JP2002212888A - Method for producing banana pulp for japanese paper - Google Patents
Method for producing banana pulp for japanese paperInfo
- Publication number
- JP2002212888A JP2002212888A JP2001004324A JP2001004324A JP2002212888A JP 2002212888 A JP2002212888 A JP 2002212888A JP 2001004324 A JP2001004324 A JP 2001004324A JP 2001004324 A JP2001004324 A JP 2001004324A JP 2002212888 A JP2002212888 A JP 2002212888A
- Authority
- JP
- Japan
- Prior art keywords
- pulp
- banana
- japanese paper
- hemp
- banana pulp
- 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
- 235000018290 Musa x paradisiaca Nutrition 0.000 title claims abstract description 33
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 13
- 240000005561 Musa balbisiana Species 0.000 title 1
- 241000234295 Musa Species 0.000 claims abstract description 34
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 14
- 244000025254 Cannabis sativa Species 0.000 claims abstract description 13
- 235000012766 Cannabis sativa ssp. sativa var. sativa Nutrition 0.000 claims abstract description 13
- 235000012765 Cannabis sativa ssp. sativa var. spontanea Nutrition 0.000 claims abstract description 13
- 235000009120 camo Nutrition 0.000 claims abstract description 13
- 235000005607 chanvre indien Nutrition 0.000 claims abstract description 13
- 239000011487 hemp Substances 0.000 claims abstract description 13
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 239000007864 aqueous solution Substances 0.000 claims abstract description 5
- 238000000034 method Methods 0.000 claims description 23
- 238000010411 cooking Methods 0.000 claims description 12
- 239000003513 alkali Substances 0.000 claims description 10
- 239000003518 caustics Substances 0.000 claims description 7
- 238000010025 steaming Methods 0.000 claims description 7
- 150000004056 anthraquinones Chemical class 0.000 claims description 5
- 235000019353 potassium silicate Nutrition 0.000 claims description 3
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 3
- 239000002738 chelating agent Substances 0.000 claims 1
- 239000000835 fiber Substances 0.000 abstract description 13
- 230000007613 environmental effect Effects 0.000 abstract description 7
- 239000002994 raw material Substances 0.000 abstract description 6
- 239000000243 solution Substances 0.000 abstract description 4
- 239000000463 material Substances 0.000 abstract description 3
- 229910001854 alkali hydroxide Inorganic materials 0.000 abstract 1
- 150000008044 alkali metal hydroxides Chemical class 0.000 abstract 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 15
- 239000002699 waste material Substances 0.000 description 10
- 239000000126 substance Substances 0.000 description 8
- 238000004537 pulping Methods 0.000 description 7
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 6
- 240000000907 Musa textilis Species 0.000 description 4
- 229920001131 Pulp (paper) Polymers 0.000 description 4
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 description 4
- 241001265525 Edgeworthia chrysantha Species 0.000 description 3
- 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 3
- 230000000694 effects Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000002023 wood Substances 0.000 description 3
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- 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 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 2
- 235000021015 bananas Nutrition 0.000 description 2
- 239000002585 base Substances 0.000 description 2
- 238000004061 bleaching Methods 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 238000007873 sieving Methods 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 235000010265 sodium sulphite Nutrition 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- INPHIYULSHLAHR-UHFFFAOYSA-N 1-pentylanthracene-9,10-dione Chemical compound O=C1C2=CC=CC=C2C(=O)C2=C1C=CC=C2CCCCC INPHIYULSHLAHR-UHFFFAOYSA-N 0.000 description 1
- BDDLHHRCDSJVKV-UHFFFAOYSA-N 7028-40-2 Chemical compound CC(O)=O.CC(O)=O.CC(O)=O.CC(O)=O BDDLHHRCDSJVKV-UHFFFAOYSA-N 0.000 description 1
- 241000272814 Anser sp. Species 0.000 description 1
- 240000006248 Broussonetia kazinoki Species 0.000 description 1
- 235000006716 Broussonetia kazinoki Nutrition 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 1
- 235000003332 Ilex aquifolium Nutrition 0.000 description 1
- 235000002296 Ilex sandwicensis Nutrition 0.000 description 1
- 235000002294 Ilex volkensiana Nutrition 0.000 description 1
- 206010028980 Neoplasm Diseases 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 238000010009 beating Methods 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- 235000012255 calcium oxide Nutrition 0.000 description 1
- 201000011510 cancer Diseases 0.000 description 1
- 206010061592 cardiac fibrillation Diseases 0.000 description 1
- 238000009993 causticizing Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- XQRLCLUYWUNEEH-UHFFFAOYSA-N diphosphonic acid Chemical compound OP(=O)OP(O)=O XQRLCLUYWUNEEH-UHFFFAOYSA-N 0.000 description 1
- 239000010840 domestic wastewater Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 230000002600 fibrillogenic effect Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011121 hardwood Substances 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
- 238000007689 inspection Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000002932 luster Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 150000004045 organic chlorine compounds Chemical class 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000011122 softwood Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 150000003464 sulfur compounds Chemical class 0.000 description 1
- 239000002759 woven fabric Substances 0.000 description 1
Landscapes
- Paper (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明はバナナ原麻を原料と
する和紙用パルプの製造法に関する。TECHNICAL FIELD The present invention relates to a method for producing pulp for Japanese paper from banana raw hemp.
