等の靱皮パルプやアバ
カ等の長繊維パルプを用いた和紙又は和紙風の用紙を用
いた名刺、便箋及び封筒等を使うことは個性的な贅沢な
趣味として一部で行なわれてきた。最近、地球環境に対
する関心が高まるにつけ、全く木材パルプを用いずに1
00%非木材パルプの紙を求め名刺や便箋にして使うこ
とが行なわれだしたが、本来和紙の原料として使われる
長繊維パルプは高価である。一方従来のバガス(砂糖キ
ビの搾り粕)のパルプは安く求められるが、繊維が短く
濾水性が悪く抄紙適性が低く、化学的にはペントサン含
有量が多いため、得られる紙は密度が高く、硬く、引き
裂き強度等諸強度が低く、パリパリになりやすく、代用
品的に評価されるため、高級感を求める人々には好まれ
なかった。2. Description of the Related Art The use of business cards, stationery, envelopes, and the like made of Japanese paper or Japanese paper using long fiber pulp, such as bast pulp, abaca, etc., is one of the unique luxury hobbies. Department has been done. Recently, as the interest in the global environment has increased, the use of wood pulp
It has been practiced to use 00% non-wood pulp paper for business cards and stationery, but long fiber pulp, which is originally used as a raw material for Japanese paper, is expensive. On the other hand, conventional pulp of bagasse (sugar millet pulp) is required at a low price, but the resulting paper has a high density because the fibers are short, the drainage is poor, the suitability for papermaking is low, and the pentosan content is high chemically. It was hard, had low strength such as tear strength, was easily crisp, and was evaluated as a substitute.
【0003】[0003]
【発明が解決しようとする課題】本発明が解決しようと
する課題とは、従来法で得られたバガスパルプを主原料
とし、繊維の長いキビ類のラインドパルプをつなぎに用
い、木材パルプを用いないで嵩だかで、長い繊維を残し
た高級感のある和紙風の名刺、便箋等の用紙とその製造
方法を提供することを課題とする。The problem to be solved by the present invention is that bagasse pulp obtained by a conventional method is used as a main raw material, and lined pulp of millet having a long fiber is used for connection, and wood pulp is not used. It is an object of the present invention to provide a high-class Japanese paper-like business card, stationery and the like paper which is bulky and retains long fibers, and a method for producing the same.
【0004】[0004]
【課題を解決するための手段】本発明者は、前記課題を
解決すべく鋭意研究を重ねた結果、本発明を完成するに
至った。すなわち、本発明によれば、砂糖キビ及びスウ
ィ−トソルガム等、砂糖を得るために栽培されるキビ類
の幹茎から長い繊維が損なわれないようにラインドを取
り出し、ラインドをアルカリ性の蒸解薬液で蒸解し繊維
の長い状態で濾水性の良いパルプをつなぎ用に取り出
し、これを従来のバガスパルプと配合し叩解を軽度にす
ませることによって、長い繊維の形態を残し、麻等の長
繊維パルプを殆ど又は全く用いること無く、嵩だかで強
度等の性能もあり、地球環境に優しいことを主張しう
る、個性的な名刺便箋等に使える和紙風の用紙と、その
製造方法が提供される。Means for Solving the Problems The inventors of the present invention have conducted intensive studies to solve the above-mentioned problems, and as a result, have completed the present invention. That is, according to the present invention, a line is taken out from stems of millet cultivated to obtain sugar, such as sugar cane and sweet sorghum, so that long fibers are not damaged, and the line is digested with an alkaline cooking chemical. In the state of long fibers, take out pulp with good drainage for connection, mix it with conventional bagasse pulp and lightly beat it, leaving long fiber form, almost or no long fiber pulp such as hemp There is provided a Japanese paper-like paper which can be used for unique business card letter paper and the like, which can be claimed to be environmentally friendly without being bulky and has high performance such as strength.
