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JP2017008175A - Manufacturing method of dry solid article of cellulose nanofiber - Google Patents

Manufacturing method of dry solid article of cellulose nanofiber Download PDF

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JP2017008175A
JP2017008175A JP2015123837A JP2015123837A JP2017008175A JP 2017008175 A JP2017008175 A JP 2017008175A JP 2015123837 A JP2015123837 A JP 2015123837A JP 2015123837 A JP2015123837 A JP 2015123837A JP 2017008175 A JP2017008175 A JP 2017008175A
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cnf
drying
dry solid
cellulose nanofiber
cellulose
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JP6727531B2 (en
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丈史 中谷
Takeshi Nakatani
丈史 中谷
木村 浩司
Koji Kimura
浩司 木村
伸治 佐藤
Shinji Sato
伸治 佐藤
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Nippon Paper Industries Co Ltd
Jujo Paper Co Ltd
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Nippon Paper Industries Co Ltd
Jujo Paper Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a manufacturing method of a dry solid article of a cellulose nanofiber having properties that change in physical properties such as viscosity and transparency of a cellulose nanofiber dispersion, where the dry solid article of the cellulose nanofiber by drying a stably dispersed cellulose nanofiber dispersion is redispersed, is less compared to the cellulose nanofiber dispersion before drying (redispersion property).SOLUTION: There is provided a manufacturing method of dry solid article of a cellular nanofiber including adjusting an aqueous suspension for the cellular nanofiber to pH of 9 to 11 and dehydrating and drying it.SELECTED DRAWING: None

Description

本発明は、セルロースナノファイバーの乾燥固形物の製造方法に関する。   The present invention relates to a method for producing a dry solid of cellulose nanofiber.

セルロースナノファイバー(CNF)は、水系分散性に優れている約4〜数百nm程度の大きさの微細繊維であり、食品、化粧品、医療品又は塗料等の粘度の保持、食品原料生地の強化、水分の保持、食品安定性向上、低カロリー添加物又は乳化安定化助剤として利用されていることが期待されている。   Cellulose nanofiber (CNF) is a fine fiber with a size of about 4 to several hundreds of nanometers, which is excellent in water-based dispersibility, maintains the viscosity of food, cosmetics, medical products, paints, etc., and strengthens food raw material dough It is expected to be used as a moisture retention, food stability improvement, low calorie additive or emulsion stabilization aid.

水に分散している状態(湿潤状態)のCNFを乾燥させた固形物は、微細なセルロース繊維間に水素結合が形成されるため、この乾燥固形物に水を加えても、乾燥前(湿潤状態)の溶解性、分散性、沈降度、及び粘度などの諸特性が復元しない。このため、CNFは水に分散している状態(湿潤状態)で製造され、乾燥させずに湿潤状態のままで各種用途に使用されることが通常行われている。   Since solids obtained by drying CNF in a state dispersed in water (wet state) form hydrogen bonds between fine cellulose fibers, even if water is added to the dried solids, Various properties such as solubility, dispersibility, sedimentation degree, and viscosity of the state are not restored. For this reason, CNF is usually produced in a state of being dispersed in water (wet state) and used in various applications in a wet state without being dried.

しかしながら、この湿潤状態のCNFを安定させるためには、CNFに対して数倍〜数百倍の重量の水が必要であり、保存スペースの確保、保存及び輸送コストの増大等、種々の問題点がある。   However, in order to stabilize this wet CNF, water several times to several hundred times the weight of CNF is required, and there are various problems such as securing storage space, increasing storage and transportation costs. There is.

この問題を解決する手段として、凍結乾燥法や臨界点乾燥法などの他に、有機溶剤で置換処理した後に乾燥する方法(特許文献1)などが提案されている。   As means for solving this problem, in addition to freeze-drying methods, critical point drying methods, and the like, a method of performing a substitution treatment with an organic solvent and then drying (Patent Document 1) has been proposed.

特開平6−233691号Japanese Patent Laid-Open No. 6-233691

しかしながら、CNFを凍結乾燥した場合、膨大なエネルギーが必要になるとともに、条件によってはCNFの微細繊維間の水が凍結される際に、微細なセルロース繊維間の空隙よりも大きな氷晶の成長がおこり、CNFの微細繊維同士の会合が発生するなどの問題が発生する。   However, when CNF is freeze-dried, enormous energy is required, and depending on conditions, when water between fine fibers of CNF is frozen, ice crystals larger than the voids between fine cellulose fibers grow. As a result, problems such as the association of fine CNF fibers occur.