【0002】[0002]
【従来の技術】バナナの古木からアバカに形状が似た麻
状の粗繊維(以下バナナ原麻と呼ぶ)が抽出されること
は知られていたが、この粗繊維はアバカ(マニラ麻)に
比べ強度が劣りロ−プや織物など麻としての用途がない
ので、採取する者も殆ど無く、バナナの古木は大量に捨
てられてきた。2. Description of the Related Art It has been known that hemp-like crude fibers having a shape similar to abaca (hereinafter referred to as banana raw hemp) are extracted from old banana trees, but this crude fiber is compared with abaca (manila hemp). Since there is no use as hemp such as rope or woven fabric due to poor strength, there is almost no person who collects it, and a large amount of old banana trees have been discarded.
【0003】このバナナ原麻は亜硫酸ナトリウム水溶液
で高温処理する、いわゆる中性亜硫酸ソ−ダ法によりア
バカパルプに似た長繊維の化学パルプが約55%の高収
率で得られることは報告されているが、工業化には至ら
なかった。理由としては、バナナの中性亜硫酸パルプで
なければならないような用途が探せなかったこと、パル
プの製造に高温高圧に耐える大がかりな反応装置を必要
とすること、パルプ廃液の処理が容易でないことなどが
あげられる。[0003] It has been reported that the banana pulp can be treated at a high temperature with an aqueous solution of sodium sulfite, that is, a so-called neutral sodium sulfite method, in which a long fiber chemical pulp similar to abaca pulp can be obtained in a high yield of about 55%. However, it did not lead to industrialization. The reason was that we couldn't find an application that required banana to be neutral sulfite pulp, required a large-scale reactor to withstand high temperature and pressure for pulp production, and it was not easy to treat pulp waste liquid. Is raised.
【0004】KP法(クラフト法)は現在パルプ化法の
主流である。木材であれば針葉樹でも広葉樹でも樹種を
選ばずパルプ化出来るが、非木材のKP法のパルプは強
度に優れるが収率が劣り、色が暗褐色で、漂白に塩素系
の漂白剤を大量に必要とし、有機塩素化合物の発生対策
が容易でなく、またパルプの製造に際して極めて悪臭の
強い硫黄化合物が発生し、小規模の工場では環境対策が
困難なため、非木材パルプの製造にKP法を用いる例は
極めて少ない。特にバナナの原麻についてはKP法によ
る工業化の例も、パルプ化実験に関する報告も全くなか
った。[0004] The KP method (craft method) is currently the mainstream of the pulping method. For wood, softwood or hardwood can be pulped regardless of the type of wood, but non-wood KP pulp has excellent strength but poor yield, dark brown color, and large amounts of chlorine bleach for bleaching. It is not easy to take measures against the generation of organic chlorine compounds, and sulfur compounds with extremely bad smell are generated during pulp production, and environmental measures are difficult in small-scale factories. Very few examples are used. In particular, there was no report on industrialization of banana hemp by the KP method or pulping experiments.
