JPS6030309A - Manufacture of composite product from lignocellulose material - Google Patents

Manufacture of composite product from lignocellulose material

Info

Publication number
JPS6030309A
JPS6030309A JP58124224A JP12422483A JPS6030309A JP S6030309 A JPS6030309 A JP S6030309A JP 58124224 A JP58124224 A JP 58124224A JP 12422483 A JP12422483 A JP 12422483A JP S6030309 A JPS6030309 A JP S6030309A
Authority
JP
Japan
Prior art keywords
sugar
water
sugars
lignocellulosic
soluble
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
Application number
JP58124224A
Other languages
Japanese (ja)
Inventor
Chiyan Shien Kuu
クー チヤン シエン
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP58124224A priority Critical patent/JPS6030309A/en
Priority to NL8302960A priority patent/NL8302960A/en
Priority to GB08323003A priority patent/GB2142943B/en
Priority to DE19833333032 priority patent/DE3333032A1/en
Priority to IN1142/CAL/83A priority patent/IN161051B/en
Priority to FR8316190A priority patent/FR2549768A1/en
Priority to KR1019830004872A priority patent/KR920000756B1/en
Priority to SU833656698A priority patent/SU1212318A3/en
Priority to MX199301A priority patent/MX172616B/en
Priority to IT23636/83A priority patent/IT1169684B/en
Priority to ZA838301A priority patent/ZA838301B/en
Priority to BR8306450A priority patent/BR8306450A/en
Priority to DK554583A priority patent/DK554583A/en
Priority to PH29979A priority patent/PH19188A/en
Publication of JPS6030309A publication Critical patent/JPS6030309A/en
Pending legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H5/00Special paper or cardboard not otherwise provided for
    • D21H5/12Special paper or cardboard not otherwise provided for characterised by the use of special fibrous materials
    • D21H5/14Special paper or cardboard not otherwise provided for characterised by the use of special fibrous materials of cellulose fibres only
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H1/00Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/40Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
    • D04H1/54Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties by welding together the fibres, e.g. by partially melting or dissolving

Abstract

PURPOSE:To produce a composite product without adding adhesive bonding agent by a method in which finely crushed raw material composed of lignocellulose material containing sugar is formed into a desired mat after it has been dried, and then it is formed under heating and pressurizing. CONSTITUTION:The raw material composed of the lignocellulose material containing sugar (e.g. the bagasse of sugar cane, cone cane and sunflower cane, etc.) is finely crushed, and is divided into particle, fiber, strand and flake. After this finely crushed material has been dried, it is formed into a desired mat. This mat is press-heated under sufficient pressure and in sufficient time to compress the formed product at the temperature equal to or higher than 180 deg.C. The kinds of liberated sugar and saccharid are chemically sophisticated under pressurizing and heating and act as adhering and reinforcing agent. The formed product excellent in strength, dimensional stability and resistance for boiled water and aid hydrolyzing may be obtained without adding other adhesive bonding agent or adhesive.

Description

【発明の詳細な説明】 トウモロコシの茎、ヒマワリの茎、アマの茎及び他のリ
グノセルロース材料類、とりわけ、水溶性で抽出容易な
糖類、炭水化物類又はサツカリド類を含有する非樹木性
植物のものから複合製品を製造することに関する。
DETAILED DESCRIPTION OF THE INVENTION Corn stalks, sunflower stalks, flax stalks and other lignocellulosic materials, especially those of non-arboreal plants containing water-soluble and easily extractable sugars, carbohydrates or saccharides. Relating to manufacturing composite products from.

更に詳しくは、本発明は、糖含有リグノセルロース材料
類、例えばサトウキビのバガス、モロコシの茎、トウモ
ロコシの茎、ヒマワリの茎、アマの茎等から、接着結合
剤又は接着剤を添加することなく、複合製品を製造する
ことに関する。この製造は遊離糖類、炭水化物類又はサ
ツカリド類を、鍾 熱を加えて接着剤兼増声剤として利用することにより達
成される。
More particularly, the present invention provides for the production of sugar-containing lignocellulosic materials such as sugarcane bagasse, sorghum stalks, corn stalks, sunflower stalks, flax stalks, etc., without the addition of adhesive binders or adhesives. Concerning manufacturing composite products. This production is accomplished by using free sugars, carbohydrates or saccharides as an adhesive and voice enhancer with the addition of heat.

サトウキビバガスのパネル製品の慣用の製造においては
、フェノール−ホルムアルデヒド及び尿素−ホルムアル
デヒドの如き合成熱硬化性樹脂結合剤が慣用的に使用さ
れており、この場合、外装グレードの製品については一
層高価なフェノール−ホルムアルデヒドが使用されてい
る。複合製品の全材料費の大部分は慣用樹脂結合剤のせ
いである。高価な樹脂結合剤を使用することなく複合製
品を製造することは経済的に魅力がある。更に又、無結
合剤製造システムは製造法を簡単にし、かつ混合作業及
び装置を無くすことにより製造費を減少する。それ故、
複合製品の製造において無結合剤法を使用することが望
ましいことが経済的及び技術的観点から容易に理解され
るであろう。
In the conventional manufacture of sugarcane bagasse panel products, synthetic thermosetting resin binders such as phenol-formaldehyde and urea-formaldehyde are conventionally used, in which case the more expensive phenol binders are used for exterior grade products. -Formaldehyde is used. A large portion of the total material cost of a composite product is due to conventional resin binders. It is economically attractive to produce composite products without the use of expensive resin binders. Furthermore, the binderless manufacturing system simplifies the manufacturing process and reduces manufacturing costs by eliminating mixing operations and equipment. Therefore,
It will be readily appreciated from an economic and technical point of view that it is desirable to use binderless methods in the manufacture of composite products.