また、CNFの微細繊維の間の空隙は非常に小さい上に、微細なセルロース繊維の表面には多量の水が水和しているため、溶剤置換によって乾燥させるには、多量の溶剤と時間が必要となる。さらに、溶剤に置換することができない水分が内在してしまうために、溶剤の乾燥過程でCNFの微細なセルロース繊維の表面同士が水素結合によって強固に結合してしまう。このため、もとのCNFの状態に復元することは困難である。   In addition, since the gap between the fine fibers of CNF is very small and a large amount of water is hydrated on the surface of the fine cellulose fiber, a large amount of solvent and time are required for drying by solvent replacement. Necessary. Furthermore, since moisture that cannot be replaced by the solvent is inherent, the surfaces of the fine cellulose fibers of CNF are strongly bonded to each other by hydrogen bonding in the course of drying the solvent. For this reason, it is difficult to restore the original CNF state.

そこで、本発明は、安定に分散されているCNF分散液を乾燥させたCNF乾燥固形物を水に再分散したCNF分散液の粘度、透明性などの物性が、乾燥前のCNF分散液と比較して変化が少ない特性(再分散性)を有するCNFの乾燥固形物の製造方法を提供することを目的とする。
Therefore, in the present invention, physical properties such as viscosity and transparency of a CNF dispersion obtained by re-dispersing a CNF dry solid obtained by drying a stably dispersed CNF dispersion in water are compared with those of the CNF dispersion before drying. It is an object of the present invention to provide a method for producing a dry solid of CNF having characteristics (redispersibility) with little change.

本発明は、下記の[1]〜[2]を提供する。
[1] セルロースナノファイバーの水性懸濁液のpHを9〜11に調整した後に、脱水・乾燥させることを特徴とするセルロースナノファイバーの乾燥固形物の製造方法。
[2] [1]に記載の方法により製造されるセルロースナノファイバーの乾燥固形物。
The present invention provides the following [1] to [2].
[1] A method for producing a dried solid of cellulose nanofibers, wherein the pH of the aqueous suspension of cellulose nanofibers is adjusted to 9 to 11, followed by dehydration and drying.
[2] A dry solid of cellulose nanofibers produced by the method according to [1].

本発明によれば、安定に分散されているCNF分散液を乾燥させたCNF乾燥固形物を水に再分散したCNF分散液の粘度、透明性などの物性が、乾燥前のCNF分散液と比較して変化が少ない特性(再分散性)を有するCNFの乾燥固形物の製造方法を提供することができる。   According to the present invention, physical properties such as viscosity and transparency of a CNF dispersion obtained by re-dispersing a CNF dry solid obtained by drying a stably dispersed CNF dispersion in water are compared with those of a CNF dispersion before drying. Thus, a method for producing a dry solid of CNF having characteristics (redispersibility) with little change can be provided.

本発明は、セルロースナノファイバーの水性懸濁液のpHを9〜11に調整した後に、脱水・乾燥させることで得られるセルロースナノファイバーの乾燥固形物は、その固形物を水に分散させた湿潤状態のCNFが、乾燥前の湿潤状態のCNFの溶解性、分散性、沈降度、及び粘度などの諸特性の変化が少ない特性(再分散性)のを有する。   In the present invention, after the pH of the aqueous suspension of cellulose nanofibers is adjusted to 9 to 11, the dry solid matter of cellulose nanofibers obtained by dehydration and drying is wet obtained by dispersing the solid matter in water. The CNF in the state has characteristics (redispersibility) with little change in properties such as solubility, dispersibility, sedimentation degree, and viscosity of the wet CNF before drying.

本発明のCNFの乾燥固形物が優れた再分散性を発現する理由は明らかではないが、乾燥前のCNFの水分散液のアルカリ領域(pH9〜11)に調整することで、乾燥時による酸劣化、CNFの凝集を抑制されていると推測される。ただし、pHが高すぎると、アルカリによる劣化、CNFの結晶構造の変化の恐れがある。   The reason why the dry solid of CNF of the present invention exhibits excellent redispersibility is not clear, but by adjusting to the alkaline region (pH 9 to 11) of the aqueous CNF dispersion before drying, the acid during drying can be adjusted. It is estimated that deterioration and aggregation of CNF are suppressed. However, if the pH is too high, there is a risk of deterioration due to alkali and a change in the crystal structure of CNF.

なお、本発明において、セルロースナノファイバーの乾燥固形物とは、水分量が12重量%以下になるように脱水・乾燥したセルロースナノファイバーを意味する。   In addition, in this invention, the dry solid substance of a cellulose nanofiber means the cellulose nanofiber which dehydrated and dried so that the moisture content might be 12 weight% or less.

