JPH05230477A - Coal slurry composition and its preparation - Google Patents

Coal slurry composition and its preparation

Info

Publication number
JPH05230477A
JPH05230477A JP3078192A JP3078192A JPH05230477A JP H05230477 A JPH05230477 A JP H05230477A JP 3078192 A JP3078192 A JP 3078192A JP 3078192 A JP3078192 A JP 3078192A JP H05230477 A JPH05230477 A JP H05230477A
Authority
JP
Japan
Prior art keywords
coal
cellulose
aqueous slurry
water
slurry
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
JP3078192A
Other languages
Japanese (ja)
Inventor
Eiji Ono
栄治 小野
Shigeru Yamanaka
茂 山中
Makoto Iwatsuki
誠 岩月
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.)
Ajinomoto Co Inc
Original Assignee
Ajinomoto Co Inc
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 Ajinomoto Co Inc filed Critical Ajinomoto Co Inc
Priority to JP3078192A priority Critical patent/JPH05230477A/en
Publication of JPH05230477A publication Critical patent/JPH05230477A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the title composition excellent in aqueous dispersion stability and fluidity by incorporating a specified amount of cellulose fibers as a dispersion stabilizer into a specified aqueous slurry of coal. CONSTITUTION:An aqueous slurry of coal, consisting of fine coal particles having a mean particle diameter of 200mum or smaller and water, which contains a dispersion stabilizer comprising cellulose fibers (e.g. microbial cellulose) in an amount of 0.005-0.04wt.%, in terms of dried cellulose fibers, based on the slurry.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は石炭水性スラリーの分散
安定性の改良に関する。
FIELD OF THE INVENTION This invention relates to improving the dispersion stability of coal aqueous slurries.

【0002】[0002]

【従来の技術】エネルギー源として広く利用されている
石油は、近い将来価格の高騰のみならず枯渇することも
予想される。代替エネルギー源としては、原子力、太陽
熱、バイオマスなどが考えられているが、安全性、価格
などの点で実用化までにはかなりの時間が必要と見られ
ている。
2. Description of the Related Art Petroleum, which is widely used as an energy source, is expected to run out in the near future as well as rising prices. Nuclear power, solar heat, biomass, etc. are considered as alternative energy sources, but it is considered that a considerable amount of time will be required before they can be put to practical use in terms of safety and price.

【0003】一方、石油の利用拡大の中で近年石炭が見
直されている。というのは、石炭は世界的に豊富に存在
すること、コストが安いことから、この石炭をエネルギ
ー資源として再利用することについて世界が見直そうと
している。近年石炭が固体であるために生じる低い輸送
効率、ボイラーへの供給作業性の悪さ、作業時の粉塵の
発生による爆発の危険性等の問題があったが、石炭水性
スラリーにすることでこれらの問題点を解決できる可能
性がある。このためには水分散安定性ならびに流動性の
良い石炭水性スラリーの製造法が望まれている。これま
で石炭水性スラリーの製造法について紛状石炭に水およ
び水溶性多糖もしくは界面活性剤を添加する方法(特開
昭58−96693)がある。
On the other hand, coal is being reviewed in recent years as the use of petroleum is expanded. Because of the abundance of coal in the world and the low cost, the world is trying to reconsider the reuse of this coal as an energy resource. In recent years, there were problems such as low transportation efficiency caused by the solid state of coal, poor workability of supplying to the boiler, risk of explosion due to generation of dust during work, etc. It may be possible to solve the problem. For this purpose, a method for producing a coal aqueous slurry having good water dispersion stability and fluidity is desired. Heretofore, as a method for producing an aqueous coal slurry, there has been a method in which water and a water-soluble polysaccharide or a surfactant are added to powder coal (JP-A-58-969693).