【0005】[0005]
【発明の実施の形態】本発明で使われるつなぎ用パルプ
の原料植物は砂糖キビ又は及びスウィ−トソルガム等糖
液、さらには糖を得るために栽培されているキビ類であ
る。これら糖液を取るキビ類は外側が硬いラインドと、
内部はピス(髄質)及びケインジュ−スからなる。本発
明でこれらキビ類を、強いつなぎ用のパルプの原料とす
ることを可能とした最大のものは、前処理として従来製
糖工場でしたようにざくざくに破砕せずに、第1工程と
してキビ類の幹茎を斜めにかつ並行に厚み3〜60m
m、好ましくは厚み6〜30mmに並行に切断し、脱汁
したのちピスとケインジュ−スを分離除去することによ
って、キビの長い繊維を痛めずにパルプ原料となる長い
ラインドとして、大量の取り出しを可能にしたことにあ
る。これは幹茎を斜めに同じ30mmの厚さに切るにし
ても、幹茎に直角に切れば得られるラインドの長さは3
0mmであるが、30°に切れば幹茎の厚みは30mm
で長さは60mmとなり、20°に切れは厚みは30m
mで長さは88mmとなることでもその効果が説明され
る。BEST MODE FOR CARRYING OUT THE INVENTION The raw material of the connecting pulp used in the present invention is sugar cane or sugar syrup such as sweet sorghum, and millet cultivated to obtain sugar. The millet that takes these sugar solutions has a hard line on the outside,
The interior is composed of pis (medulla) and cane juice. In the present invention, the largest millet that can be used as a raw material for pulp for strong connection is milling as a first step without crushing the mill as in a conventional sugar mill as a pretreatment. Of the stem of the trunk diagonally and in parallel 3-60m thick
m, preferably 6 to 30 mm in thickness, cut in parallel, and after dewatering, separate and remove pis and cane juice to remove large amounts of long milled fiber as a long line that becomes a raw material for pulp without damaging long fibers. It is made possible. This means that even if the stem is cut diagonally to the same thickness of 30 mm, the line length obtained by cutting the stem at right angles is 3 mm.
0mm, but if cut at 30 °, the thickness of the stem is 30mm
And the length becomes 60mm, and the cut at 20 ° is 30m thick
The effect is also explained when the length becomes 88 mm in m.
【0006】長いラインドはキビ類の幹茎を斜めに切
り、糖液とカス(バガス)とを分離し、バガスから更に
ピスを分離することによって収得することができる。用
いる装置としては、まず幹茎を斜めに切断するにはチッ
パ−又は類似の機械が用いられる。キビ類のチップの脱
汁にはスクリュ−プレスの他、従来の製糖工場で用いて
いたロ−ルプレスのような圧縮脱汁装置が一番搾りには
適し、バガスの洗浄と残糖の回収には向流洗浄機能を有
する回収装置及びデフュ−ザ−装置等が効率よく使用で
きる。一番搾りの濃い糖液からは極良質の黒糖が得られ
る。また、薄いが無色透明な回収糖液は非発酵成分が少
ないので、酵母等の製造に用いれば、従来の暗褐色の廃
糖蜜を培地に用いるのに比べ、その排水は極めてきれい
で地球に対する環境負荷を少なくすることが可能であ
る。本発明の搾り粕中のラインドとピスの分離は乾式法
でも湿式法でも容易に行なわれる。ラインドは濾水性が
良く、引き裂き強度及び諸強度の大きいパルプの原料と
なる。従来法では砂糖キビから糖液を搾る際にバガス中
のラインドもピスも籾殻のように破砕され第3の中間成
分とも言える微細繊維ができる。そのため荒く砕かれた
ラインドから細かく破砕されたラインドやピスとを分離
除去するのが困難で、得られるパルプも微細繊維とピス
が多く含まれ濾水性が悪く、引裂き強度をはじめ諸強度
小さかった。[0006] A long line can be obtained by cutting the stem of millet obliquely, separating the sugar solution from the scum (bagasse), and further separating the pis from the bagasse. As a device to be used, a chipper or a similar machine is used to cut the stem stem diagonally. In addition to screw presses, compression desiccation equipment such as the roll press used in conventional sugar factories is most suitable for squeezing millet chips, for bagasse washing and residual sugar recovery. The collection device and the diffuser device having the countercurrent washing function can be used efficiently. Highest quality brown sugar can be obtained from the sugar solution that is the most squeezed. In addition, since the thin but colorless and transparent recovered sugar liquid has few non-fermented components, its wastewater is extremely clean and environmentally friendly to the earth when used for the production of yeast, etc., compared to the conventional dark brown molasses used as a culture medium. It is possible to reduce the load. The separation of line and pis in the pomace of the present invention can be easily performed by either a dry method or a wet method. Lined has good drainage and is a raw material for pulp with high tear strength and various strengths. In the conventional method, when the sugar solution is squeezed from sugar cane, both the line and the pis in bagasse are crushed like rice hulls, and fine fibers which can be said to be the third intermediate component are formed. For this reason, it was difficult to separate and remove finely crushed lines and pis from coarsely crushed lines. The resulting pulp also contained many fine fibers and pis, had poor drainage, and had low strength including tear strength.