(pH調整剤)
本発明において、セルロースナノファイバーの水性懸濁液のpHを9〜11に調整するために用いる薬品は特に限定されるものではなく、水酸化ナトリウム、水酸化カリウム、水酸化カルシウム、水酸化バリウム、水酸化マグネシウム、アンモニア、水酸化銅、水酸化アルミニウム、水酸化鉄、水酸化アンモニウム、炭酸水素ナトリウム、炭酸水素カリウム、炭酸ナトリウム、炭酸カルシウム、炭酸マグネシウム、酸化マグネシウムから選ばれた塩基性無機化合物、あるいはアルギニン、リジン、ヒスチジン及びオルニチンから選ばれた塩基性有機化合物などを例示することができる。
(PH adjuster)
In the present invention, the chemical used for adjusting the pH of the aqueous suspension of cellulose nanofibers to 9 to 11 is not particularly limited, and sodium hydroxide, potassium hydroxide, calcium hydroxide, barium hydroxide, A basic inorganic compound selected from magnesium hydroxide, ammonia, copper hydroxide, aluminum hydroxide, iron hydroxide, ammonium hydroxide, sodium hydrogen carbonate, potassium hydrogen carbonate, sodium carbonate, calcium carbonate, magnesium carbonate, magnesium oxide, Alternatively, a basic organic compound selected from arginine, lysine, histidine and ornithine can be exemplified.

(セルロースナノファイバー)
本発明において、セルロースナノファイバー(CNF)は、繊維幅が4〜500nm程度、アスペクト比が100以上の微細繊維であり、パルプなどのセルロース原料を解繊することによって得ることができる。
(Cellulose nanofiber)
In the present invention, the cellulose nanofiber (CNF) is a fine fiber having a fiber width of about 4 to 500 nm and an aspect ratio of 100 or more, and can be obtained by fibrillating a cellulose raw material such as pulp.

(セルロース原料)
本発明において、セルロース原料としては、植物(例えば、木材、竹、麻、ジュート、ケナフ、農地残廃物、布、パルプ(針葉樹未漂白クラフトパルプ(NUKP)、針葉樹漂
白クラフトパルプ(NBKP)、広葉樹未漂白クラフトパルプ(LUKP)、広葉樹漂白クラフトパルプ(LBKP)、針葉樹未漂白サルファイトパルプ(NUSP)、針葉樹漂白サルファイトパルプ(NBSP)サーモメカニカルパルプ(TMP)、再生パルプ、古紙等)、動物(例えばホヤ類)、藻類、微生物(例えば酢酸菌(アセトバクター))、微生物産生物等を起源とするものが知られており、本発明ではそのいずれも使用できる。好ましくは植物又は微生物由来のセルロース繊維であり、より好ましくは植物由来のセルロース繊維である。
(Cellulose raw material)
In the present invention, as the cellulose raw material, plants (for example, wood, bamboo, hemp, jute, kenaf, farmland waste, cloth, pulp (coniferous unbleached kraft pulp (NUKP), coniferous bleached kraft pulp (NBKP), hardwood not yet) Bleached kraft pulp (LUKP), hardwood bleached kraft pulp (LBKP), softwood unbleached sulfite pulp (NUSP), softwood bleached sulfite pulp (NBSP) thermomechanical pulp (TMP), recycled pulp, waste paper, etc.), animals (for example, Squirrels), algae, microorganisms (for example, acetic acid bacteria (Acetobacter)), microbial products, etc. are known, and any of them can be used in the present invention, preferably cellulose fibers derived from plants or microorganisms More preferably, it is a cellulose fiber derived from a plant.

(解繊)
本発明において、解繊する装置は特に限定されないが、高速回転式、コロイドミル式、高圧式、ロールミル式、超音波式などの装置を用いて前記水分散体に強力なせん断力を印加することが好ましい。特に、効率よく解繊するには、前記水分散体に50MPa以上の圧力を印加し、かつ強力なせん断力を印加できる湿式の高圧または超高圧ホモジナイザを用いることが好ましい。前記圧力は、より好ましくは100MPa以上であり、さらに好ましくは140MPa以上である。また、高圧ホモジナイザでの解繊・分散処理に先立って、必要に応じて、高速せん断ミキサーなどの公知の混合、攪拌、乳化、分散装置を用いて、上記のCNFに予備処理を施すことも可能である。
(Defibration)
In the present invention, an apparatus for defibrating is not particularly limited, but a strong shearing force is applied to the aqueous dispersion using an apparatus such as a high-speed rotation type, a colloid mill type, a high pressure type, a roll mill type, or an ultrasonic type. Is preferred. In particular, for efficient defibration, it is preferable to use a wet high-pressure or ultrahigh-pressure homogenizer that can apply a pressure of 50 MPa or more to the aqueous dispersion and can apply a strong shearing force. The pressure is more preferably 100 MPa or more, and further preferably 140 MPa or more. In addition, prior to defibration / dispersion with a high-pressure homogenizer, it is possible to pre-treat the CNF using a known mixing, stirring, emulsifying, and dispersing device such as a high-speed shear mixer as necessary. It is.