バガスパネル製品の慣用製造法においては、髄及び残存
遊離糖の除去は良質のパネル製品にとつて不可欠である
。この髄は真の繊維と比べて非常に短い、薄壁の細胞で
あって、一層高い比率の糖を含有しているが、最終製品
の強度に寄与しない。
In the conventional manufacturing process of bagasse panel products, removal of pith and residual free sugars is essential for a good quality panel product. This pith is a very short, thin-walled cell compared to true fibers, and although it contains a higher proportion of sugars, it does not contribute to the strength of the final product.

髄は綿毛状であるため、殊に液状樹脂を使用した場合、
過剰の樹脂結合剤を吸収することになろう。
Since the pulp is fluffy, especially when using liquid resin,
It will absorb excess resin binder.

髄は又、スポンジのようにはたらき、バガス複合パネル
製品からこれを除去しない場合、水を吸上げ過度に膨潤
する。又、バガスは、茎の種類、その成熟度、収穫法及
び精微粉砕装置の効率に左右されるが、通常のコないし
6%の残存糖を含有している。バガス中の残存糖は加工
前に除去し又は最小量にされ々ければ、ボード製造及び
それにつぐ使用のさいに問題を生ずる可能性がある。糖
はバガスボード製造の際に使用する慣用の樹脂結合剤と
化学的に相溶性であっては々らず、結合を妨害し、乏し
い強度を生ずる可能性がある。残存糖が熱間圧縮中に化
学的に改質されるか消費されるのでなければ、糖は、バ
ガスボードが湿潤条件にさらされる時、醗酵を始め、か
くして不快臭を発し、遂には化学的及び生物学的劣化を
生ずることになる。このことはバガスポードの使用にお
ける有効寿命を実質上、短縮することになろう。
The pith also acts like a sponge and, if not removed from the bagasse composite panel product, will wick water and swell excessively. Bagasse also typically contains between 0 and 6% residual sugar, depending on the type of stalk, its maturity, the harvesting method and the efficiency of the fine grinding equipment. Residual sugars in bagasse, if not removed or minimized prior to processing, can cause problems during board manufacture and subsequent use. Sugars are not chemically compatible with conventional resin binders used in bagasse board production and can interfere with bonding and result in poor strength. Unless the residual sugars are chemically modified or consumed during hot pressing, the sugars will begin to ferment when the bagasse board is exposed to humid conditions, thus emitting unpleasant odors and eventually becoming chemically and biological deterioration. This would substantially shorten the useful life of the bagasse pods in use.

従って、サトウキビのバガスから満足な製品を製造する
ことを期待する場合には、鋭端及び脱糖の作業が必要と
なる。これらの作業は製造費を増加させるだけでなく、
工程を複雑なものにする。
Therefore, sharpening and desugarization operations are necessary if one hopes to produce a satisfactory product from sugarcane bagasse. These operations not only increase manufacturing costs, but also
Make the process complicated.

上記慣用法とは著しく異なり、複合バガス製品、例えば
建築用ボード、家具用ボード、再構成用材及び成形品を
、樹脂結合剤の使用及び髄と残存糖の除去無しに製造で
きることが見出された。糖類、炭水化物類又はサツカリ
ド類はリグノセルロース臆 材料中に結合剤だけでなく増矛要素を与えて、良好な強
度性状とすばらしい寸法安定性をもった複合製品を生ず
る。
In marked contrast to the conventional methods described above, it has been found that composite bagasse products such as building boards, furniture boards, reconstitution materials and molded articles can be produced without the use of resin binders and without the removal of pith and residual sugars. . Sugars, carbohydrates or saccharides provide not only a binder but also a reinforcing element in the lignocellulosic material, resulting in a composite product with good strength properties and excellent dimensional stability.

本発明によれば、この方法は、高い比率の遊離糖、特に
非樹木性植物からのものを含有するバガス又は他のリグ
ノセルロース材料の微粉砕素材を実質上、必要とする。
According to the invention, the method essentially requires a finely ground mass of bagasse or other lignocellulosic material containing a high proportion of free sugars, especially from non-arboreal plants.

この微粉砕素材を先ず、低水分含有率、好ましくはオー
ブン乾燥重量に基づき一〜r%に乾燥する。この素材は
全部が他のリグノセルロース又は非リグノセルロース材
料でできていてもよく、又はこれらと部分的に組合わさ
ったものでもよい。この素材を、樹脂結合剤を加えるこ
となく、少くとも110℃の温度で、かつ上記材料を配
合して成形品にするのに十分な圧で、その場で結合を発
現させ、熱硬化させるのに十分な時間の間、成形して、
残存糖を、沸とう水及び酸加水分解に対して極めて抵抗
性のある不溶性かつ不溶融性の重合体物質に変える。
This finely ground material is first dried to a low moisture content, preferably 1 to r% based on oven dry weight. This material may be made entirely of, or partially combined with, other lignocellulosic or non-lignocellulosic materials. This material is bonded and thermally cured in situ without the addition of a resin binder at a temperature of at least 110°C and at a pressure sufficient to form a molded article with the above materials. Shape for a sufficient period of time to
The residual sugar is converted into an insoluble and infusible polymeric substance that is extremely resistant to boiling water and acid hydrolysis.