【0007】第2工程のアルカリ性蒸解薬液による蒸解
は、苛性アルカリのみの水溶液を蒸解薬液とするAP
法、苛性アルカリと硫化アルカリの混合液を蒸解薬液と
するKP法及びPA(過酸化水素−アルカリ法)法等が
ある。PA法は過酸化水素のアルカリ溶液に下記の蒸解
助剤のうち少なくとも1種以上加えたものを蒸解薬液と
するパルプ化法である。In the second step of cooking with an alkaline cooking liquor, an AP using an aqueous solution containing only caustic alkali as the cooking liquor is used.
And a KP method and a PA (hydrogen peroxide-alkali method) method using a mixture of caustic alkali and alkali sulfide as a cooking chemical. The PA method is a pulping method in which at least one or more of the following cooking aids is added to an alkaline solution of hydrogen peroxide to prepare a cooking chemical liquid.
【0008】PA法の蒸解助剤としてはキレ−ト剤、ア
ントラキノン類、マグネシウム化合物、水と任意に混ざ
り合う極性の有機溶剤、所望により酸素等が挙げられ
る。PA法で用いるアルカリ溶液はカリウム又はナトリ
ウムの水酸化物で、その炭酸塩が共存することは更に望
ましい。アルカリの量は(以下原料ラインドの対絶乾量
表示)活性アルカリがNa2 O換算で13〜30%、好
ましくは17〜22%、苛性化率は50〜95%、好ま
しくは70〜85%で、炭酸塩が共存することによって
繊維の損傷が少なく、パルプの高収率化が望める。過酸
化水素、又は及び過炭酸等水に投入して過酸化水素を放
出する過酸化物の使用量はH2 O2 換算で0.5〜15
%で、好ましくは1.0〜5%である。蒸解助剤の使用
量は、各種助剤により異なるが、キレ−ト剤は0.02
〜1%、好ましくは0.1〜0.3%である。アントラ
キノン類は0.003〜1%、好ましくは0.05〜
0.3%である。マグネシウム化合物は0.05〜0.
5%、好ましくは0.1〜0.3%である。水と任意に
混ざり合う極性の有機溶剤は0.02〜1%で好ましく
は0.05〜0.3%である。[0008] Examples of the cooking aid in the PA method include a chelating agent, anthraquinones, a magnesium compound, a polar organic solvent that can be arbitrarily mixed with water, and oxygen if desired. The alkaline solution used in the PA method is a hydroxide of potassium or sodium, and it is more desirable that the carbonate thereof coexist. The amount of alkali (hereinafter referred to as the absolute dry weight of the raw material line) is 13 to 30%, preferably 17 to 22% in terms of Na2O, and the causticization ratio is 50 to 95%, preferably 70 to 85%. In addition, due to the coexistence of carbonates, fiber damage is small, and a high yield of pulp can be expected. The amount of peroxide used to release hydrogen peroxide when injected into water such as hydrogen peroxide or percarbonate is 0.5 to 15 in terms of H2 O2.
%, Preferably 1.0 to 5%. The amount of the cooking aid used varies depending on the type of auxiliary, but the amount of the chelating agent is 0.02.
11%, preferably 0.1-0.3%. Anthraquinones are 0.003 to 1%, preferably 0.05 to
0.3%. The magnesium compound is 0.05 to 0.1.
5%, preferably 0.1 to 0.3%. The polar organic solvent arbitrarily mixed with water is 0.02 to 1%, preferably 0.05 to 0.3%.
【0009】PA法によるラインドの蒸解は過酸化水素
との接触に耐えるステンレス等の材質を用いた容器の中
に、ラインドとPA法の蒸解薬液(所望により酸素を圧
入)を加えて蒸解を行う。蒸解温度は90〜180℃、
好ましくは110〜150℃、蒸解時間は10〜360
分、好ましくは20〜120分である。液比は液相蒸解
で3〜12L/kg、好ましくは5.0〜7.0L/k
gである。気相蒸解では1.2〜3.0L/kgで、好
ましくは1.5〜2.5L/kgである。気相蒸解によ
れば蒸気原単位を下げることが可能であり、パルプ廃液
を高濃度で回収可能であるので、濃縮装置等を小さくす
ることも、濃縮用の蒸気量を減らすことができるので、
地球環境に優しく、且つ経済的にも有利である。PA法
によれば得られるパルプがAP法に比べ収率が高く、強
度が優れる。またKP法に比べれば、悪臭が発生せず、
環境対策が極めて容易であり、パルプ収率が高く、未晒
パルプの色が遙に薄く、漂白も容易なため経済的にも有
利である。[0009] In the digestion of lined by the PA method, the lined and the cooking liquid of the PA method (optionally pressurized with oxygen) are added to a vessel made of a material such as stainless steel that can withstand contact with hydrogen peroxide. . Cooking temperature is 90 ~ 180 ℃,
Preferably 110-150 ° C, digestion time 10-360.