【0005】さきに発明者はバナナの原麻をPA法(過
酸化水素−アルカリ法)の蒸解薬液(過酸化水素の苛性
アルカリの混合液)を用い高温高圧下で処理するだけ
で、パルプ化することに成功した。このPA法のバナナ
パルプは高収率(約55%)で、三椏(みつまた)及び
雁皮(がんぴ)のパルプに比べれば光沢こそ劣るが、強
度の優れた良質の長繊維パルプで、未晒でも白色度が高
く、漂白により容易に高白色度の晒パルプが得られた。
さらに用途開発も行い、和紙の製造やスピ−カ−コ−ン
の製造等に優れた素材として評価されて需要も量産体勢
も出来た。またPA法は亜硫酸ソ−ダ法やKP法とは異
なり硫黄を使わないパルプ化法なので悪臭の発生が無
い。パルプ廃液は濃縮燃焼により、廃液の高度処理がで
き、生成する炭酸アルカリを主成分とする灰は、生石灰
で苛性化することにより苛性アルカリの回収が同時にか
つ容易に出来るなど多くの利点があるため、PA法は工
業化にも成功した。[0005] The inventor of the present invention used only pulping of banana raw material under high temperature and high pressure by using a digestion solution (mixed solution of hydrogen peroxide and caustic alkali) of the PA method (hydrogen peroxide-alkali method). Was successful. The banana pulp produced by the PA method has a high yield (about 55%) and is less luster than pulp of Mitsumata (mitsumata) and goose (cancer). Even when bleached, the bleached pulp with high whiteness was easily obtained by bleaching.
In addition, the company developed applications, and was evaluated as an excellent material for the production of Japanese paper and speaker cones, and both demand and mass production were achieved. Unlike the sulfite method and the KP method, the PA method is a pulping method that does not use sulfur, so that no odor is generated. Pulp waste liquor can be subjected to advanced treatment of waste liquor by concentrated combustion, and the resulting ash mainly composed of alkali carbonate has many advantages such that caustic alkali can be simultaneously and easily recovered by causticizing with quick lime. The PA method has also been successfully industrialized.
【0006】しかし、PA法にとって最大の顧客であっ
てよい和紙工業界は、バナナのPA法のパルプが優れて
いるからといって外部から購入し、配合して用いる例は
むしろ稀であった。従来和紙工業界は特殊仕様の紙を極
めて少量ずつ製造するため、用いるパルプは楮(こう
ぞ)、三椏(みつまた)等を原料とし、紙の仕様に合っ
た最適のパルプを、その都度和紙工場の平釜などの簡易
な装置を用い、伝統技術で製造して使用していた。[0006] However, in the Washi industry, which may be the largest customer for the PA method, it is rather rare that bananas are purchased and compounded from the outside just because the pulp of the PA method is excellent. . Conventionally, the Japanese paper industry manufactures specially-specified paper in very small quantities, so the pulp used is made from kozo, mitsumata, etc., and the optimal pulp that meets the paper specifications is produced each time. It was manufactured and used by traditional techniques using a simple device such as a flat pot.
【0007】今日パルプ廃液を、濃縮燃焼処理するとと
もに薬品やエネルギギ−を回収する組み合わせは、極め
て経済的でエネルギ−節約型の廃液処理システムとして
支持されている。しかしこれは大掛かりなシステムで大
規模のパルプ工場でないと採用が経済的に困難で、木材
パルプ工場では日産1,000トン以上、非木材パルプ
工場では、通常100トン以上が常識とされてきた。し
かして、和紙の原料パルプの製造のように、大きくても
日産数トン規模のパルプを製紙工場ごとに製造する場合
には、排水処理は経済的に実施が困難なため、これに対
する環境規制は厳しくなかった。[0007] Today, the combination of pulp waste liquor condensing and burning and recovering chemicals and energy is supported as a very economical and energy-saving waste liquor treatment system. However, this is a large-scale system, and it is economically difficult to adopt it unless it is a large-scale pulp mill. In wood pulp mills, the daily production is more than 1,000 tons, and in non-wood pulp mills, usually 100 tons or more is common knowledge. However, when manufacturing pulp of at most several tons per day at each paper mill, as in the production of raw pulp for Japanese paper, wastewater treatment is difficult to implement economically. It was not severe.
【0008】しかし、家庭の生活雑排水が環境問題の厳
しく論議される状況下で、和紙工業を含む中小企業の排
水が現状のまま放置される時代が長く続かないと危惧さ
れている。和紙業界にあってはそのため、長期の展望を
立て難く、発展の大きな障害となっていた。However, under the circumstance where the domestic wastewater is severely debated on environmental issues, it is feared that the era in which the wastewater of small and medium-sized enterprises including the Washi Industry is left as it is will not continue for a long time. Therefore, in the Japanese paper industry, it was difficult to make a long-term outlook, and this was a major obstacle to development.