(乾燥方法)
本発明方法において、脱水・乾燥方法としては、従来公知のものであれば良く、例えば、スプレイドライ、圧搾、風乾、熱風乾燥、及び真空乾燥を挙げることができる。本発明方法で具体的に用いる乾燥装置の例としては、以下のようなものである。すなわち、連続式のトンネル乾燥装置、バンド乾燥装置、縦型乾燥装置、垂直ターボ乾燥装置、多重段円板乾燥装置、通気乾燥装置、回転乾燥装置、気流乾燥装置、スプレードライヤ乾燥装置、噴霧乾燥装置、円筒乾燥装置、ドラム乾燥装置、スクリューコンベア乾燥装置、加熱管付回転乾燥装置、振動輸送乾燥装置等、回分式の箱型乾燥装置、通気乾燥装置、真空箱型乾燥装置、及び撹拌乾燥装置等の乾燥装置を単独で又は2つ以上組み合わせて用いることができる。
(Drying method)
In the method of the present invention, any conventional dehydration / drying method may be used, and examples include spray drying, pressing, air drying, hot air drying, and vacuum drying. Examples of the drying apparatus specifically used in the method of the present invention are as follows. That is, continuous tunnel dryer, band dryer, vertical dryer, vertical turbo dryer, multi-stage disk dryer, aeration dryer, rotary dryer, air dryer, spray dryer dryer, spray dryer , Cylindrical dryers, drum dryers, screw conveyor dryers, rotary dryers with heating tubes, vibration transport dryers, batch-type box dryers, aeration dryers, vacuum box dryers, stirring dryers, etc. These drying apparatuses can be used alone or in combination of two or more.

これらの中でも、ドラム乾燥装置を用いることが、均一に被乾燥物に熱エネルギーを直接供給するためエネルギー効率の点から好ましい。また、乾燥前の水を含んだセルロースナノファイバーに於いて、乾燥処理効率を上げるために、水分をできるだけ少なくする前濃縮処理を行うことが通常行われるが、この際液粘度の上昇が乾燥処理の障害となる。これに対して、ドラムにブレードやダイ等により薄膜を形成させて乾燥させる事により、乾燥処理をより効率的に、均一に短時間で行うことができる。更に、ドラム乾燥装置は必要以上に熱を加えずに、直ちに乾燥物を回収できる点からも好ましい。   Among these, it is preferable to use a drum drying apparatus from the viewpoint of energy efficiency because the heat energy is uniformly supplied directly to an object to be dried. In addition, in order to increase the efficiency of the drying process for cellulose nanofibers containing water before drying, a pre-concentration process that reduces the amount of water as much as possible is usually performed. It becomes an obstacle. On the other hand, a drying process can be performed more efficiently and uniformly in a short time by forming a thin film on a drum with a blade, a die or the like and drying it. Furthermore, the drum dryer is preferable from the viewpoint that the dried product can be recovered immediately without applying more heat than necessary.

以下、実施例を挙げて本発明をさらに詳細に説明するが、本発明はこれらに限定される
ものではない。
<CNFの製造>
針葉樹由来の漂白済み未叩解クラフトパルプ(白色度85%)を水で1.0%(w/v)に調整し、超高圧ホモジナイザー(20℃、150Mpa)で50回処理して、セルロースナノファイバー分散液を得た。得られた繊維は、平均繊維径が60nm、アスペクト比が110であった。
Hereinafter, although an example is given and the present invention is explained still in detail, the present invention is not limited to these.
<Manufacturing CNF>
Cellulose nanofiber A dispersion was obtained. The obtained fiber had an average fiber diameter of 60 nm and an aspect ratio of 110.