【0004】一般に石炭粒子は微細であればあるほど水
分散性が大きくなることが知られている。即ち、平均粒
径 200μm以下の微細石炭を用いて60%以上の水溶液濃
度の石炭水性スラリーは得られるが、その石炭水性スラ
リーには流動性は殆どなく、したがってパイプ輸送など
に供することができない。
It is generally known that the finer the coal particles, the greater the water dispersibility. That is, although a coal aqueous slurry having an aqueous solution concentration of 60% or more can be obtained by using fine coal having an average particle size of 200 μm or less, the coal aqueous slurry has almost no fluidity and therefore cannot be used for pipe transportation and the like.

【0005】一方、水溶液濃度を40〜50%に調製し、流
動性をある程度付与した石炭水性スラリーは、短時間で
石炭粒子の沈澱が生じるか、あるいは石炭粒子の固化が
生じてしまう。このような現象が起こると輸送中のパイ
プ内に石炭粒子が沈澱し、輸送効率が低下すると共にパ
イプの目詰まりの原因となる。これらのことから、流動
性のもった石炭水性スラリーの調製法が望まれている。
On the other hand, in an aqueous coal slurry prepared by adjusting the concentration of the aqueous solution to 40 to 50% and imparting fluidity to some extent, coal particles are precipitated in a short time or coal particles are solidified. When such a phenomenon occurs, coal particles settle in the pipe during transportation, which lowers transportation efficiency and causes clogging of the pipe. From these things, the preparation method of the coal aqueous slurry with fluidity is desired.

【0006】[0006]

【本発明が解決しようとする課題】本発明の目的は石炭
微粒子の水中での分散安定性が良く、かつ流動性の優れ
た石炭水性スラリー組成物及びその製造方法の提供する
ことにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a coal aqueous slurry composition having excellent dispersion stability of coal fine particles in water and excellent fluidity, and a method for producing the same.

【0007】[0007]

【課題を解決するための手段】上記課題を解決する為
に、本発明者等は鋭意検討を重ねた結果、石炭水性スラ
リーにセルロース性繊維を添加、混合することにより分
散安定性の優れた石炭水性スラリー組成物が得られるこ
とを見いだし本発明を完成するに至った。すなはち本発
明は平均粒径200μm以下の石炭微粒子と水を含有してな
る石炭水性スラリーにおいて、セルロース性繊維または
これを含有する水溶液もしくはゲルをセルロース繊維乾
燥物に換算し、該石炭水性スラリーに対し0.005な
いし0.04重量%分散安定剤として含有することを特
徴とする石炭スラリー組成物及びこれの製造法である。
以下に本発明を詳細に説明する。
[Means for Solving the Problems] In order to solve the above problems, the inventors of the present invention have conducted extensive studies, and as a result, by adding and mixing cellulosic fibers to a coal aqueous slurry, coal having excellent dispersion stability is obtained. It was found that an aqueous slurry composition was obtained, and the present invention was completed. In other words, the present invention is a coal aqueous slurry containing coal fine particles having an average particle size of 200 μm or less and water, in which a cellulosic fiber or an aqueous solution or gel containing the same is converted into a cellulose fiber dried product, and the coal aqueous slurry is obtained. On the other hand, a coal slurry composition containing 0.005 to 0.04% by weight of a dispersion stabilizer as a dispersion stabilizer and a method for producing the same.
The present invention will be described in detail below.

【0008】本発明に用いられるセルロース性繊維と
は、木材パルプ、木綿パルプ、麻パルプ、MFC(ダイ
セル化学工業株式会社製)等の植物由来のセルロースま
たは微生物が産生する微生物セルロースをいう。
The cellulosic fiber used in the present invention means plant-derived cellulose such as wood pulp, cotton pulp, hemp pulp, MFC (manufactured by Daicel Chemical Industries Ltd.) or microbial cellulose produced by microorganisms.