【0009】[0009]
【発明が解決しようとする課題】本発明の目的は、和紙
工場に付帯する極小規模のパルプ工場においても、優れ
たバナナパルプを、環境負荷を小さく且つ簡単に製造出
来る方法を提供する。SUMMARY OF THE INVENTION An object of the present invention is to provide a method for easily producing excellent banana pulp with a low environmental load even in a very small pulp mill attached to a Japanese paper mill.
【0010】[0010]
【課題を解決するための手段】本発明者は、上記の課題
を解決するため鋭意研究をし続けた結果、平釜の中にバ
ナナ原麻を苛性アルカリ水溶液とともに入れて常圧下で
煮沸して柔らかくし、ビ−タ−で機械的に処理したとこ
ろ長繊維パルプが得られるという事実を見いだした。Means for Solving the Problems As a result of continuing intensive studies to solve the above-mentioned problems, the present inventors put banana raw material together with a caustic alkali aqueous solution in a flat pot and boiled it under normal pressure. It was found that softening and mechanical treatment with a beater resulted in long fiber pulp.
【0011】即ち、以上の事実に基づき研究を続け、化
学パルプ化法によらずとも、常圧下での苛性アルカリ又
は及び過酸化水素による蒸煮と、ビ−タ−等による機械
処理との組み合わせからなる半化学パルプ化法で、バナ
ナの原麻から和紙用に適した光沢のある長繊維パルプが
極めて容易に高収率で得るとともに、同時に排水の環境
負荷を大幅に減らすことを可能にし、本発明を完成する
に至った。That is, based on the above facts, the research has been continued and, without using the chemical pulping method, the combination of steaming with caustic alkali or hydrogen peroxide under normal pressure and mechanical treatment with a beater or the like has been considered. This semi-chemical pulping method makes it possible to obtain high-yield glossy long-fiber pulp suitable for Japanese paper from banana hemp, while at the same time greatly reducing the environmental impact of wastewater. The invention has been completed.
【0012】[0012]
【発明の実施の形態】パルプの繊維原料としては、バナ
ナの幹(葉柄)から採取した麻状の繊維(原麻)を用い
る。通常原麻はバナナを採取する度に切り倒されて捨て
られる古木から採取できる。BEST MODE FOR CARRYING OUT THE INVENTION As a fiber raw material for pulp, hemp-like fibers (raw hemp) collected from banana trunks (stalks) are used. Normally, hemp can be collected from old trees that are cut down and discarded each time a banana is collected.
【0013】蒸煮液として用いる苛性アルカリは水酸化
ナトリウムに限らず水酸化カリウムでもよく、用いる量
は等モル数であれば同等の効果が期待出来る。この際炭
酸アルカリの混入は妨げない。水酸化ナトリウムを標準
とした場合、NaOHとして5〜40%、好ましくは1
5〜25%(以下使用薬品量は対原料絶乾物で表示)で
ある。The caustic alkali used as the cooking liquor is not limited to sodium hydroxide but may be potassium hydroxide. The same effect can be expected if the amount used is equimolar. At this time, mixing of alkali carbonate is not prevented. When sodium hydroxide is used as a standard, 5 to 40% as NaOH, preferably 1%
The amount is 5 to 25% (hereinafter, the amount of chemicals used is expressed in terms of absolute dry material).
【0014】過酸化水素の添加量はH2O2 として0.
5〜10%、好ましくは1〜5%である。The amount of hydrogen peroxide added is 0.1 as H 2 O 2 .
It is 5 to 10%, preferably 1 to 5%.
【0015】蒸煮の際、助剤として以下の少なくとも1
種以上を添加することが望ましい。過酸化水素の安定剤
として水ガラス及びDTPA(ディエチレン.トリアミ
ン.ペンタ.アセティックアシド)、EDTA(エチレ
ンジアミン.テトラアセティックアシド)及び、ジフォ
スフォン酸等のキレ−ト剤及びアントラキノン、アミル
アントラキノン、タ−シャルブチルアントラキノン等の
アントラキノン類が挙げられる。使用量としては水ガラ
スは0.1〜3%、好ましくは0.3〜1%で、キレ−
ト剤は0.05〜2%、好ましくは0.1〜0.5%
で、アントラキノン類は0.02〜0.5%、好ましく
は0.03〜0.2%である。At the time of steaming, at least one of the following
It is desirable to add more than one species. Water glass and chelates such as DTPA (diethylene. Triamine. Penta. Acetic acidide), EDTA (ethylenediamine. Tetraacetic acid) and diphosphonic acid, and anthraquinone, amyl anthraquinone, -Anthraquinones such as charbutyl anthraquinone. The amount of water glass used is 0.1-3%, preferably 0.3-1%.
