JPH07102074A - Method for converting cellulose material into minute particle - Google Patents

Method for converting cellulose material into minute particle

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Publication number
JPH07102074A
JPH07102074A JP24496893A JP24496893A JPH07102074A JP H07102074 A JPH07102074 A JP H07102074A JP 24496893 A JP24496893 A JP 24496893A JP 24496893 A JP24496893 A JP 24496893A JP H07102074 A JPH07102074 A JP H07102074A
Authority
JP
Japan
Prior art keywords
cellulose material
cellulose
particle size
dispersion
pressure
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.)
Withdrawn
Application number
JP24496893A
Other languages
Japanese (ja)
Inventor
Yoshinobu Minami
義信 南
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.)
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Asahi Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP24496893A priority Critical patent/JPH07102074A/en
Publication of JPH07102074A publication Critical patent/JPH07102074A/en
Withdrawn legal-status Critical Current

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Abstract

PURPOSE:To efficiently convert a cellulose material into minute particles. CONSTITUTION:A cellulose material is converted into an aq. dispersion having a solid content of 1-20wt.% at a predispersion step and then subjected to a face-to-face collision in a minute orifice under a pressure of 600kg/cm<2> or higher.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、セルロース系素材の微
細化方法に関する。即ち本発明は、食品、医薬品、化粧
品、塗料、セラミックス、樹脂、触媒、その他工業用品
等広い分野において、懸濁安定剤、乳化安定剤、増粘安
定剤、等の安定剤、組織付与剤、クラウディー剤、研磨
剤、食物繊維、油脂代替物等として利用可能なセルロー
ス系素材の微細化方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for making cellulosic material fine. That is, the present invention, foods, pharmaceuticals, cosmetics, paints, ceramics, resins, catalysts, in a wide range of other industrial products, suspension stabilizers, emulsion stabilizers, thickening stabilizers, etc. stabilizers, texture imparting agents, The present invention relates to a method for refining a cellulosic material that can be used as a cloudy agent, an abrasive, dietary fiber, an oil and fat substitute, and the like.

【0002】[0002]

【従来の技術】従来よりセルロースの微細化については
種々の方法が試みられている。例えば、特公昭62−3
0220号公報には微結晶セルロース懸濁液を高圧用均
質化装置によって均質化する方法の開示があるが、充分
に微細化するためには何回も繰り返し処理を行う必要が
あり実用的な方法とは言えない。また、特開平3−16
3135号公報には、積算体積50%の粒径が0.3〜
6μmの微粒化セルロース及びセルロース系素材を媒体
ミルによって微粒子化する方法の開示がある。
2. Description of the Related Art Conventionally, various methods have been tried for making cellulose fine. For example, Japanese Examined Japanese Patent Publication Sho 62-3
Japanese Unexamined Patent Publication No. 0220 discloses a method of homogenizing a microcrystalline cellulose suspension with a homogenizer for high pressure, but it is necessary to repeat the treatment many times in order to sufficiently miniaturize the suspension, which is a practical method. It can not be said. In addition, JP-A-3-16
No. 3135 discloses that the particle size with an integrated volume of 50% is 0.3-
There is a disclosure of a method of atomizing 6 μm micronized cellulose and a cellulosic material by a media mill.

【0003】しかしながら、この方法では、6mm以
下、通常は3mm以下の金属製、セラミック製等の小粒
径のビーズを強制撹拌させることによってセルロース系
素材の微粒化が行われるが、セルロース濃度を高めた
り、微粒化の進行に伴う粘度の上昇によってビーズの運
動が制限され生産性が低下するという問題がある。ま
た、媒体同士及び媒体と撹拌翼等との衝突により経時的
に摩耗が起こるという問題がある。また、得られた微粒
化セルロースは、個々の粒子の長径と短径の比即ちアス
ペクト比が大きく、このため、滑らかさに欠ける。
However, according to this method, the cellulosic material is atomized by forcibly stirring beads having a small particle diameter of 6 mm or less, usually 3 mm or less, such as metal or ceramic, and the cellulose concentration is increased. Alternatively, there is a problem that the movement of the beads is restricted due to an increase in viscosity with the progress of atomization, and the productivity is reduced. Further, there is a problem that abrasion occurs over time due to collision between the media and between the media and the stirring blades. Further, the obtained micronized cellulose has a large ratio of major axis to minor axis of individual particles, that is, an aspect ratio, and therefore lacks smoothness.