【0009】本発明に用いられる植物由来のセルロース
はトイレット・ペーパー、稲藁、木材パルプ等より得ら
れるセルロースを微細化して用いることができる。微細
化にあたっては、 植物性セルロースに5〜20倍量の水を
添加してワーリング・ブレンダーで10,000rmpで10〜
60分細粒化して用いることが好ましい。また微生物セル
ロースは微生物、特に酢酸菌を用いて産生されるセルロ
ースであり幅 10〜100nmの繊維状が好ましく用いられ
る。微生物セルロースは、生産された状態では、結晶性
および一軸配向性が非常に高いセルロースからなる非常
に細い(幅あるいは直径 100nm以下と言われる)リボン
状の繊維が複雑に絡み合ったネットワーク状の構造をし
ており、この構造物は、その中の空隙に多量の液体を含
んでおり、その外観はゲル状である。この微生物セルロ
ース構造物内の空隙に含まれている液体成分、例えば水
は、自由水として存在し、外力を加えると容易に絞り出
されてくる。このように結晶性が非常に高い多数のリボ
ン状の繊維により構成されているので湿状態のもので
も、引張等の外力にたいして耐える。微生物セルロース
は、植物起源の木綿、木材パルプ等のセルロースと一次
構造上は差がないが、上に述べたようなネットワークの
ようないわゆる高次構造は、植物起源のセルロースでは
見られない、微生物セルロース特有のものであり、それ
ゆえ、ゲル状であるにもかかわらず強度を持つこと等、
種々の性質を示す。また、シート状の微生物セルロース
は、結晶性の高いα−セルロースで構成されること、非
常に表面配向性が強いことの特徴を有している。
As the plant-derived cellulose used in the present invention, cellulose obtained from toilet paper, rice straw, wood pulp or the like can be used after being finely divided. For miniaturization, add 5 to 20 times the amount of water to vegetable cellulose and add 10 to 10 at 10,000 rpm with a Waring blender.
It is preferably used after being granulated for 60 minutes. The microbial cellulose is a cellulose produced by using microorganisms, particularly acetic acid bacteria, and a fibrous form having a width of 10 to 100 nm is preferably used. As produced, microbial cellulose has a network-like structure in which very thin (width or diameter of 100 nm or less) ribbon-shaped fibers made of cellulose with extremely high crystallinity and uniaxial orientation are intricately entangled. This structure contains a large amount of liquid in the voids therein, and its appearance is gel-like. The liquid component contained in the voids in the microbial cellulose structure, such as water, exists as free water and is easily squeezed out when an external force is applied. Since it is composed of a large number of ribbon-shaped fibers having extremely high crystallinity, it can withstand external forces such as tension even in a wet state. Microbial cellulose is not different in the primary structure from cellulose of plant-derived cotton, wood pulp, etc., but the so-called higher-order structure such as the network described above is not found in plant-derived cellulose. It is peculiar to cellulose, and therefore has strength despite being gelled.
It exhibits various properties. In addition, the sheet-shaped microbial cellulose is characterized in that it is composed of α-cellulose having high crystallinity and has a very strong surface orientation.

【0010】微生物セルロースは、セルロースおよびセ
ルロースを主鎖としたヘテロ多糖を含むものおよびβ、
α等のグルカンを含む。ヘテロ多糖の場合はセルロース
以外の構成成分として、マンノース、フラクトース、ガ
ラクトース、キシロース、アラビノース、ラムノース、
ウロン酸等の六炭糖、五炭糖および有機酸等を含む。こ
れらの多糖が単一物質として存在するセルロースもある
し、2種類以上の多糖が混在しているセルロースもあ
る。 このようなセルロースを生産する微生物は、特に
限定されないが、例えばアセトバクター・パスツリアヌ
ス(Acetobacter pasturianus)ATCC 10821、同アセチ(A.
aceti)、同ランセンス(A.ransens)、サルシナ・ベント
リクリ(Sarcina ventriculi)、バクテリウム・キシロイ
デス(Bacterium xyloides)、シュードモナス属細菌、ア
グロバクテリウム属細菌、リゾビウム属細菌等が挙げら
れる。
Microbial celluloses include those containing cellulose and heteropolysaccharides having cellulose as the main chain and β,
Including glucan such as α. In the case of a heteropolysaccharide, as constituent components other than cellulose, mannose, fructose, galactose, xylose, arabinose, rhamnose,
It includes hexoses such as uronic acid, pentoses and organic acids. There are celluloses in which these polysaccharides exist as a single substance, and there are celluloses in which two or more types of polysaccharides are mixed. Microorganisms that produce such cellulose are not particularly limited, for example, Acetobacter pasturianus ATCC 10821, aceti (A.
aceti), A. ransens, Sarcina ventriculi, Bacterium xyloides, Pseudomonas bacteria, Agrobacterium bacteria, Rhizobium bacteria and the like.