Agent is 0.05-2%, preferably 0.1-0.5%
The content of anthraquinones is 0.02 to 0.5%, preferably 0.03 to 0.2%.
【0016】液比は1.5〜10 リットル/kgで、
気相蒸煮では好ましくは2〜3リットル/kg、液相蒸
煮では好ましくは5〜8リットル/kgである。The liquid ratio is 1.5 to 10 liter / kg.
For gas-phase cooking, it is preferably 2-3 liters / kg, and for liquid-phase cooking, it is preferably 5-8 liters / kg.
【0017】蒸煮時間は常圧下で、0.5〜5時間、気
相蒸煮では好ましくは0.5〜1.5時間、液相蒸煮で
は好ましくは1〜3時間である。The cooking time is 0.5 to 5 hours under normal pressure, preferably 0.5 to 1.5 hours for gas phase cooking, and preferably 1 to 3 hours for liquid phase cooking.
【0018】蒸煮後のバナナの原麻はビ−タ−、エッジ
ランナ−等を用いて機械的解繊処理を行えば、単繊維状
になり、パルプを高収率で、かつ環境負荷を少ない状態
で得ることができる。バナナパルプは光沢のある高白色
度の長繊維パルプではあるが解繊の際に繊維同志のもつ
れが少ないので、通常は効率のよいホレンダ−及びナイ
ヤガラビ−タ−等製紙工場にあるものが使え、必ずしも
効率の悪い薙刀(なぎなた)ビ−タ−を使う必要がな
い。特に繊維のもつれを防ぎ、かつ紙の強度を求めたい
場合はエッジランナ−の使用による解繊と叩解は効果的
である。If the raw banana after steaming is subjected to a mechanical fibrillation treatment using a beater, an edge runner or the like, it becomes a single fiber, and the pulp is produced in a high yield and with a low environmental load. Can be obtained at Although banana pulp is a long-fiber pulp with gloss and high whiteness, the fibers are less entangled during defibration, so that those which are usually used in efficient paper mills such as a holly and a niagaraviter can be used. It is not always necessary to use an inefficient naginata beater. In particular, when it is desired to prevent fiber entanglement and obtain the strength of the paper, defibration and beating by using an edge runner are effective.
【0019】パルプ廃液の処理に濃縮燃焼法を用いれば
有機物を一挙に片づけることが出来るが、本発明による
パルプの収率が高いので廃液の有機物の量は非常に少な
く、環境負荷が小さく生物処理及び凝集沈殿法等の化学
処理の装置は小さくてすむ。The use of the concentrated combustion method for the treatment of pulp waste liquid makes it possible to remove organic substances at once. Equipment for chemical treatment such as treatment and coagulation sedimentation method is small.
【0020】[0020]
【発明の効果】本発明は実施が容易で、大きな実施効果
が期待できる。The present invention is easy to carry out, and a great effect can be expected.
【0021】本発明は一種の半化学パルプ化法である
が、製造に当たって新たな設備は殆ど、または全く必要
としない。また反応は常圧で行うため、特に圧力容器と
して用いるものは地球釜を含めても全く無く、保守点検
が極めて容易である。約75%と言う極めて高収率で、
光沢がある高白色度のバナナの長繊維パルプが自家製で
供給可能となるので、国内の伝統的和紙メ−カ−の活性
化に役立つ。また高収率化により廃液中に溶出する有機
物の量を半分以下に減らす事ができ、排水処理を容易に
するとともに、環境負荷を一挙に約1/3に低減するこ
とが可能となる。蒸煮に際し、更にカリウムベ−スを用
いれば、パルプ廃液も当然カリウムベ−スとなるので、
肥料効果もあり、ナトリウムベ−スの廃液が下流の耕地
に与えるナトリウムによる塩害を無くすことも可能であ
る。Although the present invention is a type of semi-chemical pulping process, the production requires little or no new equipment. In addition, since the reaction is carried out at normal pressure, there is no particular use as a pressure vessel even if an earth pot is included, and maintenance and inspection are extremely easy. With a very high yield of about 75%,
Banana long-fiber pulp with gloss and high whiteness can be supplied on a home-made basis, which helps to activate domestic traditional Japanese paper manufacturers. Further, by increasing the yield, the amount of organic substances eluted in the waste liquid can be reduced to half or less, and the wastewater treatment can be facilitated, and the environmental load can be reduced to about 1/3 at a stroke. If a potassium base is used during steaming, the pulp waste liquid naturally becomes a potassium base.