【0004】[0004]

【発明が解決しようとする課題】本発明は、これらの従
来技術の問題を解決し食品、医薬品、化粧品、工業用品
等の広い分野にわたり利用可能な高度の懸濁・分散・乳
化等の安定剤、高度の保形性付与剤、組織付与剤、クラ
ウディー剤、油脂代替物等に用いることが出来る微細化
セルロース系素材を、実用的に効率よく製造する方法を
提供する事を目的としている。
DISCLOSURE OF THE INVENTION The present invention solves these problems of the prior art and is a high-level stabilizer for suspension, dispersion, emulsification, etc., which can be used in a wide range of fields such as foods, pharmaceuticals, cosmetics, and industrial products. , A highly shape-retaining agent, a texture imparting agent, a cloudy agent, a fat-and-oil substitute, and the like.

【0005】[0005]

【課題を解決するための手段】本発明者は、これらの従
来技術の問題点を解決するために鋭意研究を重ねた結果
本発明に到達した。即ち、本発明は、セルロース系素材
を、予備分散工程で固形分1〜20重量%の水系分散液
とし、次いで微細オリフィス内において圧力600Kg
/cm2 以上の条件で対面衝突させることを特徴とする
セルロース系素材の微細化方法に関するものである。
The inventor of the present invention has arrived at the present invention as a result of extensive research to solve these problems of the prior art. That is, according to the present invention, a cellulosic material is made into an aqueous dispersion having a solid content of 1 to 20% by weight in a preliminary dispersion step, and then a pressure of 600 kg is applied in a fine orifice.
The present invention relates to a method for micronizing a cellulosic material, which is characterized by causing face-to-face collision under a condition of not less than / cm 2 .

【0006】微細化に供されるセルロース系素材として
は、木材パルプ、精製リンター等のセルロース系素材を
酸加水分解、アルカリ酸化分解、酵素分解、スチームエ
クスプロージョン分解等により解重合処理した後精製し
た平均重合度30〜375の水湿セルロース及びこれを
乾燥したセルロースを用いることが出来る。また、この
セルロースと水溶性のガム類及び又は澱粉分解物類等と
の複合体を用いることが出来る。更にパルプ等を鉱酸等
により軽度に加水分解した後、粉砕したセルロースを用
いることが出来る。
As a cellulosic material to be subjected to micronization, cellulosic materials such as wood pulp and refined linter are depolymerized by acid hydrolysis, alkaline oxidative decomposition, enzymatic decomposition, steam explosion decomposition, etc., and then refined. Wet cellulose having an average degree of polymerization of 30 to 375 and cellulose obtained by drying this can be used. Further, a complex of this cellulose with water-soluble gums and / or starch decomposition products can be used. Further, pulp or the like is lightly hydrolyzed with a mineral acid or the like, and then crushed cellulose can be used.

【0007】市販されているセルロース系素材として
は、セルロースパウダー、結晶セルロース、結晶セルロ
ースと水溶性ガム類等との複合体等がある。セルロース
系素材を微細化するに当たっては、予備分散により均質
に分散ないし出来るだけ磨砕することが必要であり、平
均粒径で25μm以下、微細オリフィス内での閉塞を防
止し、次工程でより微細化するためには15μm以下と
することが好ましい。
Examples of commercially available cellulosic materials include cellulose powder, crystalline cellulose, and a complex of crystalline cellulose and water-soluble gums. To make the cellulosic material finer, it is necessary to disperse it homogeneously or to grind it as much as possible by preliminary dispersion. It has an average particle size of 25 μm or less, prevents clogging in the fine orifice, and is finer in the next step. In order to achieve this, the thickness is preferably 15 μm or less.