【0011】微生物セルロースの生成蓄積のためには、
上記の微生物を用いて、通常の細菌を培養する一般的な
方法に従えばよい。すなわち、炭素源、窒素源、無機塩
類、その他必要に応じて、アミノ酸、ビタミン等の有機
微量栄養素を含有する通常の栄養培地に添加し、20℃な
いし40℃に制御し培養を行えばよい。 このようにして
産生された微生物セルロースは、無洗浄でも使用できる
が、菌体あるいは培地成分を含むので、用途に応じて洗
浄することもできる。洗浄は、希アルカリ、希酸、有機
溶剤、熱水等を単独あるいは組み合わせて行えばよい。
For the production and accumulation of microbial cellulose,
A general method for culturing ordinary bacteria using the above-mentioned microorganism may be followed. That is, it may be added to a normal nutrient medium containing a carbon source, a nitrogen source, an inorganic salt, and other organic micronutrients such as amino acids and vitamins, if necessary, and controlled at 20 ° C to 40 ° C for culturing. The microbial cellulose produced in this manner can be used without washing, but since it contains bacterial cells or medium components, it can be washed depending on the application. The washing may be performed with a dilute alkali, a dilute acid, an organic solvent, hot water or the like alone or in combination.

【0012】洗浄後に得られた微生物セルロースのゲル
は、ワーリング・ブレンダーを用いて微生物セルロース
のゲルが繊維状になるまで微細化して使用すればよい。
即ち、石炭水性スラリーに添加する微生物セルロースの
微細化にあたって、水分98%の微生物セルロースのゲル
1cm角のもの10kgをワーリング・ブレンダーで10,0
00rpmで15〜30分が好ましい。
The microbial cellulose gel obtained after washing may be used by micronizing it using a Waring blender until the microbial cellulose gel becomes fibrous.
That is, when refining the microbial cellulose to be added to the coal aqueous slurry, 10 kg of a 1 cm square gel of microbial cellulose with a water content of 98% is used with a Waring blender for 10,0
15 to 30 minutes at 00 rpm is preferred.

【0013】本発明の石炭スラリー組成物の製造法は、
従来の石炭水性スラリーに乾燥状もしくは水溶性もしく
はゲル状のセルロース繊維を該分散水溶として添加し、
100〜500 rpmで20分〜 3時間ゆっくりと攪拌混合す
ることで好ましく調製できる。以下実施例に基づいて説
明する。
The method for producing the coal slurry composition of the present invention comprises:
A dry or water-soluble or gelled cellulose fiber is added to the conventional coal aqueous slurry as the dispersed water solution,
It can be preferably prepared by slowly stirring and mixing at 100 to 500 rpm for 20 minutes to 3 hours. A description will be given below based on examples.

【0014】[0014]

【実施例】【Example】

【0015】試験方法1 水の分散度試験 口径28mmのメスシリンダーに石炭スラリーまたは石
炭水性スラリーを100ml張り込み常温で静置し、粉
状石炭と水の境界面とから求めた。
Test Method 1 Water Dispersion Test 100 ml of coal slurry or coal aqueous slurry was placed in a graduated cylinder having a diameter of 28 mm and allowed to stand at room temperature, and it was determined from the interface between pulverized coal and water.