Minutes, preferably 20 to 120 minutes. The liquid ratio is 3 to 12 L / kg, preferably 5.0 to 7.0 L / k by liquid phase cooking.
g. In the gas phase digestion, it is 1.2 to 3.0 L / kg, preferably 1.5 to 2.5 L / kg. According to the gas-phase cooking, it is possible to reduce the unit steam consumption, and it is possible to collect the pulp waste liquid at a high concentration, so that it is possible to reduce the size of a concentrating device and the like, and to reduce the amount of steam for concentration.
It is environmentally friendly and economically advantageous. According to the PA method, the pulp obtained is higher in yield and superior in strength than the AP method. Also, compared to the KP method, no odor is generated,
Environmental measures are extremely easy, the pulp yield is high, the color of unbleached pulp is much lighter, and bleaching is easy, which is economically advantageous.
【0010】第3工程の和紙風の用紙の抄紙は、上記の
つなぎパルプと従来のバガスパルプのみを用いて行なう
ことができるし、従来強度及び高級感を与えるのに効果
があるとされてきた麻等の長繊維パルプの添加をほとん
ど又は全く無しに済ますことも可能である。主原料とし
て用いるバガスパルプはAP法、KP法及びPA法等、
アルカリ性の蒸解薬液を用いて製造するパルプ法が用い
ることができるが、特にPA法によるパルプは未晒でも
白色度が高く、引っ張り強度や破裂強度等が大きく、漂
白性もよいので、その使用が好ましい。抄紙は常法によ
って行なわれる。すなわち、長網抄紙機、ツウィンワイ
ヤ−マシン、多槽式の円網抄紙機又は短網ヤンキ−マシ
ン等による抄紙が可能である。抄紙に先立ってデスクリ
ファイナ−又はビ−タ−により濾水度がC.S.F.で
400〜650cc、好ましくは500〜650cc程
度に軽く叩解が行われるが、キビ類のラインドをPA法
でパルプ化したパルプは濾水度が高い分だけ、軽い叩解
によって諸強度を増加させることができるので、嵩だか
でかつ繊維の形状を残した和紙風の用紙の製造に都合が
良い。抄紙に際しては好みによりサイズ剤、湿紙強度増
強剤その他の助剤を加え原質濃度0.1〜0.8%、好
ましくは0.3〜0.5%で抄紙機のワイヤ−パ−ト供
給する。供給された原質はワイヤ−パ−トで湿紙を形成
し、プレスパ−トに送り水を搾り、さらにドライパ−ト
送って乾燥し、密度0.3〜0.7g/cc好ましくは
0.35〜0.55g/ccの嵩だかの強くて和紙風の
用紙に仕上げる。In the third step, papermaking of Japanese paper can be carried out using only the above-mentioned tethered pulp and conventional bagasse pulp, and hemp has conventionally been said to be effective in providing strength and luxury. It is also possible to add little or no long fiber pulp. Bagasse pulp used as the main raw material can be obtained by AP method, KP method, PA method, etc.
A pulp method manufactured using an alkaline cooking liquid can be used. Particularly, pulp produced by the PA method has a high degree of whiteness, a high tensile strength and a high bursting strength, and a good bleaching property even when not exposed, so its use is good. preferable. Papermaking is performed by a conventional method. That is, paper making by a fourdrinier paper machine, a twin-wire machine, a multi-tank-type round paper machine or a short net yankee machine is possible. Prior to papermaking, the freeness is adjusted to C.I. by a desk refiner or a beater. S. F. 400 to 650 cc, preferably about 500 to 650 cc, but the milled pulp obtained by pulping the millet line by the PA method can increase various strengths by light beating as much as the freeness is high. Since it is possible, it is convenient for manufacturing Japanese paper-like paper which is bulky and retains the fiber shape. At the time of paper making, a sizing agent, a wet paper strength enhancer and other auxiliaries are added according to preference, and the original material concentration is 0.1 to 0.8%, preferably 0.3 to 0.5%, and the wire part of the paper machine is used. Supply. The raw material supplied is formed into a wet paper with a wire part, sent to a press part to squeeze water, and further sent to a dry part for drying, and has a density of 0.3 to 0.7 g / cc, preferably 0.1 to 0.7 g / cc. The paper is finished in a strong, Japanese paper style with a bulk of 35 to 0.55 g / cc.