原料の微粉砕は特に有用である、何故ならば、個々の粒
子、フレーク又はストランドが形成及び成形作業を容易
にし改善するからである。更に又、微粉砕は同時に、植
物の茎からの表皮材料の存在を減少させ、最小量にする
からである。通常、上皮物質からなる表皮の薄い外層は
水及び接着を受−ケつけない。無結合剤系においては、
個々の粒子間に均一かつ密接な圧縮があり、強い結合、
緻密かつ滑らかな組織を生ずるという主たる理由により
、通常、粒子が細かい程、一層良好な製品が得られる。
Micronization of the raw material is particularly useful because the individual particles, flakes or strands facilitate and improve forming and shaping operations. Moreover, milling simultaneously reduces the presence of cuticle material from the plant stem to a minimum amount. Normally, the thin outer layer of the epidermis, consisting of epithelial material, is impervious to water and adhesion. In binder-free systems,
There is uniform and close compression between individual particles, strong bonding,
Finer particles usually yield better products, primarily because they produce a denser and smoother texture.

反対に、慣用法は一層細かい粒子を使用することは経済
的に不可能である。何故ならば、粒子が細かくなる程、
高価な合成樹脂結合剤の量を一層多くする必要があるか
らである。
On the contrary, conventional methods do not economically allow the use of finer particles. This is because the finer the particles,
This is because it is necessary to increase the amount of the expensive synthetic resin binder.

本発明においては、複合製品製造の際、他、の糖非含有
リグノセルロース材料と組合せる場合には極めて細かい
粒子を使用することが好ましい。実質上、この細かい粒
子は慣用製造法における粉末樹脂結合剤のようにはたら
く。
In the present invention, it is preferred to use very fine particles when combined with other sugar-free lignocellulosic materials to produce composite products. In effect, the fine particles act like powdered resin binders in conventional manufacturing methods.

サトウキビのバガス及びとりわけ非樹木性の植物の、他
の糖含有リグノセルロース材料の使用の有利な効果は、
熱成形中に溶融し、かつ上記リグノセルロース材料をそ
の場で重合し結合する糖及びその材料中に生成する水溶
性物質に帰することができよう。
The beneficial effects of the use of sugarcane bagasse and other sugar-containing lignocellulosic materials, especially of non-woody plants, are
This may be attributed to the sugars that melt during thermoforming and polymerize and bind the lignocellulosic material in situ and the water-soluble substances formed in the material.

更に、リグノセルロース組織の細胞壁中を透過した糖及
び水溶性物質も、変成し、熱硬化して架へ 橋硬質物質となり、成形品全体中くまなく増潰剤として
はたらくことになろう。
Furthermore, the sugars and water-soluble substances that have permeated through the cell walls of the lignocellulosic tissue will also be denatured and thermally hardened to become a cross-linked hard substance, which will serve as a filler throughout the entire molded article.

かくしてこの成形品は秀れた強度性状、寸法安定性及び
沸とう水及び酸加水分解に対する抵抗性を示す。これら
の結果は、リグノセルロース材料が高い比率の糖及び水
溶性物質を含有する場合に最高程度に得られる。
The molded articles thus exhibit excellent strength properties, dimensional stability and resistance to boiling water and acid hydrolysis. These results are best obtained when the lignocellulosic material contains a high proportion of sugars and water-soluble substances.

本発明における結合系中に含まれる化学反応は十分には
解明されていない。糖は酸及びアルカリの両者により減
成して小分子量の化合物となり、その際、糖分子から水
が失われることは周知である。130〜170℃の温度
で加圧下の弱酸又は純水でさえ、糖と反応する場合には
、約20%のヒドロキシメチル−フルフラールが生成す
る。他の中間体及びフルフラール誘導体も同様の条件下
に炭水化物から生成できよう。これらの誘導体は非常に
反応性であって、更に重合し変成して昇温下に不溶性か
ら不溶融性の架橋物質を生成するこ抗性がある。
The chemical reactions involved in the bonding system of the present invention are not fully understood. It is well known that sugars are degraded by both acids and alkalis to small molecular weight compounds, with water being lost from the sugar molecules. Approximately 20% of hydroxymethyl-furfural is produced when weak acids or even pure water under pressure at temperatures of 130-170° C. are reacted with sugars. Other intermediates and furfural derivatives could be produced from carbohydrates under similar conditions. These derivatives are highly reactive and resist further polymerization and modification to form insoluble to infusible crosslinked materials at elevated temperatures.