【0016】試験方法2 粘度試験 粘度計:東京計器株式会社、DVK−B型で摂氏20度
のもとで測定した。
Test Method 2 Viscosity Test Viscometer: Measured with a DVK-B type, Tokyo Keiki Co., Ltd. at 20 degrees Celsius.

【0017】石炭水性スラリーの調製 粒径 150μm以下の褐炭(ジーベンケミカル株式会社よ
り微紛炭として入手)140g を水60gに分散混合 500r
pmで30分間攪拌して調整した。
Preparation of Coal Aqueous Slurry 140 g of lignite coal (obtained as fine dust coal from G-Ben Chemical Co., Ltd.) having a particle size of 150 μm or less is dispersed and mixed in 60 g of water to 500 r.
It was adjusted by stirring at pm for 30 minutes.

【0018】微生物セルロースゲルの調製 微生物セルロースゲルをワーリング・ブレンダーを用い
て10,000rpmで15分間行い乾燥物換算で 2%になるよ
うに調製した。
Preparation of Microbial Cellulose Gel Microbial cellulose gel was prepared by using a Waring blender at 10,000 rpm for 15 minutes so as to be 2% in terms of dry matter.

【0019】[0019]

【実施例1−4】微生物セルロースゲルをワーリング・
ブレンダーで10,000rpmで15分間行い微細化したもの
を表1に示した量を石炭水性スラリーに添加した後、混
合機で 500rpm30分間混合し石炭スラリーを得た。こ
れを摂氏20度で所定時間放置したときの粘度および分離
度を測定し併せて表1に示した。
Examples 1-4: Warming microbial cellulose gel
The amount shown in Table 1 was added to the coal aqueous slurry in the amount shown in Table 1 after being refined by a blender at 10,000 rpm for 15 minutes, and then mixed with a mixer at 500 rpm for 30 minutes to obtain a coal slurry. The viscosity and the degree of separation when this was allowed to stand at 20 degrees Celsius for a predetermined time were measured and are also shown in Table 1.

【0020】[0020]

【表1】 [Table 1]

【0021】[0021]

【比較例1−4】石炭水性スラリーまたはこれに表1に
示したように微生物セルロース、ポリオキシエチレンラ
ウリルエーテル(LEO)、リグニンスルホン酸ナトリ
ウム(LAS)を各々添加した後、これを摂氏20度で
所定時間放置したときの粘度および分離度を測定し併せ
て表1に示した。
[Comparative Example 1-4] Coal aqueous slurry or microbial cellulose, polyoxyethylene lauryl ether (LEO), and sodium lignin sulfonate (LAS) were added to each as shown in Table 1 and then added to 20 degrees Celsius. The viscosity and the degree of separation when left to stand for a predetermined time were measured and shown in Table 1.

【0022】[0022]