【発明の効果】本発明によれば、バガスパルプを主原料
とし、つなぎパルプとしてキビ類のラインドパルプを用
いることにより、木材パルプを用いることなしに、非木
材パルプのみで嵩だかの和紙風の名刺便箋等個性的な用
紙を提供するとともに、その製造方法の提供ができる。
すなわち、従来バガスパルプは強度が低くて単味では通
常の坪量の紙の製造は不可とされてきた。また、坪量の
大きい厚紙を抄紙するために強い叩解を行なえば原料中
にペントサン含有量が大きいため、濾水性はさらに悪く
なり抄紙は困難となり、得られる紙は硬くパリパリにな
りやすかった。本発明では原料植物のキビ類を斜めにか
つ並行に切断することにより、長いラインドを取り出
し、これをアルカリ蒸解、好ましくはPA蒸解すること
によって、従来低いとされてきた濾水性を上げ、引き裂
き高度をはじめとする諸強度の大きいパルプを得、これ
をつなぎパルプとして使うことにより叩解を軽く、又は
全く行なわないでも強度があり、嵩だかで繊維の形状を
多く残した和紙風のバガス紙を製造することが可能とな
った。According to the present invention, by using bagasse pulp as a main raw material and using millet lined pulp as a connecting pulp, a business card of Japanese paper style which is bulky only with non-wood pulp without using wood pulp. It is possible to provide a unique sheet of paper such as stationery and a method of manufacturing the same.
That is, conventionally, bagasse pulp has a low strength, and it has been considered impossible to produce paper having a normal basis weight simply. Further, if strong beating was performed to make a cardboard having a large basis weight, the pentosan content in the raw material was large, so that drainage was further deteriorated, making papermaking difficult, and the resulting paper was hard and crisp. In the present invention, a long line is taken out by cutting the millet of the raw material plant diagonally and in parallel, and this is subjected to alkali digestion, preferably PA digestion, to increase the drainage which has been conventionally regarded as low, and to increase the tearing height. And other pulp with high strength, and use it as a connecting pulp to produce Japanese paper bagasse paper that is light, beaten, or strong at all and has a large bulk of fibers. It became possible to do.
【0012】[0012]
【実施例】次に、本発明を実施例によって更に具体的に
説明するが、本発明はこの実施例によって限定されな
い。Next, the present invention will be described more specifically with reference to examples, but the present invention is not limited to these examples.
【0013】[0013]
【実施例1】Embodiment 1
【0014】砂糖キビの幹茎3,000kgを回転板に
2枚の刃を30°の角度で固定した原動機付きのチッパ
−で厚み20mm、長さ40mmの砂糖キビのチップを
作った。砂糖キビチップをスクリュ−プレスで固形分4
5%になるまで破壊脱汁した。破壊脱汁して得たケイン
ジュ−スは常法により濃縮し、良質の一番搾りの黒糖を
得た。破壊脱汁後の砂糖キビチップは向流洗浄機で残糖
を洗い出し酵母の培地に利用した。残糖を洗い出し後、
バガスは再度スクリュ−プレスで搾ったのち、乾式で原
動機付きの10メッシュの振動篩を用いピスとラインド
を分離除去し、長さ約35mmの脱糖、脱ピスして得ら
れたラインドを絶乾量換算で210kg得た。A sugar millet chip having a thickness of 20 mm and a length of 40 mm was prepared with a chipper equipped with a motor in which 3,000 kg of sugar cane stem was fixed to a rotating plate with two blades fixed at an angle of 30 °. Sugar millet chips with a screw press for solid content 4
It was disrupted and desalted to 5%. The cane juice obtained by destruction and desiccation was concentrated by a conventional method to obtain a high-quality first-squeezed brown sugar. Sugar millet chips after destruction and desiccation were washed with a countercurrent washing machine to remove residual sugar and used as a yeast medium. After washing out the residual sugar,
Bagasse was squeezed again with a screw press, and the pis and line were separated and removed using a 10-mesh vibrating sieve with a dry motor in a dry system. 210 kg was obtained in terms of quantity.