【0008】予備分散機としては各種の分散、乳化、磨
砕機等を用いることが出来る。例えば、プロペラ型分散
機、高速ミキサー、ホモミキサー、カッター等の各種ミ
キサー、ボールミル、コロイドミル等のミル類、高圧ホ
モジナイザーに代表される分散、乳化機、ニーダー、プ
ラネタリーミキサー、エクストルーダー等に代表される
混練、磨砕機等が使用出来る。
Various dispersing, emulsifying and grinding machines can be used as the preliminary dispersing machine. For example, propeller type dispersers, high speed mixers, homomixers, various mixers such as cutters, ball mills, mills such as colloid mills, dispersions represented by high pressure homogenizers, emulsifiers, kneaders, planetary mixers, extruders, etc. The kneading and grinding machines used can be used.

【0009】予備分散工程に続く微細オリフィス内で微
細化する装置としては、例えば超高圧ホモジナイザーを
用いるのが好ましい。超高圧ホモジナイザーとは加速さ
れた高流速によるせん断力、急激な圧力降下(キャビテ
ーション)および高流速の粒子同士が微細オリフィス内
で対面衝突することによる衝撃力によって磨砕を行う装
置である。微細化する場合の圧力は約600Kg/cm
2 以上が必要であり、これ未満の圧力では微細化が不十
分となり実用的ではない。市販されている装置として
は、ナノマイザー(ナノマイザー株式会社製)、マイク
ロフルイダイザー(Microfluidics社製)
等を用いることが出来る。
As a device for refining in the fine orifice following the preliminary dispersion step, for example, an ultrahigh pressure homogenizer is preferably used. The ultra-high pressure homogenizer is a device that grinds by shearing force due to accelerated high flow velocity, rapid pressure drop (cavitation), and impact force caused by face-to-face collision of particles with high flow velocity in a fine orifice. The pressure for miniaturization is about 600 Kg / cm
A pressure of 2 or more is required, and a pressure of less than this is not practical because the miniaturization is insufficient. The commercially available devices are Nanomizer (manufactured by Nanomizer Co., Ltd.) and Microfluidizer (manufactured by Microfluidics).
Etc. can be used.

【0010】これらの予備分散及び微細化装置による分
散においては、熱水を用いることが効果的である。微細
化におけるセルロース系素材の水系分散液の濃度は、固
形分で1〜20重量%である。1重量%未満では実用的
とは言えず、20重量%を越えると、微細化装置の運転
における安定運転性、微細化効率が低下する。
It is effective to use hot water for the preliminary dispersion and the dispersion by the finer. The concentration of the aqueous dispersion of the cellulosic material in micronization is 1 to 20% by weight in terms of solid content. If it is less than 1% by weight, it cannot be said to be practical, and if it exceeds 20% by weight, stable operability and miniaturization efficiency in the operation of the miniaturization apparatus are deteriorated.