(平均繊維径、アスペクト比の測定方法)
セルロース繊維の平均繊維径および平均繊維長は、電界放出型走査電子顕微鏡(FE−SEM)を用いて、ランダムに選んだ200本の繊維について解析した。なおアスペクト比は下記の式により算出した:
アスペクト比=平均繊維長/平均繊維径
(Measuring method of average fiber diameter and aspect ratio)
The average fiber diameter and average fiber length of the cellulose fibers were analyzed for 200 randomly selected fibers using a field emission scanning electron microscope (FE-SEM). The aspect ratio was calculated by the following formula:
Aspect ratio = average fiber length / average fiber diameter

<実施例1>
上記CNF(平均繊維径:60nm、アスペクト比:110)の0.7質量%水性懸濁液をTKホモミキサー(12,000rpm)で60分間攪拌した。この水性懸濁液に、水酸化ナトリウム水溶液0.5%を加え、pHを9に調整した後、蒸気圧力0.5MPa.G、ドラム回転数2rpmのドラム乾燥機D0303(カツラギ工業)で乾燥し、水分量5重量%のCNFの乾燥固形物を得た。
<Example 1>
A 0.7% by mass aqueous suspension of the above CNF (average fiber diameter: 60 nm, aspect ratio: 110) was stirred with a TK homomixer (12,000 rpm) for 60 minutes. To this aqueous suspension, 0.5% aqueous sodium hydroxide solution was added to adjust the pH to 9, and then the vapor pressure was 0.5 MPa. G, and dried with a drum dryer D0303 (Katsuragi Industry Co., Ltd.) with a drum rotation speed of 2 rpm, to obtain a dry solid of CNF having a water content of 5% by weight.

次に、上記で得られた乾燥固形物に0.7質量%水性懸濁液になるように水を添加し、TKホモミキサー(12,000rpm)を用いて60分間攪拌し、CNFを再分散した水性懸濁液を得た。   Next, water is added to the dried solid obtained above so that it becomes a 0.7% by mass aqueous suspension, and the mixture is stirred for 60 minutes using a TK homomixer (12,000 rpm) to redisperse CNF. An aqueous suspension was obtained.

(B型粘度の測定)
CNF(固形分0.7%、25℃)のB型粘度を測定した。なおB型粘度の測定条件は、回転数30rpm、3分とした。
(透明度の測定)
CNF分散液(固形分0.1%)の透明度(660nm 光の透過率)をUV分光光度計 U−3000(日立ハイテク)を用いて測定した。
(Measurement of B type viscosity)
The B-type viscosity of CNF (solid content 0.7%, 25 ° C.) was measured. The measurement conditions for the B-type viscosity were 30 rpm and 3 minutes.
(Measurement of transparency)
The transparency (660 nm light transmittance) of the CNF dispersion (solid content 0.1%) was measured using a UV spectrophotometer U-3000 (Hitachi High-Tech).

(復元率の評価)
B型粘度、透明度の復元率は以下の式で算出した。
復元率(%)=(乾燥前の粘度あるいは透明度)/(再分散後の粘度あるいは透明度)×100
(Evaluation of restoration rate)
The restoration rate of B type viscosity and transparency was calculated by the following formula.
Restoration rate (%) = (viscosity or transparency before drying) / (viscosity or transparency after redispersion) × 100

<実施例2>
pHを11に調整以外は実施例1と同様にして行った。
<Example 2>
The procedure was the same as in Example 1 except that the pH was adjusted to 11.

<比較例1>
pH調整を行わなかった以外は実施例1と同様にして行ったが、水性懸濁液にCNFの凝集物の沈降物が著しく発生したため、評価することができなかった。
<Comparative Example 1>
The procedure was the same as in Example 1 except that the pH was not adjusted. However, since a precipitate of CNF aggregates was remarkably generated in the aqueous suspension, it could not be evaluated.

<比較例2>
pHを8に調整以外は実施例1と同様にして行ったが、水性懸濁液にCNFの凝集物の沈降物が著しく発生したため、評価することができなかった。
<Comparative example 2>
The procedure was the same as in Example 1 except that the pH was adjusted to 8. However, the precipitation of CNF aggregates was remarkably generated in the aqueous suspension, and thus the evaluation could not be performed.

Figure 2017008175
Figure 2017008175

Claims (2)

セルロースナノファイバーの水性懸濁液のpHを9〜11に調整した後に、脱水及び乾燥させることを特徴とするセルロースナノファイバーの乾燥固形物の製造方法。   A method for producing a dried solid of cellulose nanofibers, wherein the pH of an aqueous suspension of cellulose nanofibers is adjusted to 9 to 11, followed by dehydration and drying. 請求項1に記載の方法により製造されるセルロースナノファイバーの乾燥固形物。 The dry solid substance of the cellulose nanofiber manufactured by the method of Claim 1.
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