【0015】ラインドはナトリウムベ−スのPA法(液
比を1.8L/kg、活性アルカリ:Na2 Oとして1
8%、苛性化率85%、過酸化水素:H2 O2 として3
%、キレ−ト剤としてDTPAを0.3%,アントラキ
ノン類としてエチルアントラキノンを0.1%、水に任
意に混ざり合う極性の有機溶剤としてNMP(ノルマル
メチルピロリドン)を0.1%、マグネシウム化合物と
して酸化マグネシウムを0.2%で125℃、2時間)
の気相蒸解を行った。このPA法の気相蒸解で得られた
未晒パルプは、さらに2段晒を行なった。すなわち、第
1段にアルカリ性過酸化水素処理、第2段に二酸化塩素
処理して、白色度83%、濾水度C.S.F.715c
c、裂断長5.8km、比破裂強度3.4、比引き裂き
強度106のキビ類の晒ラインドパルプを対ラインド5
0%の収率で得た。The sodium salt-based PA method (liquid ratio 1.8 L / kg, active alkali: Na 2 O 1
8%, causticization rate 85%, hydrogen peroxide: 3 as H2 O2
%, DTPA as a chelating agent 0.3%, ethyl anthraquinone as anthraquinones 0.1%, NMP (normal methylpyrrolidone) as a polar organic solvent arbitrarily mixed with water 0.1%, magnesium compound Magnesium oxide at 0.2% at 125 ° C for 2 hours)
Was subjected to gas phase digestion. The unbleached pulp obtained by the gas phase cooking in the PA method was further subjected to two-stage bleaching. That is, the first stage is treated with alkaline hydrogen peroxide, the second stage is treated with chlorine dioxide, and the whiteness is 83% and the freeness is C.I. S. F. 715c
c, bleached milled pulp having a breaking length of 5.8 km, a specific burst strength of 3.4, and a specific tear strength of 106 was compared with a lined pulp of 5
Obtained in 0% yield.
【0016】上質紙の抄紙はバガスのAP法によるパル
プ(白色度81.8%、濾水度C.S.F.500c
c、裂断長2.8km、比破裂強度2.3、比引き裂き
強度45、)を70%に、ラインドの晒PA法パルプを
濾水度C.S.F.650ccまで叩解したものを30
%を配合し、アルキルケテンダイマ−を0.2%加え、
原質濃度0.3%、試験用の長網抄紙機を用いて常法に
より抄紙し、和紙風の用紙(密度0.45g/cc、白
色度82.8%、裂断長4.8km、比破裂強度3.
0、比引き裂き強度87)を得た。The high quality paper is made of bagasse pulp (whiteness 81.8%, freeness CSF 500c) by the AP method.
c, tear length 2.8 km, specific burst strength 2.3, specific tear strength 45) to 70%, and the bleached PA method pulp with a freeness of C.I. S. F. 30 beaten to 650cc
%, Adding 0.2% of alkyl ketene dimer,
A paper was made by a conventional method using a fourdrinier paper machine for testing with an original material concentration of 0.3%, and washi-style paper (density: 0.45 g / cc, whiteness: 82.8%, breaking length: 4.8 km, 2. Specific burst strength
0, specific tear strength 87).
【0017】[0017]
【実施例2】砂糖キビの幹茎を実施例1で得られたPA
法のパルプ10%と、アバカの屑をPA法で実施例1と
同一条件で蒸解して得られたパルプ(裂断長9.2k
m、比破裂強度4.5、比引き裂き強度189)5%、
をバガスの従来法の晒AP85%と配合し、ディスクリ
ファイナ−で濾水度C.S.F.510ccまで叩解
し、中性サイズ剤を加え試験用の長網抄紙機を用い常法
で米坪量120g/m2の和紙風の名刺用紙と、60g
/m2の便箋用紙と85g/m2の便箋用紙を得た。名刺
用紙は、密度0.47g/cc裂断長3.8km、比破
裂強度2.9、比引き裂き強度85を示し、他の紙もほ
ぼ同等の値を示した。EXAMPLE 2 The sugar cane stem was used to obtain PA obtained in Example 1.
Pulp obtained by digesting abaca waste by the PA method under the same conditions as in Example 1 (break length 9.2 k)
m, specific burst strength 4.5, specific tear strength 189) 5%,
Was blended with 85% of the conventional bleached AP of bagasse, and the freeness C.I. S. F. Beat to 510 cc, add a neutral sizing agent, use a fourdrinier paper machine for testing, and use a conventional method of Japanese paper business card paper with a basis weight of 120 g / m 2 and 60 g.