【0011】本発明の微細化方法は、不純物の混入がな
く、セルロース系素材を実用的に効率よく微細化出来る
方法であり、得られる微細セルロース系素材は1μm以
下の粒子の割合が高く、丸みを帯びたアスペクト比の小
さい粒子形状のものが得られ、滑らかな組織を有し粘度
の高いものが得られるという特徴がある。このため、食
品、医薬品、化粧品、塗料、セラミックス、樹脂、触
媒、その他工業用品等広い分野において、懸濁安定剤、
乳化安定剤、増粘安定剤、等の安定剤、組織付与剤、ク
ラウディー剤、研磨剤、食物繊維、油脂代替物等として
の利用が可能である。なお、粒度の測定は、HORIB
Aレーザー回折式粒度分布測定装置(LA−500型、
株式会社堀場製作所製)を用い、平均粒径は積算体積5
0%の粒径である。。
The micronization method of the present invention is a method for practically and efficiently micronizing a cellulosic material without inclusion of impurities. The resulting microcellular material has a high proportion of particles of 1 μm or less and has a roundness. It is characterized in that particles having a small aspect ratio and having a smooth structure and a high viscosity can be obtained. Therefore, suspension stabilizers in a wide range of fields such as foods, pharmaceuticals, cosmetics, paints, ceramics, resins, catalysts and other industrial products.
It can be used as a stabilizer such as an emulsion stabilizer and a thickening stabilizer, a texture imparting agent, a cloudy agent, an abrasive, a dietary fiber, a fat and oil substitute, and the like. In addition, the measurement of particle size
A laser diffraction particle size distribution analyzer (LA-500 type,
HORIBA, Ltd.) and the average particle size is 5
The particle size is 0%. .

【0012】[0012]

【実施例】次に、実施例によって本発明をさらに詳細に
説明する。
EXAMPLES Next, the present invention will be described in more detail by way of examples.

【0013】[0013]

【実施例1】市販DPパルプを細断後、10%塩酸中で
105℃20分間加水分解して得られた酸不溶性残渣を
ろ過、洗浄、精製した後、噴霧乾燥により水分4.7%
の結晶セルロースを得た。この結晶セルロースの固形分
を10重量%とし、エースホモジナイザー(日本精機
製)で25℃において15000rpm、10分間の予
備分散を行った。予備分散液の平均粒径は14.3μm
であった。続いて、この予備分散液を高圧破砕装置(M
icrofluidics社製マイクロフルイダイザー
M−110Y)で1200Kg/cm2 の条件で3回通
過して微細化結晶セルロースを得た。この微細化結晶セ
ルロースの平均粒径を表1に示す。
Example 1 Commercially available DP pulp was shredded, hydrolyzed in 10% hydrochloric acid at 105 ° C. for 20 minutes to obtain an acid-insoluble residue, which was filtered, washed and purified, and then spray-dried to give a water content of 4.7%.
Of crystalline cellulose was obtained. The solid content of this crystalline cellulose was adjusted to 10% by weight, and preliminary dispersion was performed at 25 ° C. for 1 minute at 15,000 rpm with an ace homogenizer (manufactured by Nippon Seiki Co., Ltd.). Average particle size of the pre-dispersion is 14.3 μm
Met. Then, the pre-dispersion liquid is mixed with a high-pressure crushing device (M
Microfluidizer M-110Y) manufactured by icrofluidics Co., Ltd. was passed 3 times under the condition of 1200 Kg / cm 2 to obtain micronized crystalline cellulose. Table 1 shows the average particle size of this micronized crystalline cellulose.

【0014】[0014]

【実施例2】結晶セルロース複合体「アビセル」〈登録
商標〉RC−N81(旭化成工業株式会社製)を固形分
10重量%とし、TKホモミキサー(特殊機化工業株式
会社製)で25℃において5000rpm、30分間の
予備分散を行った。予備分散液の平均粒径は12.5μ
mであった。続いて、この予備分散液を高圧破砕装置
(Microfluidics社製マイクロフルイダイ
ザーM−610型)で1200Kg/cm2 の条件で3
回通過して微細化結晶セルロース複合体を得た。このも
のの平均粒径を表1に示す。
Example 2 A crystalline cellulose composite "Avicel"<registeredtrademark> RC-N81 (manufactured by Asahi Kasei Kogyo Co., Ltd.) was used as a solid content of 10% by weight, and the mixture was mixed with a TK homomixer (manufactured by Tokushu Kika Kogyo Co., Ltd.) at 25 ° C. Preliminary dispersion was performed at 5000 rpm for 30 minutes. Average particle size of pre-dispersion is 12.5μ
It was m. Subsequently, this pre-dispersion liquid was applied to a high pressure crusher (Microfluidizer M-610 type manufactured by Microfluidics Co., Ltd.) under the condition of 1200 Kg / cm 2 for 3 times.
It was passed once to obtain a micronized crystalline cellulose composite. The average particle size of this product is shown in Table 1.