There is also a fertilizer effect, and it is also possible to eliminate salt damage caused by sodium caused by sodium-based waste liquid on downstream arable land.
【0022】またプロセスと設備が単純なので、南のバ
ナナ生産国でも新規に小型のパルプ和紙の一貫工場の立
ち上げと、それに伴う雇用の創出も期待できる。In addition, since the process and equipment are simple, it is expected that even in the southern banana-producing countries, a new integrated small-sized pulp and paper mill will be started up and jobs will be created accordingly.
【0023】また副次的に、南の120ケ国で生産され
る4,500万トンのバナナとともに発生し、捨てられ
てきた大量の古木からバナナ原麻約50万トンがパルプ
原料とし採取されるようになれば、それに伴う新たな雇
用の創出も期待できる。As a secondary matter, about 500,000 tons of banana hemp are collected as pulp raw material from a large amount of abandoned trees generated with 45 million tons of bananas produced in 120 southern countries. In that case, new employment can be expected.
【0024】[0024]
【実施例】以下実施例をもって本発明をさらに説明す
る。ただし、本発明は当該実施例のみに限定されるもの
ではない。また、特に指定しない限り「%」は重量%を
指す。またパルプの収率は風乾パルプ(水分10%とし
て)に対する風乾原料(水分15%として)の重量%を
指すものとする。The present invention will be further described with reference to the following examples. However, the present invention is not limited only to the embodiment. Unless otherwise specified, "%" indicates% by weight. The pulp yield refers to the weight percent of air-dried raw material (as moisture 15%) based on air-dried pulp (as moisture 10%).
【0025】[0025]
【実施例1】バナナの古木から採取した良質のバナナ原
麻100kgを平釜に入れ、蒸煮液として、水酸化ナト
リウム15kgに水を加えて600リットルの蒸煮液と
し、、100℃で2時間蒸煮した。蒸煮後ホレンダ−で
30分間処理して離解し、得られたパルプに過酸化水素
(100%換算で)を3%、水酸化ナトリウム1%加え
て液比10リットル/kgで1昼夜放置し、C.S.
F.(カナディアン濾水度)680ミリリットル、白色
度61.4%の晒バナナパルプを74.4kg得た。得
られたバナナパルプはさらに、ホレンダ−で叩解し裂断
長6.9km、比破裂強さ4.5、比引き裂き強さ18
0であり、ふるい分け試験の結果14メッシュオン3
7.2%、28メッシュオン20.8%、100メッシ
ュオン9.9%、200メッシュオン14.2%、20
0メッシュパス17.9%であった。Example 1 100 kg of high-quality banana raw hemp collected from an old banana tree was put into a flat pot, and as a cooking solution, water was added to 15 kg of sodium hydroxide to make a 600 liter cooking solution, and steamed at 100 ° C. for 2 hours. did. After steaming, the mixture was treated with a hender for 30 minutes to disintegrate it, and 3% of hydrogen peroxide (in terms of 100%) and 1% of sodium hydroxide were added to the obtained pulp, and the mixture was allowed to stand at a liquid ratio of 10 L / kg for one day and night. C. S.
F. (Canadian freeness) 74.4 kg of bleached banana pulp having 680 ml and whiteness of 61.4% was obtained. The obtained banana pulp was further beaten with a hender, and the breaking length was 6.9 km, the specific burst strength was 4.5, and the specific tear strength was 18.
0 and the result of the sieving test is 14 mesh on 3
7.2%, 28 mesh on 20.8%, 100 mesh on 9.9%, 200 mesh on 14.2%, 20
0 mesh pass was 17.9%.