【実施例5−9】石炭水性スラリーにMFC(ダイセル
化学工業(株)製、品番409051、セルロース2
%、水分98%)は無処理のもの、木材クズ31gWO
水道水980gに入れてワーリング・ブレンダーで1
0,000rpmで30分間微細化したもの、トイレット
ペーパーは約1cm角に切断したトイレットペーパー2
2gを水道水980gに入れてワーリング・ブレンダー
で10,000rpmで15分間微細化したもの、微生
物セルロースは約1cm角に切断した微生物セルロート
ナゲル500gを水道水500gに入れてワーリング・
ブレンダーで10,000rpmDE15分間微細化し
たものを乾燥物に換算して表2に示したセルロースを表
2に示した量を添加した後、混合機で 500rpm3
0分間混合し石炭スラリーを得た。これを摂氏20度で
所定時間静置し、この状態での粘度および分離度を測
定し表2に示した。
[Example 5-9] MFC (manufactured by Daicel Chemical Industries, Ltd., product number 409051, cellulose 2 was added to an aqueous coal slurry.
%, Moisture 98%) is untreated, wood scrap 31g WO
Put it in 980 g of tap water and use a Waring Blender 1
Toilet paper finely cut at 30,000 rpm for 30 minutes, toilet paper cut into about 1 cm square 2
2 g of tap water was put into 980 g of water and finely divided by a Waring blender at 10,000 rpm for 15 minutes.
After converting the finely divided product with a blender at 10,000 rpm for 15 minutes into a dried product, and adding the cellulose shown in Table 2 in the amount shown in Table 2, 500 rpm3 with a mixer.
The mixture was mixed for 0 minutes to obtain a coal slurry. This was allowed to stand at 20 ° C. for a predetermined time, and the viscosity and the degree of separation in this state were measured and shown in Table 2.

【0023】[0023]

【表2】 [Table 2]

【0024】[0024]

【比較例5−6】石炭水性スラリー及びこれにLASを
表2に示した量を添加した後、混合機で500rpm3
0分間混合し石炭水性スラリーを得た。これを摂氏20
度で所定時間静置し、この状態での粘度および分離度を
測定し併せて表2に示した。
[Comparative Example 5-6] Aqueous coal slurry and LAS in the amounts shown in Table 2 were added, and then 500 rpm3 with a mixer.
The mixture was mixed for 0 minutes to obtain a coal aqueous slurry. 20 degrees Celsius
The test piece was allowed to stand for a predetermined time at a temperature, and the viscosity and the degree of separation in this state were measured and are also shown in Table 2.

【0025】[0025]

【効果】本発明の石炭スラリー組成物及び製造法は、従
来法に比べて少量のセルロースの添加で水分散安定性、
流動性に優れている有用な技術である。
[Effect] The coal slurry composition and the manufacturing method of the present invention are stable in water dispersion by adding a small amount of cellulose as compared with the conventional method.
This is a useful technique with excellent fluidity.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】平均粒径200μm以下の石炭微粒子と水を含
有してなる石炭水性スラリーにおいて、セルロース性繊
維をセルロース繊維乾燥物に換算し、該石炭水性スラリ
ーに対し0.005ないし0.04重量%分散安定剤と
して含有することを特徴とする石炭スラリー組成物。
1. A coal aqueous slurry containing fine coal particles having an average particle size of 200 μm or less and water, in which cellulosic fibers are converted into a dried cellulose fiber product and 0.005 to 0.04 relative to the coal aqueous slurry. A coal slurry composition, characterized by containing as a wt% dispersion stabilizer.
【請求項2】平均粒径200μm以下の石炭微粒子と水を含
有してなる石炭水性スラリーにセルロース性繊維をセル
ロース繊維乾燥物に換算し、該石炭水性スラリーに対し
0.005ないし0.04重量%分散安定剤として添加
することを特徴とする石炭スラリー組成物の製造法。
2. A coal aqueous slurry containing coal fine particles having an average particle diameter of 200 μm or less and water, in which cellulosic fibers are converted into a dried cellulose fiber product, and 0.005 to 0.04 weight of the coal aqueous slurry is obtained. % A dispersion stabilizer is added, and the manufacturing method of the coal slurry composition characterized by the above-mentioned.
JP3078192A 1992-02-18 1992-02-18 Coal slurry composition and its preparation Pending JPH05230477A (en)

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Application Number Priority Date Filing Date Title
JP3078192A JPH05230477A (en) 1992-02-18 1992-02-18 Coal slurry composition and its preparation

Publications (1)

Publication Number Publication Date
JPH05230477A true JPH05230477A (en) 1993-09-07

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Country Status (1)

Country Link
JP (1) JPH05230477A (en)

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