【0015】[0015]

【実施例3】結晶セルロース複合体「アビセル」〈登録
商標〉RC−N30(旭化成工業株式会社製)を固形分
10重量%とし、TKホモミキサー(特殊機化工業株式
会社製)で60℃において5000rpm、10分間の
予備分散を行った。予備分散液の平均粒径は10.0μ
mであった。続いて、この予備分散液を高圧破砕装置
(ナノマイザー株式会社製ナノマイザーLA−31型)
で1200Kg/cm2の条件で3回通過して微細化結
晶セルロース複合体を得た。このものの平均粒径を表1
に示す。
Example 3 A crystalline cellulose composite “Avicel” <registered trademark> RC-N30 (manufactured by Asahi Kasei Kogyo Co., Ltd.) was used as a solid content of 10% by weight, and the solid content was 60 ° C. with a TK homomixer (manufactured by Tokushu Kika Kogyo Co., Ltd.). Preliminary dispersion was performed at 5000 rpm for 10 minutes. Average particle size of pre-dispersion is 10.0μ
It was m. Subsequently, this preliminary dispersion liquid was subjected to a high-pressure crushing device (Nanomizer LA-31 type manufactured by Nanomizer Co., Ltd.).
At 1200 Kg / cm 2 for 3 times to obtain a micronized crystalline cellulose composite. Table 1 shows the average particle size of this product.
Shown in.

【0016】[0016]

【比較例1】特公昭62−30220、実施例1の方法
に従って、結晶セルロース「アビセル」〈登録商標〉F
D−101の均質化処理を行った。この時FD−101
を固形分2重量%とし、TKホモミキサー(特殊機化工
業株式会社製)で25℃において5000rpm、10
分間の予備分散を行った。予備分散液の平均粒径は2
6.1μmであった。続いて高圧用均質化装置(ゴーリ
ンホモジナイザー:15M−8TA)を用いて液温25
℃で仕込み、560Kg/cm2 の条件で3回通過で均
質化処理を行った。得られた均質化結晶セルロースの平
均粒径を表1に示す。
Comparative Example 1 Crystalline cellulose "Avicel"<registeredtrademark> F according to the method of JP-B-62-30220, Example 1.
D-101 was homogenized. At this time FD-101
To a solid content of 2% by weight and 5,000 rpm at 25 ° C. with a TK homomixer (manufactured by Tokushu Kika Kogyo Co., Ltd.)
Preliminary dispersion for 1 minute was performed. The average particle size of the predispersion is 2
It was 6.1 μm. Then, using a homogenizer for high pressure (Gorlin homogenizer: 15M-8TA), the liquid temperature was adjusted to 25.
The mixture was charged at 0 ° C. and homogenized by three passes under the condition of 560 Kg / cm 2 . The average particle size of the obtained homogenized crystalline cellulose is shown in Table 1.

【0017】[0017]

【試験例1】粒子の形状を顕微鏡によって観察した結
果、実施例1〜3のサンプルは丸みのある形状を示す。
これに対して比較例1のサンプルはやや丸みがあるが粗
大な粒子である。これらのサンプルについて口中及び指
による官能テストを行った結果、本発明の方法で得られ
る微細化セルロースはざらつきのない滑らかなものであ
った。これに対して比較例1のサンプルは肌理が粗く、
ざらつきが感じられ、粒子形状の観察結果と一致した。
[Test Example 1] As a result of observing the shape of particles with a microscope, the samples of Examples 1 to 3 show a rounded shape.
On the other hand, the sample of Comparative Example 1 is slightly rounded but has coarse particles. As a result of a sensory test with the mouth and fingers of these samples, the micronized cellulose obtained by the method of the present invention was smooth without roughness. On the other hand, the sample of Comparative Example 1 has a rough texture,
Roughness was felt, which was consistent with the observation result of the particle shape.