上述の反応のすべて又はいくつかが本発明の結合生成法
中に含まれ得るものと信ぜられる。更に、昇温下におけ
る糖及び水溶性物質の化学的変質は不可逆の化学的及び
物理的変化であり、かつ本発明にとって不可欠のもので
あると信ぜられる。本ジメチル−フルフラールからなる
炭水化物のフラン脱水生成物を含有しているものと推測
される。
It is believed that all or some of the reactions described above may be included in the bond production methods of the present invention. Furthermore, it is believed that the chemical alteration of sugars and water-soluble substances at elevated temperatures is an irreversible chemical and physical change and is essential to the present invention. It is presumed that this product contains a furan dehydration product of a carbohydrate consisting of dimethyl-furfural.

本発明により製造したサトウキビのバガスの物理的及び
機械的性状は高価々合成樹脂結合剤のこれまでの使用に
より製造した常とうのバガスポードの性状に少くとも比
肩できるか又はそれより良好なものであることが見出さ
れた。
The physical and mechanical properties of the sugarcane bagasse produced according to the invention are at least comparable to or better than those of conventional bagasse pods produced by the conventional use of expensive synthetic resin binders. It was discovered that

本発明の実施態様を下記の実施例において詳細に記述し
例示することにする。
Embodiments of the invention will be described and illustrated in detail in the Examples below.

実施例1 3.1%の水分含有率をもつ乾燥サトウキビバガスを常
とうの精微粉砕工場から得だ。このものは7.2重量%
の水溶性物質を含有しており、この物質から、4(,7
%の還元糖(グルコースとして)が見出された。更に行
なった実験によりバガスは約70重量%の真の繊維と3
0重量%の髄を含有していることがわかった。
Example 1 Dried sugarcane bagasse with a moisture content of 3.1% was obtained from a conventional fine grinding mill. This stuff is 7.2% by weight
It contains 4 (,7) water-soluble substances.
% reducing sugars (as glucose) were found. Further experiments have shown that bagasse contains approximately 70% by weight of true fibers and 3.
It was found to contain 0% by weight of pith.

バガスをハンマーミルで粉砕すると2つの画分の粒子を
生じた。/乙メツシュのタイラー篩を通過した粒子を面
層用に使用し、/6メツシユより大きい粒子を3一層マ
ット用の心材として使用した。オーブン乾燥重量による
面心比は/:lであった。このマットから、!OOx!
;OO×/ハ/闘のボードをis分間、熱間圧縮して2
35℃の温度及び2.ざMPaの圧における比重が0.
72のものにしだ。この熱間圧縮の間に、水分以外の成
る量の物質が水蒸気及び種々の煙霧として蒸発するのが
認められた。マットの重量損失は、r、<z%に達し、
元のマットの水分含有率30g%より遥かに多かった。
Grinding the bagasse in a hammer mill produced two fractions of particles. The particles that passed through the /Otsu mesh Tyler sieve were used for the surface layer, and the particles larger than /6 mesh were used as the core material for the 3-layer mat. The face center ratio by oven dry weight was /:l. From this mat! OOx!
;OO × / Ha / Hot compress the fighting board for is minutes 2
a temperature of 35°C and 2. Specific gravity at a pressure of 0.0 MPa.
It's 72 things. During this hot compression, amounts of substances other than water were observed to evaporate as water vapor and various fumes. The weight loss of the mat reaches r,<z%;
The water content was much higher than the 30g% of the original mat.

この余分の重量損失は昇温下に過酷な化学反応があった
ことを示している。最終の分析によシ、僅かに0.7%
の還元糖が仕上ボード中に残存していることが確認され
た。この量は商用バガスボード中の量より遥かに少かっ
た。
This extra weight loss indicates that there was a severe chemical reaction at elevated temperatures. According to final analysis, only 0.7%
It was confirmed that reducing sugars remained in the finished board. This amount was much lower than the amount in commercial bagasse boards.

曲げ強さ試験によれば乾燥MOR(破壊係数)は/lJ
MPa、乾燥MOE (弾性率)は3.I GPaであ
った。湿潤MORはざ、A MPaであった。湿潤曲げ
強さは標本を沸とう水中に2時間浸漬し、ついでこれを
湿潤かつ冷たい状態で試験することにより得られた。
According to the bending strength test, the dry MOR (modulus of rupture) is /lJ
MPa, dry MOE (modulus of elasticity) is 3. It was IGPa. The wet MOR was A MPa. Wet flexural strength was obtained by immersing the specimens in boiling water for 2 hours and then testing them wet and cold.

実施例2 内部の糖含有軟質髄をサトウキビの茎の外部硬質層又は
皮から分離するサトウキビ分離機を用いてサトウキビの
皮を作った。皮バガスは、糖がこれから抽出されなかっ
たので、2g。6%の水溶性物質と7763%の還元糖
を含有していた。
Example 2 Sugarcane hulls were made using a sugarcane separator that separates the internal sugar-containing soft pulp from the external hard layer or skin of the sugarcane stalk. 2g of peeled bagasse since no sugar was extracted from it. It contained 6% water-soluble substances and 7763% reducing sugars.