/ Yield stationery paper stationery paper and 85 g / m 2 of m 2. The business card paper showed a density of 0.47 g / cc, a breaking length of 3.8 km, a specific burst strength of 2.9, and a specific tear strength of 85, and other papers also showed almost the same values.
【0018】[0018]
【実施例3】キビ類としてスウィ−トソルガムの幹茎を
2,000kgを回転板に2枚の刃を30°の角度で固
定した原動機付きのチッパ−で厚み15mm、長さ30
mmのチップを作った。スウィ−トソルガムのチップは
スクリュ−プレスで固形分43%まで破壊脱汁した。破
壊脱汁して得た糖液はインヴァ−タ−ゼを固定したバイ
オリアクタ−で処理し、転化糖を収得した。破壊脱汁後
のチップは向流洗浄機で残糖を洗い出し4.5%の濃度
の糖液を回収し、食糧酵母の培地として利用した。糖を
洗い出した後バガスは再度スクリュ−プレスで搾ったの
ち、原動機付き10メッシュの振動篩でピスとラインド
を分離除去し、長さ約30mmの脱糖、脱ピスして得ら
れたラインドを絶乾量換算で150kg得た。脱糖、脱
ピスして得られたラインドはカリウムベ−スのPA蒸解
薬液(液比1.8L/kg、活性アルカリ:Na2 Oと
して18%、苛性化率85%、過酸化水素:H2 O2 と
して3%、キレ−ト剤として1−ヒドロキシエタン−1
−1ジホスホン酸を0.3%、アントラキノンを0.1
%、NMPを0.1%、酸化マグネシウムを0.2%)
で125℃、2時間の気相蒸解を行なった。このPA法
の気相蒸解により、白色度52%、カッパ−価4、濾水
度C.S.F.710cc、裂断長6.7km、比破裂
強度4.0、比引き裂き強度120、のスウィ−トソル
ガムの未晒のPA法パルプが対ラインド52%で得られ
た。同パルプは実施例1の砂糖キビの未晒パルプと同様
の条件で2段漂白してスウィ−トソルガムの晒パルプと
した。上質紙の抄紙は実施例2で用いた同一ロットのバ
ガスのAP法による晒パルプ80%と、ラインドの晒P
A法パルプを20%とを配合し、アルキルケテンダイマ
−を0.2%加え、原質濃度0.3%で、試験用の長網
抄紙機を用いて常法により抄紙し、米坪量125g/m
2の名刺用紙を得た。この用紙は密度0.47g/c
c、裂断長3.8km、比破裂強度2.9、比引き裂き
強度85を示した。Embodiment 3 2,000 kg of sweet sorghum stems as millet are mounted on a rotating plate with a motor-driven chipper having two blades fixed at an angle of 30 °, with a thickness of 15 mm and a length of 30 mm.
mm chips were made. Sweet sorghum chips were disrupted and desalted to 43% solids with a screw press. The sugar solution obtained by disruptive desalting was treated in a bioreactor having immobilized invertase to obtain invert sugar. After destruction and desiccation, the chips were washed with a countercurrent washing machine to remove residual sugar, and a 4.5% concentration sugar solution was recovered and used as a culture medium for food yeast. After the sugar was washed out, the bagasse was squeezed again with a screw press, and then the piss and the line were separated and removed with a 10-mesh vibrating sieve equipped with a motor. 150 kg was obtained in terms of dry weight. The line obtained by desugaring and depissing is a potassium-based PA digestion solution (liquid ratio 1.8 L / kg, active alkali: 18% as Na2 O, causticization rate 85%, hydrogen peroxide: H2 O2). 3%, 1-hydroxyethane-1 as a chelating agent
-1 diphosphonic acid 0.3%, anthraquinone 0.1%
%, NMP 0.1%, magnesium oxide 0.2%)
At 125 ° C. for 2 hours. By the PA method, whiteness was 52%, kappa number was 4, and freeness was C.I. S. F. An unbleached PA pulp of sweet sorghum of 710 cc, a breaking length of 6.7 km, a specific burst strength of 4.0 and a specific tear strength of 120 was obtained at a line ratio of 52%. This pulp was bleached in two stages under the same conditions as the unbleached sugar mill pulp of Example 1 to obtain a sweet sorghum bleached pulp. The papermaking of high quality paper was 80% bleached pulp by the AP method of bagasse of the same lot used in Example 2 and bleached P of lined.
A method pulp was blended with 20%, an alkyl ketene dimer was added at 0.2%, and the raw material concentration was 0.3%. 125 g / m
2 business card paper was obtained. This paper has a density of 0.47 g / c
c, the breaking length was 3.8 km, the specific burst strength was 2.9, and the specific tear strength was 85.