【0026】[0026]
【実施例2】バナナの古木から採取した良質のバナナ原
麻100kgを1m容のステンレス製の地球釜に入れ、
これに水酸化カリウム21kg、過酸化水素(100%
換算で)2.5kgとアントラキノン85gに水を加え
て300リットルの蒸煮液として加え、常圧下、100
℃で1.5時間回転させながら蒸煮した。蒸煮後エッジ
ランナ−で60分間処理し、C.S.F.520ミリリ
ットルで、光沢のある白色度65%のパルプを78.3
kg得た。このパルプは従来の収率55%のパルプに比
べパルプ廃液中に入る原麻の固形分量は下の式に示すよ
うに一挙に34%に削減できることが分かった。従来の
収率55%の化学パルプの場合 45:55=0.8
2であり、本発明の収率78.3%のパルプの場合 2
1.7:78.3=0.28で、その削減率は、0.2
8/0.82=0.34 と大きく削減が可能。得られ
たバナナパルプはさらに裂断長7.2km、比破裂強さ
4.7、比引き裂き強さ220を示し、ふるい分け試験
の結果は、14メッシュオン40.3%、28メッシュ
オン22.6%、100メッシュオン13.2%、20
0メッシュオン10.9%、200メッシュパス13.
0%であった。Example 2 100 kg of high-quality banana raw hemp collected from an old banana tree was put into a 1 m stainless steel earth pot,
21 kg of potassium hydroxide and hydrogen peroxide (100%
2.5 kg and 85 g of anthraquinone were added to water and added as 300 liters of a cooking liquid.
Steamed while rotating at 1.5 ° C. for 1.5 hours. After steaming, the mixture was treated with an edge runner for 60 minutes. S. F. 78.3 pulp of 520 ml with glossy whiteness of 65%
kg. It was found that the solid content of hemp in the pulp waste liquid can be reduced to 34% at a stroke as shown in the following formula, as compared with the conventional pulp having a yield of 55%. 45: 55 = 0.8 for a conventional 55% yield chemical pulp
2 in the case of the pulp having a yield of 78.3% according to the present invention.
1.7: 78.3 = 0.28, and the reduction rate is 0.2
8 / 0.82 = 0.34 can be greatly reduced. The obtained banana pulp further showed a breaking length of 7.2 km, a specific burst strength of 4.7 and a specific tear strength of 220. The results of the sieving test were as follows: 14 mesh on 40.3%, 28 mesh on 22.6 %, 100 mesh on 13.2%, 20
12. 0 mesh on 10.9%, 200 mesh pass
It was 0%.
Claims (2)
ナナ原麻を所望により蒸煮前に浸漬したるのち常圧下で
蒸煮するか、又は直ちに常圧下で蒸煮したるのち、ビ−
タ−又はエッジランナ−等で機械的に解繊することを特
徴とする和紙用バナナパルプの製造方法。1. An aqueous solution of caustic alkali is used as a cooking liquid, and banana raw hemp is immersed before steaming and then steamed under normal pressure, or immediately steamed under normal pressure, and then beaded.
A method for producing banana pulp for Japanese paper, which comprises mechanically defibrating with a tar or an edge runner.
化水素を加え、所望により蒸煮助剤として水ガラス、キ
レ−ト剤、アントラキノン類のうち少なくとも1種を加
えることを特徴とする請求項1の和紙用バナナパルプの
製造方法。2. A method according to claim 1, wherein hydrogen peroxide is added to an aqueous solution of caustic alkali as a cooking liquid, and at least one of water glass, a chelating agent and anthraquinones is optionally added as a cooking aid. Production method of banana pulp for Japanese paper.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001004324A JP2002212888A (en) | 2001-01-12 | 2001-01-12 | Method for producing banana pulp for japanese paper |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001004324A JP2002212888A (en) | 2001-01-12 | 2001-01-12 | Method for producing banana pulp for japanese paper |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2002212888A true JP2002212888A (en) | 2002-07-31 |
Family
ID=18872529
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001004324A Pending JP2002212888A (en) | 2001-01-12 | 2001-01-12 | Method for producing banana pulp for japanese paper |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2002212888A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2372432C2 (en) * | 2004-09-16 | 2009-11-10 | Папирус Австралия Лимитед | Method and device for removal of fibre leaves from herbaceous part of banana plants for production of cotton goods |
-
2001
- 2001-01-12 JP JP2001004324A patent/JP2002212888A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2372432C2 (en) * | 2004-09-16 | 2009-11-10 | Папирус Австралия Лимитед | Method and device for removal of fibre leaves from herbaceous part of banana plants for production of cotton goods |
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