この皮バガスを細断して幅、厚み共に、八!ないし3,
2解の、約5%の水分を含有するストランドをつくった
。ストランドは長さが/、tないし3QQmtnの範囲
にあり、一方向に配向し、成形して3ざx s o x
 rtso闘の寸法とO,tSの比重をもつ複合用材に
した。成形温度は30分間、3.lIMPaの圧で22
!;℃であった。曲げ強さ試験によれば、乾燥MORは
31.AMPa、湿潤MORはlざ、6MPaであった
This peeled bagasse is shredded to a width and thickness of 8! or 3,
A strand containing approximately 5% moisture was produced. The strands have lengths ranging from /, t to 3QQmtn, are unidirectionally oriented, and shaped to form
It was made into a composite material with dimensions of RTSO and specific gravity of O, tS. Molding temperature: 30 minutes; 3. 22 at a pressure of lIMPa
! ;℃. According to the bending strength test, the dry MOR is 31. AMPa and wet MOR were 6 MPa.

実施例3 サトウキビ分離機を用いて作った、新鮮なサトウキビの
皮を、異なった時間の間、水中で煮沸する処理に付して
糖を除去した。皮の三つのバッチをそれぞれ!、IO及
び30分間煮沸し、第グのバッチは煮沸せずに、対照と
しての実験中に含ませた。煮沸後、皮を乾燥してg%の
水分含有率のものとし、ついでハンマーミルで粉砕して
±20メツシュのタイラー篩の両分にしだ。化学分析に
よると、残存糖は煮沸時間の増加に反比例していた。こ
のことは又、水溶性物質と還元糖の間のほぼ直線の関係
を示している。下記第1表は上記煮沸処理の結果を示す
ものである。
Example 3 Fresh sugarcane husks made using a sugarcane separator were subjected to a treatment of boiling in water for different times to remove sugar. Three batches of peel each! , IO and boiled for 30 minutes; a second batch was not boiled and was included in the experiment as a control. After boiling, the skin was dried to a moisture content of g%, then ground in a hammer mill and passed through a ±20 mesh Tyler sieve. Chemical analysis showed that residual sugar was inversely proportional to increasing boiling time. This also indicates a nearly linear relationship between water-soluble substances and reducing sugars. Table 1 below shows the results of the boiling treatment.

第1表 水中で煮沸処理した皮の1個のX 皮繊維のオ
ーブン乾燥重量としての含有率皮組成物の各バッチを用
いて、三つの異なったプレス温度(/ざ0,210及び
コlIO℃)、二つの異なったプレス時間(IO及び2
0分)及び圧締圧3.tIMPaを用い、3; 00 
x !; 00 X //、/fnmで比重が約0.7
0の6枚のボードを作った。面層組成物(−20メツシ
ユ)の水分含有率は約9.0%であり、心組成物(+、
!Oメツシュ)のそれは3.0%であった。マットのオ
ーブン乾燥重量による面心比は/:/であった。tざ枚
のボードについての試験結果を下記の第2表中に表示し
である。
Table 1 Content of one piece of skin treated by boiling in water as oven-dry weight ), two different press times (IO and 2
0 minutes) and clamping pressure 3. using tIMPa, 3;00
x! ; Specific gravity is approximately 0.7 at 00 X //, /fnm
I made 6 boards of 0. The water content of the face layer composition (-20 mesh) is about 9.0%, and the water content of the core composition (+,
! O mesh) was 3.0%. The face center ratio of the mat based on oven dry weight was /:/. The test results for t boards are shown in Table 2 below.

第2表に示した試験結果から明らかなように、ボードの
性状は皮の糖含有率が増加するにつれて改善されている
。又、プレス温度が一層高く、プレス時間が一層長くな
る程、ボードの品質がよくなった。皮組成物ボードは、
主として、極めて細かい粒子のため、緻密で滑らかな表
面と暗褐色を持ち、かつマットの面相中に高い糖及び水
分の含有率を持っていた。皮バガスポード、殊に、一層
高い糖含有率と苛酷なプレスを用いて作ったボードの寸
法安定性は慣用法の製品とくらべて優秀で薙 あった。このことは重合糖の結合及び増l効果によるも
のである。
As is clear from the test results shown in Table 2, the properties of the board improve as the sugar content of the skin increases. Also, the higher the pressing temperature and the longer the pressing time, the better the quality of the board. skin composition board
Mainly due to extremely fine particles, it had a dense and smooth surface and dark brown color, and had a high sugar and water content in the matte phase. The dimensional stability of the skin bagasse pods, especially the boards made with higher sugar content and harsher pressing, was superior to that of conventional products. This is due to the binding and liter-enhancing effect of polymerized sugar.

実施例4 この実施例は他のリグノセルロース材料と組合わせたサ
トウキビバガスからの混合複合製品の製造を示すもので
ある。
Example 4 This example demonstrates the production of a mixed composite product from sugarcane bagasse in combination with other lignocellulosic materials.