Claims (5)
いキビ類のラインド(幹の厚い皮)のパルプを従として
つなぎ用に配合し木材パルプを用いない、丈夫で嵩だか
であることを特徴とする個性的な名刺便箋等の用紙とし
ての和紙風のバガス紙。(1) It is mainly made of ordinary bagasse pulp, and is a tough and bulky material which is blended with a long-fiber millet lined pulp (thick bark of the trunk) for connection and uses no wood pulp. Japanese paper bagasse paper as paper for personalized business cards such as letter paper.
パルプを、軽く又は全く叩解せずにつなぎ用パルプと
し、これに通常の方法で得たバガスパルプを軽く又は全
く叩解せずに主原料とし、木材パルプを用いずに完全試
料を調製し、丈夫で嵩だかなバガス紙を抄造する請求項
1の方法。2. The milled lined pulp obtained in a long fiber state is used as a connecting pulp without beating lightly or at all, and the bagasse pulp obtained by a usual method is used as a main raw material without lightly or completely beating. The method according to claim 1, wherein a complete sample is prepared without using wood pulp, and a strong and bulky bagasse paper is formed.
キビ類の幹茎を斜め、かつ並行に切断し、脱汁、脱ピス
し、繊維の長い状態でキビ類のラインドをパルプ原料と
して取り出すのを第1工程とし、ラインドをアルカリ性
蒸解薬液で処理し、引き裂き強度をはじめ諸強度の大き
い化学パルプをつなぎ用のラインドパルプとして得るの
を第2工程とし、パルプ廃液は濃縮燃焼し、アルカリと
エネルギ−を回収し、アルカリは次回のアルカリ蒸解用
薬液を回収し、再利用するのを第3工程とする請求項
1、及び2の方法。3. The process of cutting the stem of sugarcane or millet such as sweet sorghum diagonally and in parallel, draining and depissing, and extracting the millet line as a pulp raw material in a long fiber state. In a first step, the line is treated with an alkaline cooking chemical, and in a second step, a chemical pulp having high tear strength and various strengths is obtained as a lined pulp for connection. The pulp waste liquid is concentrated and burned, and alkali and energy are removed. 3. The method according to claim 1, wherein the third step is to collect and reuse the chemical for alkali cooking next time.
の、アルカリ性の蒸解薬液が、PA法(過酸化水素のア
ルカリ溶液に蒸解助剤として、キレ−ト剤、アントラキ
ノン類、マグネシウム化合物、酸素及び水と任意の割合
で混合する極性の有機溶剤のうち少なくとも1種以上を
含む液で蒸解する)の蒸解薬液である請求項1、2及び
3の方法。4. An alkaline cooking liquor for obtaining lined pulp for tethering is prepared by the PA method (a chelating agent, anthraquinones, magnesium compounds, oxygen and water as an auxiliary cooking aid in an alkaline solution of hydrogen peroxide). And a liquid containing at least one kind of polar organic solvent mixed at an arbitrary ratio with the above).
の、アルカリ性の蒸解薬液が、PA法の蒸解薬液である
請求項1、2、3及び4の方法。5. The method according to claim 1, wherein the alkaline cooking liquor for obtaining bagasse pulp as a main raw material is a cooking liquor of the PA method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10358403A JP2000170090A (en) | 1998-12-03 | 1998-12-03 | Japanese paper-like bagasse paper as paper form for unconventional name card, letter paper or the like, and production of the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10358403A JP2000170090A (en) | 1998-12-03 | 1998-12-03 | Japanese paper-like bagasse paper as paper form for unconventional name card, letter paper or the like, and production of the same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2000170090A true JP2000170090A (en) | 2000-06-20 |
Family
ID=18459122
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10358403A Pending JP2000170090A (en) | 1998-12-03 | 1998-12-03 | Japanese paper-like bagasse paper as paper form for unconventional name card, letter paper or the like, and production of the same |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2000170090A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103031778A (en) * | 2012-12-10 | 2013-04-10 | 桂林奇峰纸业有限公司 | Method for producing translucent paper by utilizing bagasse pulp |
| US20180029764A1 (en) * | 2016-07-26 | 2018-02-01 | Footprint International, LLC. | Methods and Apparatus For Manufacturing Fiber-Based Meat Containers |
-
1998
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103031778A (en) * | 2012-12-10 | 2013-04-10 | 桂林奇峰纸业有限公司 | Method for producing translucent paper by utilizing bagasse pulp |
| 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 |
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