【0018】[0018]

【表1】 [Table 1]

【0019】[0019]

【発明の効果】本発明の微細化方法を用いることで、不
純物の混入がなく、セルロース系素材を実用的に効率よ
く微細化することが出来る。また、本発明の方法によっ
て得られる微細化セルロース系素材は、ざらつきがなく
滑らかな組織を有し、粘度の高いものが得られるという
特徴がある。このため、食品、医薬品、化粧品、塗料、
セラミックス、樹脂、触媒、その他工業用品等広い分野
において、懸濁安定剤、乳化安定剤、増粘安定剤、等の
安定剤、組織付与剤、クラウディー剤、研磨剤、食物繊
維、油脂代替物等として効果を発揮すると共にその使用
範囲を拡大することが可能となる。
EFFECTS OF THE INVENTION By using the micronization method of the present invention, the cellulosic material can be miniaturized practically and efficiently without inclusion of impurities. Further, the micronized cellulosic material obtained by the method of the present invention has a feature that it has a smooth texture without roughness and a high viscosity can be obtained. Therefore, food, pharmaceuticals, cosmetics, paints,
Stabilizers such as suspension stabilizers, emulsion stabilizers, thickening stabilizers, texture imparting agents, cloudy agents, abrasives, dietary fibers, oil substitutes in a wide range of fields such as ceramics, resins, catalysts and other industrial products. It is possible to expand the range of use as well as exhibiting the effect.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 セルロース系素材を、予備分散工程で固
形分1〜20重量%の水系分散液とし、次いで微細オリ
フィス内において圧力600Kg/cm2 以上の条件で
対面衝突させることを特徴とするセルロース系素材の微
細化方法。
1. A cellulose material characterized in that an aqueous dispersion liquid having a solid content of 1 to 20% by weight is prepared in a preliminary dispersion step, and then face-to-face collision is carried out in a fine orifice under a pressure of 600 kg / cm 2 or more. A method of refining system materials.
JP24496893A 1993-09-30 1993-09-30 Method for converting cellulose material into minute particle Withdrawn JPH07102074A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24496893A JPH07102074A (en) 1993-09-30 1993-09-30 Method for converting cellulose material into minute particle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24496893A JPH07102074A (en) 1993-09-30 1993-09-30 Method for converting cellulose material into minute particle

Publications (1)

Publication Number Publication Date
JPH07102074A true JPH07102074A (en) 1995-04-18

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JP24496893A Withdrawn JPH07102074A (en) 1993-09-30 1993-09-30 Method for converting cellulose material into minute particle

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001508116A (en) * 1997-01-21 2001-06-19 ヴオルフ・ヴアルスロデ・アクチエンゲゼルシヤフト Method for producing finely divided polysaccharide derivatives
CN1075514C (en) * 1997-10-13 2001-11-28 徐旗开 Method for producing microcrystalline cellulose by sulfating waste cotton velvet
WO2002036877A1 (en) * 2000-11-03 2002-05-10 Kemestrie Inc. Process for producing low dp microcrystalline cellulose

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001508116A (en) * 1997-01-21 2001-06-19 ヴオルフ・ヴアルスロデ・アクチエンゲゼルシヤフト Method for producing finely divided polysaccharide derivatives
CN1075514C (en) * 1997-10-13 2001-11-28 徐旗开 Method for producing microcrystalline cellulose by sulfating waste cotton velvet
WO2002036877A1 (en) * 2000-11-03 2002-05-10 Kemestrie Inc. Process for producing low dp microcrystalline cellulose
US6986828B2 (en) 2000-11-03 2006-01-17 Kemestrie Inc. Process for producing low DP microcrystalline cellulose

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