約79%の還元糖含有サトウキビ皮バガスをノ・ンマー
ミルで粉砕したところ1.20メツシユのタイラー篩を
通過した。この皮バガス砕片を同様な寸法のポプラ樹砕
片と70:30の重量比で混合した。この混合物からマ
ットをつくり、これを、235℃、2.1 MPaの圧
で70分間、熱間圧縮して、比重が0.72の!;00
x300×//、/mmのボードを作った。静曲げ試験
によれば、乾燥MORは/、!’、jMP&、湿潤MO
Rはざ、/ MPaであった。初期結合試験は390 
kPaの張力垂直強さを与えた。
When sugarcane peel bagasse containing about 79% reducing sugar was ground in a no-mer mill, it passed through a 1.20 mesh Tyler sieve. The peeled bagasse pieces were mixed with poplar tree pieces of similar size in a weight ratio of 70:30. A mat was made from this mixture and hot-pressed at 235°C and a pressure of 2.1 MPa for 70 minutes to give a specific gravity of 0.72! ;00
I made a board of x300×///mm. According to the static bending test, the dry MOR is /,! ',jMP&,wet MO
R was /MPa. Initial binding test is 390
A tensile vertical strength of kPa was given.

実施例5 この実施例は他の糖含有リグノセルロース材料を用いて
同様な結果が得られることを示すものである。
Example 5 This example shows that similar results can be obtained using other sugar-containing lignocellulosic materials.

約/ざ%の還元糖を含有するサトウモロコシの茎を乾燥
して3%の水分含有率のものとし、ハンマーミルで粉砕
したところ、20メツシユのタイラー篩を通過した。実
施例4に概略を示したのと同様なプレス条件下にこの組
成物を用いてボード(!; 00x!;00×//、/
rnmで比重0.7!; )を作った。試験結果によれ
ば、乾燥MORは/1.5MPa。
Sorghum stalks containing about 1/2% reducing sugars were dried to a moisture content of 3% and ground in a hammer mill to pass through a 20 mesh Tyler sieve. This composition was used to prepare boards (!; 00x!; 00x //, /
RNM specific gravity 0.7! ; )made. According to the test results, the dry MOR is /1.5 MPa.

湿潤MORil、9.、! MPa 、初期結合強さは
+ lrOkPaであった。
Wet MORil, 9. ,! MPa, the initial bond strength was +lrOkPa.

約/2%の可溶性物質又は約7%の還元糖を含有するト
ウモロコシの茎を乾燥して3%の水分含有率のものとし
、ハンマーミルで粉砕したところ、20メツシユのタイ
ラー篩を通過した。実施例4に概略を示しだのと同様な
プレス条件下に、この組成物を用いてボード(!; O
Ox !; 00 x //、/amで比重O,Ir2
)を作った。試験結果によれば、乾燥MORは/11.
3MPa、、湿潤MORは7.IIMPa 。
Corn stalks containing about 1/2% soluble material or about 7% reducing sugars were dried to a moisture content of 3% and ground in a hammer mill to pass through a 20 mesh Tyler sieve. This composition was used to form board (!; O
Ox! ; Specific gravity O, Ir2 at 00 x //, /am
)made. According to the test results, the dry MOR is /11.
3MPa, wet MOR is 7. IIMPa.

初期結合強さは320 kPaであった。The initial bond strength was 320 kPa.

特許出願人 大 1)昭 二Patent applicant: Dai 1) Shoji

Claims (10)

【特許請求の範囲】[Claims] (1) 糖含有リグノセルロース材料からなる原料を、
粒子、繊維、ストランド及びフレークに分離し、微粉砕
原料を乾燥し、予め乾燥した原料を所望のマットに形成
し、かつこの形成マットを、110℃以上の温度で、こ
のマットを成形品に圧縮するのに十分な圧と時間をかけ
て、プレスし加熱し、その間、接着結合が発現してその
場で熱硬化し、糖及び水溶性ある結合及び増麓剤として
の、不溶性かつ不溶融性の架橋物質に変性し重合する、
工程からなる、微粉砕の糖含有リグノセルロース材料か
ら接着結合剤を添加することなく、複合製品を製造する
方法。
(1) Raw material consisting of sugar-containing lignocellulose material,
Separating into particles, fibers, strands and flakes, drying the finely pulverized raw material, forming the pre-dried raw material into a desired mat, and compressing the formed mat into a molded article at a temperature of 110° C. or higher. Press and heat under sufficient pressure and time to make the adhesive bond develop and heat cure in situ, forming an insoluble and infusible bond with sugar and water soluble as a binding and thickening agent. Modifies and polymerizes into a crosslinked substance,
A method for producing composite products from finely divided sugar-containing lignocellulosic materials without the addition of adhesive binders, comprising the steps of:
(2) 上記糖含有リグノセルロース材料がサトウキビ
のバガス、モロコシの茎、トウモロコシの茎、ヒマワリ
の茎、アマの茎、及び糖と水溶性物質を含有する、他の
非樹木性植物である、特許請求の範囲第(1)項の方法
(2) A patent in which the sugar-containing lignocellulosic material is sugarcane bagasse, sorghum stalks, corn stalks, sunflower stalks, flax stalks, and other non-woody plants containing sugars and water-soluble substances. The method according to claim (1).
(3)上記の糖が、水溶性であり、抽出が容易であり、
かつ変成が容易である遊離糖、炭水化物又はサツカリド
であり、熱を加えて熱硬化^ して結合及び増量が可能な不溶性かつ不溶融性の物質と
なるものである、特許請求の範囲第(1)項の方法。
(3) the above sugar is water-soluble and easy to extract;
and is a free sugar, carbohydrate, or saccharide that is easily denatured and can be thermally cured by applying heat to become an insoluble and infusible substance that can be combined and increased in volume. ) method.
(4) h記のリグノセルロース材料内に生ずる上記の
糖及び水溶性物質が110℃以上の昇温敵性の、架橋重
合体物質となる、特許請求の範囲第(1)項の方法。
(4) The method of claim (1), wherein the sugars and water-soluble substances formed in the lignocellulosic material of item (h) are crosslinked polymeric substances that are resistant to temperature elevations of 110° C. or higher.
(5)上記の熱成形及びプレス温度が2.20℃以上で
ある、特許請求の範囲第(1)項の方法。
(5) The method according to claim (1), wherein the thermoforming and pressing temperature is 2.20°C or higher.
(6) 仕上複合製品中に残存する、上記の糖及び水溶
性物質が、izo℃以上の昇温下の成形作業の間の化学
的変性及び重量損失により著しく減少する、特許請求の
範囲第(1)項の方法。
(6) The above-mentioned sugars and water-soluble substances remaining in the finished composite product are significantly reduced by chemical modification and weight loss during the molding operation at elevated temperatures above Izo°C. 1) Method.
(7) 上記糖含有リグノセルロース材料を微粉砕し、
他のリグノセルロース又は非リグノセルロース材料と一
緒にして、複合製品を特徴する特許請求の範囲第(1)
項の方法。
(7) Finely pulverizing the sugar-containing lignocellulose material,
Claim (1) characterized by a composite product, together with other lignocellulosic or non-lignocellulosic materials.
Section method.
(8) 上記の糖、水溶性物質及び髄が製造前に部分的
に除去され又は除去されない、特許請求の範囲第(1)
項の方法。
(8) Claim No. 1, wherein the sugar, water-soluble substance and pith are partially removed or not removed before manufacturing.
Section method.
(9) 上記糖含有リグノセルロース材料を微粉砕して
、強い結合力、すぐれた寸法安定性及び緻密、均一で滑
らかな、細かい組織をもつ複合製品の製造用の極めて細
かい粒子又は繊維にする、特許請求の範囲第(1)項の
方法。
(9) pulverizing the sugar-containing lignocellulosic material into extremely fine particles or fibers for the production of composite products with strong binding strength, good dimensional stability and dense, uniform, smooth, fine texture; The method according to claim (1).
(10)上記複合製品が建築用ボード、家具用ボード、
再構成用材、圧縮耐火丸太及び沸とう水及び酸加水分解
に抵抗性のある、防水結合をもつ成形品である、特許請
求の範囲第(1)項の方法。
(10) The above composite product is a building board, a furniture board,
The method of claim 1, wherein the reconstitution lumber is a compressed refractory log and a molded article with a waterproof bond that is resistant to boiling water and acid hydrolysis.
JP58124224A 1983-07-07 1983-07-07 Manufacture of composite product from lignocellulose material Pending JPS6030309A (en)

Priority Applications (14)

Application Number Priority Date Filing Date Title
JP58124224A JPS6030309A (en) 1983-07-07 1983-07-07 Manufacture of composite product from lignocellulose material
NL8302960A NL8302960A (en) 1983-07-07 1983-08-24 METHOD FOR MANUFACTURING COMPOSITE PRODUCTS FROM LIGNOCELLULOSE MATERIAL
GB08323003A GB2142943B (en) 1983-07-07 1983-08-26 Process for manufacturing composite products from lignocellulosic materials
DE19833333032 DE3333032A1 (en) 1983-07-07 1983-09-13 METHOD FOR PRODUCING COMPOSITE PRODUCTS FROM LIGNOCELLULOSE MATERIALS
IN1142/CAL/83A IN161051B (en) 1983-07-07 1983-09-19
FR8316190A FR2549768A1 (en) 1983-07-07 1983-10-12 METHOD FOR MANUFACTURING COMPOSITE PRODUCTS FROM LIGNOCELLULOSIC MATERIALS AND PRODUCTS THUS OBTAINED
KR1019830004872A KR920000756B1 (en) 1983-07-07 1983-10-14 Process to produce complex compound from ligno cellulose materials
SU833656698A SU1212318A3 (en) 1983-07-07 1983-10-28 Method of producing composite articles from lignocellulose materials containing sugar
MX199301A MX172616B (en) 1983-07-07 1983-11-04 PROCEDURE FOR MANUFACTURING COMPOSITE PRODUCTS FROM LIGNOCELLULOSIC MATERIALS
IT23636/83A IT1169684B (en) 1983-07-07 1983-11-08 PROCEDURE FOR THE PRODUCTION OF PRODUCTS COMPOSED OF LIGNOCELLULOSIC MATERIALS
ZA838301A ZA838301B (en) 1983-07-07 1983-11-08 Process for manufacturing composite products from lignocellulosic materials
BR8306450A BR8306450A (en) 1983-07-07 1983-11-23 PROCESS FOR THE MANUFACTURE OF COMPOUND PRODUCTS FROM LIGNO-CELLULOSIC MATERIALS
DK554583A DK554583A (en) 1983-07-07 1983-12-01 PROCEDURE FOR MANUFACTURING COMPOSITION MATERIALS
PH29979A PH19188A (en) 1983-07-07 1983-12-14 Process for manufacturing composite products from lignocellulosic materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58124224A JPS6030309A (en) 1983-07-07 1983-07-07 Manufacture of composite product from lignocellulose material

Publications (1)

Publication Number Publication Date
JPS6030309A true JPS6030309A (en) 1985-02-15

Family

ID=14880059

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58124224A Pending JPS6030309A (en) 1983-07-07 1983-07-07 Manufacture of composite product from lignocellulose material

Country Status (14)

Country Link
JP (1) JPS6030309A (en)
KR (1) KR920000756B1 (en)
BR (1) BR8306450A (en)
DE (1) DE3333032A1 (en)
DK (1) DK554583A (en)
FR (1) FR2549768A1 (en)
GB (1) GB2142943B (en)
IN (1) IN161051B (en)
IT (1) IT1169684B (en)
MX (1) MX172616B (en)
NL (1) NL8302960A (en)
PH (1) PH19188A (en)
SU (1) SU1212318A3 (en)
ZA (1) ZA838301B (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11318669A (en) * 1997-12-16 1999-11-24 Changrong Wang Manufacturing of packaging material and sheet from stem of plant
CN101733808A (en) * 2008-11-07 2010-06-16 北京环能海臣科技有限公司 Straw section with waterproof skin compounded on surface
WO2013099364A1 (en) * 2011-12-28 2013-07-04 もったいないバイオマス株式会社 Cholesterol excretion promoter and neutral fat excretion promoter each utilizing inner stem fiber of sunflower
WO2013190777A1 (en) * 2012-06-19 2013-12-27 パナソニック株式会社 Bagasse molding
WO2018155292A1 (en) * 2017-02-24 2018-08-30 パナソニックIpマネジメント株式会社 Adhesive for thermocompression molding, wooden board and method for producing same

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FR2723328B1 (en) 1994-08-03 1996-10-31 Lacroix Soc E COMPOSITION FOR AGGLOMERATED PRODUCT COMPRISING A VEGETABLE FILLER AND SUGAR, AGGLOMERATED PRODUCT AND ITS PREPARATION METHOD
RU2458148C2 (en) * 2010-09-21 2012-08-10 Российская академия сельскохозяйственных наук Государственное научное учреждение Всероссийский научно-исследовательский институт электрификации селького хозяйства Российской академии сельскохозяйственных наук (ГНУ ВИЭСХ Россельхозакадемии) Method for production of cow parsnip white sugar
ES2390853B2 (en) * 2012-07-30 2013-03-19 Universidad Miguel Hernández De Elche Manufacturing process of particle board of lignocellulosic material
CN110405900B (en) * 2018-04-27 2022-04-12 中国科学院大连化学物理研究所 Method for preparing environment-friendly biological board by taking furfural residue of lignocellulose as raw material
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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11318669A (en) * 1997-12-16 1999-11-24 Changrong Wang Manufacturing of packaging material and sheet from stem of plant
CN101733808A (en) * 2008-11-07 2010-06-16 北京环能海臣科技有限公司 Straw section with waterproof skin compounded on surface
WO2013099364A1 (en) * 2011-12-28 2013-07-04 もったいないバイオマス株式会社 Cholesterol excretion promoter and neutral fat excretion promoter each utilizing inner stem fiber of sunflower
JPWO2013099364A1 (en) * 2011-12-28 2015-04-30 もったいないバイオマス株式会社 Cholesterol excretion enhancer and neutral fat excretion enhancer using sunflower inner stem fiber
WO2013190777A1 (en) * 2012-06-19 2013-12-27 パナソニック株式会社 Bagasse molding
CN104203515A (en) * 2012-06-19 2014-12-10 松下电器产业株式会社 Bagasse molding body
JPWO2013190777A1 (en) * 2012-06-19 2016-02-08 パナソニックIpマネジメント株式会社 Bagasse molded body
WO2018155292A1 (en) * 2017-02-24 2018-08-30 パナソニックIpマネジメント株式会社 Adhesive for thermocompression molding, wooden board and method for producing same
JPWO2018155292A1 (en) * 2017-02-24 2020-01-09 パナソニックIpマネジメント株式会社 Adhesive for hot press molding, wood board, and method for producing them
US11572491B2 (en) 2017-02-24 2023-02-07 Panasonic Intellectual Property Management Co., Ltd. Adhesive for heat press molding, wooden board, and manufacturing methods thereof

Also Published As

Publication number Publication date
IN161051B (en) 1987-09-26
ZA838301B (en) 1984-07-25
NL8302960A (en) 1985-02-01
IT8323636A0 (en) 1983-11-08
PH19188A (en) 1986-01-23
KR920000756B1 (en) 1992-01-21
FR2549768A1 (en) 1985-02-01
GB8323003D0 (en) 1983-09-28
KR850001345A (en) 1985-03-18
MX172616B (en) 1994-01-03
SU1212318A3 (en) 1986-02-15
GB2142943B (en) 1987-03-25
DK554583A (en) 1985-01-08
GB2142943A (en) 1985-01-30
BR8306450A (en) 1985-03-12
DE3333032A1 (en) 1985-01-24
IT1169684B (en) 1987-06-03
DK554583D0 (en) 1983-12-01

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